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Impacts of Ocean Acidification on Shelled Pteropods in the<br />

Southern Ocean<br />

Term Paper in Biogeochemistry and Pollutant Dynamics<br />

Author:<br />

Tutor:<br />

Nanina Blank * Prof. Dr. Nicolas Gruber **<br />

Handed in: June 22 nd 2007<br />

Reviewed: November 23 rd 2007<br />

*<br />

Opfikonstr. 49, 8050 Zürich, nblank@student.ethz.ch<br />

** <strong>Environmental</strong> <strong>Physics</strong> (<strong>UP</strong>); Institute of Biogeochemistry and Pollutant Dynamics (IBP),<br />

Departement of <strong>Environmental</strong> Sciences (D-UWIS) at the <strong>ETH</strong> Zurich,<br />

nicolas.gruber@env.ethz.ch<br />

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Abstract<br />

Roughly a third of the anthropogenic carbon dioxide emitted into the atmosphere has been taken up<br />

by the ocean (Sabine et al., 2004), where it changes both the biological and geochemical processes.<br />

The carbon dioxide makes the sea water more acidic and shifts the chemical equilibrium towards<br />

smaller carbonate ion concentrations. The Southern Ocean is naturally poor in carbonate ions due to<br />

its position in the global ocean circulation system and is thus especially vulnerable to changes<br />

induced through carbon dioxide uptake (Sarmiento and Gruber, 2006). In this ecosystem planktonic<br />

shelled mollusc, such as pteropods, are abundant. They use carbonate ions and dissolved calcium to<br />

form aragonite for their shells. For them to be able to make those shells the water has to be<br />

supersaturated with respect to carbonate. In general, surface waters have higher carbonate ion<br />

concentrations and are thus supersaturated with respect to aragonite, while the deep sea has lower<br />

carbonate ion concentrations and is thus undersaturated. As the ocean takes up anthropogenic<br />

carbon dioxide, the saturated part of the water column shrinks. According to simulations of the<br />

IS92a scenario (IPCC, 2000) the whole water column of the Southern Ocean will become<br />

undersaturated with regard to aragonite by the end of this century (Orr et al., 2005). That poses a<br />

great threat to the pteropods, because their shells show extensive erosion when exposed to<br />

undersaturated conditions (Orr et al., 2005; Feely et al., 2004) and it is not known, whether they can<br />

maintain their calcification. The exact pH dependence of aragonite calcification in pteropods is not<br />

known, but if they have a similar sensitivity as other aragonite calcifying organisms, ocean<br />

acidification will have an adverse if not fatal impact. The disappearance of pteropods from the<br />

Southern Ocean might have a severe impact on the ecosystem, especially on the organisms relying<br />

heavily on pteropods as a food source. There is also a resulting loss in calcium carbonate flux to the<br />

deep sea, but compared to the changes for the pelagic ecosystem this is likely of minor concern.<br />

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Index<br />

1 Introduction ....................................................................................................... 4<br />

2 Ocean Acidification........................................................................................... 6<br />

2.1.1 Changes in pH and carbonate.................................................................................6<br />

2.1.2 Changes in saturation state of aragonite and calcite .............................................7<br />

2.2 Ocean Acidification in the Southern Ocean....................................................................8<br />

2.2.1 Changes in saturation depth .................................................................................10<br />

3 Pteropods......................................................................................................... 12<br />

3.1 Characteristics ..............................................................................................................12<br />

3.2 Pteropods in the calcium carbonate cycle ....................................................................13<br />

3.3 Pteropods in the Southern Ocean..................................................................................14<br />

3.4 Sensitivity to changes in pH and carbonate ..................................................................14<br />

4 Impacts of ocean acidification on pteropods: Discussion .......................... 16<br />

4.1 Effects of elevated CO 2 on calcification........................................................................16<br />

4.2 Effects on ocean carbon system ....................................................................................17<br />

4.3 Cascading effects...........................................................................................................17<br />

4.4 Further effects ...............................................................................................................17<br />

4.5 Summary of effects on pteropods ..................................................................................18<br />

5 Future Research .............................................................................................. 18<br />

6 References....................................................................................................... 19<br />

Figures<br />

Figure 1: Concentrations of H 2 CO 3 *, HCO - 3 and CO 2- 3 as a function of pH ................................6<br />

Figure 2: CO 2 dissolution and aragonite formation in the ocean ...................................................7<br />

Figure 3: Carbonate ion concentration versus depth......................................................................8<br />

Figure 4: Currents feeding the Southern Ocean.............................................................................9<br />

Figure 5: Atmospheric CO 2 scenarios and surface [CO 2- 3 ] in the Southern Ocean. ....................10<br />

Figure 6: The aragonite saturation state in the surface ocean in the years 1994 and 2100..........11<br />

Figure 7: The euthecosomatour pteropod Cavolinia tridentate. ..................................................12<br />

Figure 8: A pelagic pteropod........................................................................................................12<br />

Figure 9: Vertical distribution of thecocomes in western Subantarctic and Antarctic waters. ....14<br />

Figure 10: Shell dissolution in a live pteropod ............................................................................15<br />

Figure 11: Calcification rate versus saturation state. ...................................................................16<br />

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1 Introduction<br />

The absorption of anthropogenic carbon dioxide (CO 2 ) alters the ocean’s biological and<br />

geochemical processes. Global emissions from human activity, such as the combustion of fossil<br />

fuel, have boosted the CO 2 concentration from its pre-industrial value of about 280 parts per million<br />

(ppm) to presently 380 ppm (Sabine et al., 2004). Roughly a third of the emissions have been taken<br />

up by the ocean, turning them more acidic. The threat of this continuing ocean acidification to<br />

marine life has only recently been recognised and many questions as to how marine ecosystems will<br />

react are not yet answered (Kleypas et al., 2006). A decrease in pH (increase in hydrogen ions) will<br />

shift the chemical equilibrium towards smaller carbonate ion (CO 3 2- ) concentrations. This has been<br />

shown to affect the calcification of marine organisms, which form their tests and shells out of<br />

calcium carbonate (CaCO 3 ) (Orr et al., 2005; Feely et al., 2004). Biogenic CaCO 3 excreted in the<br />

upper water layers and sinking to the deep sea triggers a global cycle of carbon fluxes. Calcification<br />

is found from the lowest trophic level, the phytoplankton, up to larger invertebrates such as<br />

echinoderms.<br />

The Southern Ocean is especially vulnerable to changes induced through CO 2 uptake due to its<br />

position in the global ocean circulation system (Sarmiento and Gruber, 2006). In this ecosystem,<br />

planktonic shelled molluscs, the pteropods, form the dominant part of the calcifying community<br />

(The Royal Society, 2005). As their habitat is very sensitive to the uptake of anthropogenic CO 2 ,<br />

they are likely to be among the first to be affected by ocean acidification. It is the aim of this paper<br />

to summarize and assess what is known about the changes these organisms are faced with and how<br />

they might respond to it.<br />

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2 Ocean Acidification<br />

2.1.1 Changes in pH and carbonate<br />

Anthropogenic emissions have increased the concentration of CO 2 from its pre-industrial value of<br />

280 parts per million (ppm) to 380 ppm today (IPCC, 2001). It will continue to rise and may well<br />

reach the 1000 ppm mark by 2100, depending on further emissions. CO 2 is soluble in water and is<br />

therefore taken up by the ocean out of the atmosphere. About 30 % of the anthropogenic CO 2,<br />

roughly 120 Petagrams (Pg = 10 15 g) of carbon (C), has already been absorbed by the sea at a rate of<br />

about 2 Pg C per year during the last 20 years (Sabine et al., 2004; Sarmiento and Gruber, 2006).<br />

Different scenarios for the future CO 2 concentration have been developed by the Intergovernmental<br />

Panel on Climate Change (IPCC) (IPCC, 2001). In this paper I chose the scenario IS92a as a<br />

reference for my considerations. That is to be coherent with the studies of Orr et al., 2005 and Feely<br />

et al., 2004, which both used the IS92a for their experiments and contain the most important data on<br />

pteropods and ocean acidification for this paper. The IS92a scenario was developed in 1992. Then it<br />

was considered an intermediate scenario with mid-range CO 2 emissions. Current emissions are<br />

higher than assumed in IS92a, though, and rather follow the newer scenario A1F in Figure 5 a.<br />

When CO 2 dissolves in water, it leads to a reduction in both pH and carbonate ion (CO 3 2- )<br />

concentration (Figure 2 a-c). The more CO 2 is taken up, the lower is the consequent pH – resulting<br />

in an acidification – and the lower is the resulting carbonate ion concentration (Figure 1). The ocean<br />

is able to buffer its pH through the reaction with dissolved carbonate:<br />

H 2 CO 3 * + CO 3 2- ↔ 2 HCO 3<br />

-<br />

or with calcium carbonate (CaCO 3 ) from the sediments or from calcifying organisms:<br />

H 2 CO 3 * + CaCO 3 ↔ Ca 2+ + 2 HCO 3<br />

-<br />

Due to its slow circulation, the ocean is a slow sink, though, taking thousands of years to equilibrate<br />

with the atmosphere from the surface to the bottom. The sediments would have a huge capacity to<br />

buffer the pH changes induced by dissolved CO 2 , but the ocean circulation is too slow compared<br />

with the rapid emissions and the sediment dissolution itself is a slow process. The average pH of the<br />

ocean has already decreased by 0.1 units compared to its preindustrial value, which corresponds to a<br />

26 % increase in the hydrogen ion concentration. Models under the IS92a scenario predict a drop of<br />

surface ocean pH of more than 0.3 by 2100 and up to 0.77 by 2300, a condition the world’s oceans<br />

likely have not experienced in the last 300 million years (Caldeira and Wickett, 2003; The Royal<br />

Society, 2005).<br />

Figure 1: Plot of the concentrations of H 2 CO 3 *, HCO - 3 and CO 2- 3 as a function of pH<br />

The concentrations are plotted for a dissolved inorganic carbon concentration [DIC] of 2000<br />

µmol kg -1 . Note that the vertical axis is logarithmic as well. From Sarmiento and Gruber, 2006.<br />

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2.1.2 Changes in saturation state of aragonite and calcite<br />

Changes in the ocean carbonate chemistry inevitably affect marine life. The first ones to be affected<br />

are most likely calcifying organisms, which need the carbonate to build up their tests and shells.<br />

There are two forms of calcium carbonate (CaCO 3 ) secreted by marine calcifying organisms,<br />

aragonite and calcite. They differ from each other in their crystalline structures: aragonite has an<br />

orthorhombic configuration and calcite a trigonal one. The different structure of aragonite results in<br />

a about 50 % higher solubility in seawater than calcite (Feely et al., 2004). To secrete either of<br />

them, the water has to be supersaturated with respect to the respective form. The state of saturation<br />

is given by:<br />

Ω aragonite = [Ca 2+ ] * [CO 3 2- ] / K sp aragonite ,<br />

respectively:<br />

Ω calcite = [Ca 2+ ] * [CO 3 2- ] / K sp calcite .<br />

with Ω >1 indicating supersaturation and Ω


2.2 Ocean Acidification in the Southern Ocean<br />

The calcifying organisms in the Southern Ocean are more vulnerable to decreases in pH and<br />

carbonate ion concentration because the surface CO 3 2- concentration there is naturally low. The<br />

boundaries of the Southern Ocean are not well defined since there are no continents bordering it,<br />

but the definition adopted here is that it encompasses all regions south of 45° S. The higher<br />

vulnerability to pH and carbonate decreases is due to the vertical distribution of [CO 3 2- ] caused by<br />

(i) the biological carbon cycle and (ii) the predominant circulation. Here is how theses two<br />

processes influence the pH and carbonate ion concentration in the water column:<br />

i) In the upper water layers, photosynthetic organisms assimilate and calcifying organisms<br />

form CaCO 3 . The assimilation of CO 2 influences the CO 3 2- concentration, it increases by 1 mol with<br />

each mol of organic matter produced (simplified, for more detailed information see Sarmiento and<br />

Gruber, 2006). The formation of CaCO 3 also has an impact on CO 3 2- concentration: it consumes 1<br />

mol carbonate ions per mol biogenic CaCO 3 produced: Ca 2+ + CO 3 2- CaCO 3 . So, assimilation<br />

produces CO 3 2- and calcium carbonate production reduces it. The organic matter, though, outweighs<br />

the CaCO 3 by a factor of up to 5 (Sarmiento and Gruber, 2006), thus the carbonate ion<br />

concentration is high in the sunlight penetrated part of the water column (Figure 3 a). When<br />

organisms die, both organic matter and CaCO 3 skeletons and shells are eventually decomposed. The<br />

remineralization of 1 mol organic matter uses up the 1 mol of CO 3 2- that was released during its<br />

formation just like the dissolution of 1 mol CaCO 3 releases again the 1 mol of CO 3 2- it consumed<br />

for its formation. But the ratio of the two decomposition processes varies with depth. While most of<br />

the organic matter is already remineralized in shallow depths (Figure 3 b), the CaCO 3 sinks deeper<br />

before it is dissolved. In the deep sea the organic matter-to-CaCO 3 ratio approximates one, but the<br />

deep remains undersaturated (Figure 3 c). The resulting pro<strong>file</strong> shows high [CO 3 2- ] in the upper and<br />

low [CO 3 2- ] in the deep water layers. The depth at which waters are exactly saturated (Ω = 1) with<br />

regard to a particular mineral phase is called the saturation horizon or saturation depth.<br />

Figure 3: Plot of the carbonate ion<br />

concentration versus depth. Also shown are the<br />

carbonate saturation concentrations with regard<br />

to calcite (solid line) and aragonite (dashed line).<br />

The surface waters (a) are supersaturated with<br />

respect to both aragonite and calcite. Further<br />

down in the water column carbonate ions are<br />

strongly decreased by remineralization of organic<br />

matter (b). In the deep carbonate ions increase<br />

slightly but stay undersaturated (c). The pro<strong>file</strong><br />

was taken in the North Pacific at 42° N, 152° W.<br />

Modified from Sarmiento and Gruber, 2006.<br />

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ii) The Southern Ocean shows extensive upwelling, drawing up the deep waters from the<br />

Atlantic, the Pacific and the Indian Ocean. This upwelling is fed by two major loops (Figure 4), one<br />

conveying deep water from the North Atlantic and another running at the bottom of the Antarctic<br />

northward and returning at mid-depth to the Southern Ocean. Hence the Southern Ocean is<br />

constantly fed with deep water depleted of carbonate ions.<br />

Figure 4: Simplified<br />

graphic of the<br />

currents feeding the<br />

Southern Ocean.<br />

The dashed circle<br />

indicates the upwelling<br />

region in the Southern<br />

Ocean, fed by deep<br />

North Atlantic water<br />

(a) and deep water<br />

from the Pacific,<br />

Atlantic and Indian<br />

Ocean basins (b).<br />

After Sarmiento and<br />

Gruber, 2006.<br />

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2.2.1 Changes in saturation depth<br />

Due to its upwelling carbonate ion-poor water the Southern Ocean is amongst all the seas the first to<br />

suffer aragonite undersaturation at the surface. As seen in the example in Figure 3 the saturation<br />

state is not uniformly distributed over the water column. In general surface waters are<br />

supersaturated with respect to aragonite while the deep sea is undersaturated. According to the<br />

model simulations of Orr et al.(2005), CO 2 concentrations in the atmosphere under the IS92a<br />

scenario will reach 788 ppm. The resulting carbonate ion concentration at the surface of the<br />

Southern Ocean will drop to 55 ± 5 µmol kg -1 , which is clearly below the aragonite saturation of 66<br />

µmol kg -1 (Figure 5). The saturation horizon will shoal from its present depth of approximately 730<br />

m all the way up to the surface (Orr et al., 2005), leaving the entire water column of the Southern<br />

Ocean undersaturated (Figure 6).<br />

Figure 5: Atmospheric CO 2<br />

scenarios and<br />

corresponding average<br />

surface [CO 3 2- ] in the<br />

Southern Ocean.<br />

Time series of average<br />

surface [CO 3 2- ] (b) in the<br />

Southern Ocean for the IPCC<br />

CO 2 scenarios (a) (IPCC,<br />

2000).<br />

Modified from Orr et al.,<br />

2005.<br />

- 10 -


a: 1994<br />

45°S<br />

b: 2100<br />

45°S 45°S<br />

Figure 6: The aragonite saturation state in the surface ocean in the year 1994 (a) and 2100 (b),<br />

respectively, as indicated by ∆[CO 3 2- ] A . The ∆[CO 3 2- ] A is the in situ [CO 3 2- ] minus that for aragoniteequilibrated<br />

sea water at the same salinity, temperature and pressure. Shown are the median concentrations<br />

of the Ocean Carbon-Cycle Model Intercomparison Project (OCMIP-2) on the surface in the year 2100 under<br />

the IPCC scenario IS92a. Positive ∆[CO 3 2- ] A indicates supersaturation; negative ∆[CO 3 2- ] A indicates<br />

undersaturation. The red dashed line (a) shows the approximate extent of the Southern Ocean, the black<br />

dashed line (b) indicates where the aragonite saturation horizon has reached the surface. Modified from Orr<br />

et al., 2005.<br />

Since calcite is not as soluble in sea water as aragonite it will need a lower pH to reach<br />

undersaturated conditions. However, calcite undersaturation in the Southern Ocean is thought to<br />

follow the one of aragonite in only 50-100 years (Orr et al., 2005).<br />

Second to follow the conditions of the Southern Ocean is the Arctic Sea, because it also has a very<br />

low buffer capacity. In regions of the North Pacific and North Atlantic the aragonite saturation<br />

horizon will shoal all the way to the surface by 2100 (Figure 6).<br />

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3 Pteropods<br />

3.1 Characteristics<br />

Pteropods are shelled pelagic snails and belong to the zooplankton group. There are two Orders of<br />

the Class of the Gastropoda, which are commonly referred to as pteropods. One being the<br />

Thecosomata, the shelled pteropods considered in this paper, the other being the shell-less<br />

Gymnosomata. The name ‘pteropod’ is derived from its most striking physiological feature, a winglike<br />

modification of the molluscan foot (ptero- for wing, -poda for foot) (Figure 7 and Figure 8).<br />

Thecosomes include 48 to 58 planktonic species. As they are very fragile, specimens get easily<br />

damaged during collection and pose difficulties in their taxonomic assignment. The species differ<br />

from each other in shell morphology, which is very multifaceted from spirally coiled or needle-like<br />

to triangular. In order to minimise weight, the shells of thecosomes are very thin with a gauge of 6<br />

µm to 100 µm. Being negatively buoyant, thecosomes use their wings for propulsion and<br />

locomotion. The jerky flapping movement led to their common name ‘sea butterflies’. Many<br />

thecosomes migrate diurnally, flapping towards the surface during the night and sinking back to<br />

deeper water during the day. (Lalli and Gilmer, 1989)<br />

Figure 7: The euthecosomatour pteropod Cavolinia<br />

tridentate.<br />

From Kleypas et al., 2006.<br />

Figure 8: A pelagic pteropod.<br />

Photo by Russ Hopcroft.<br />

All thecosomes spend their premature life as males, changing sex as they age (= protandrous<br />

hermaphrodites) (Lalli and Gilmer, 1989). Mating occurs between males that are about to mature to<br />

females, so called reciprocal fertilisation. The sperm is kept until the transition is complete and the<br />

females release fertilised eggs into the water. The lifespan of shelled pteropods is quite long,<br />

ranging from months to 2.5 years (Fabry, 1989; Kleypas et al., 2006).<br />

Being a larger zooplankton, the pteropods diet consists of phytoplankton and small zooplankton,<br />

and it provides food for many predatory species of the higher trophic levels. Thecosomes secrete a<br />

mucous web both for feeding and buoyancy (Lalli and Gilmer, 1989). The web is orbicular or<br />

funnel-shaped and can exceed the thecosomes body size many times over. It is periodically drawn<br />

in and the entangled prey is forwarded to the mouth. If disturbed, the animal will abandon its web.<br />

Deserted feeding webs of thecosomes locally influence the ecosystem they live in. While drifting in<br />

the water, organic particles entangle in the mucus and it thus serves as a breeding ground for<br />

bacteria and as a food source for small grazers. The pteropod feces transport biogenic matter out of<br />

the surface waters to the deep.<br />

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Thecosomes are preyed on by larger carnivorous zooplankton, fishes, marine mammals such as<br />

baleen whales and ringed seals, marine birds and gymnopods. Commercial fish like mackerel,<br />

herring, North Pacific salmon or yellowfin tuna are also known to prey on shelled pteropods. To<br />

some of the predators, thecosomes make up only an occasional part of their diet whenever available,<br />

some are heavily dependent on them (Seibel and Dierssen, 2003) and some feed exclusively on the<br />

marine snails. An example is the thecosome Clio antarctica in the Antarctic, whose only food<br />

source is Limacina helicina, another thecosome (Seibel et al., 2003).<br />

3.2 Pteropods in the calcium carbonate cycle<br />

Pelagic snails form their shells out of aragonite, taking up carbonate ions (CO 3 2- ) dissolved in the<br />

upper water layers and calcium (Ca 2+ ), which is abundant throughout the water column (Figure 2 e).<br />

Shells of the dead molluscs sink, exporting the aragonite to deeper water where it is either deposited<br />

forming sediments on the sea-floor or is dissolved if sinking below the aragonite saturation depth<br />

(Figure 2 f, g).<br />

There seems to be no agreement yet as to the exact contribution of pteropod aragonite shells to the<br />

global export flux of carbonate from surface waters. This results from the lack of appropriate<br />

measurement techniques and lack of observations. Pteropods have different sizes, generation times<br />

and dissolution rates than foraminifera or coccolithophores, the major calcite producers, and are<br />

therefore difficult to compare. Deep sediments as well as sediment traps show limited numbers of<br />

pteropod shells because aragonite dissolves rapidly in undersaturated water both during sinking<br />

through the water column and lying on the sea bed. So-called ‘pteropod ooze’, sediments with a<br />

high proportion of calcium carbonate from pelagic snails, are found primarily in shallow waters<br />

above the aragonite compensation depth. Studies suggest that aragonite contributes 12 % (Lalli and<br />

Gilmer, 1989) to 50 % of the global carbonate export from surface waters to the deep (Berner in<br />

Berger, 1977; Byrne et al., 1984). The estimated 50 % was based on a method that only used data<br />

from above-average pteropod-rich sediments. 50 % is thought to be too high by Berger (1977) and<br />

Lalli (1989). Berner and Hojo (1984) suggested 12 % of the calcium carbonate flux to be<br />

contributed by aragonite (Lalli, 1989). Since they used sediment traps to determine the amount of<br />

sinking thecosomes, the shells may already have been partly dissolved when the traps were<br />

collected and the 12 % therefore been an underestimation. However there is little doubt that<br />

aragonite plays a rather important role in the global oceanic carbon cycle. In the Ross Sea and the<br />

Antarctic Polar Front pteropods have been found to dominate the export flux of carbonate (Orr et<br />

al., 2005).<br />

- 13 -


3.3 Pteropods in the Southern Ocean<br />

Some species are confined to very narrow environmental niches. In the Southern Ocean mainly four<br />

species occur, namely Clio sulcata and Clio antarctica, Limacina helicina and Limacina retroversa<br />

(Figure 9). The Limacina sp. are found in the shallower Subantarctic and Antarctic waters,<br />

respectively, to a depth of about 250 m while the Clio sp. live between 200 and 800 m depth.<br />

Thecosome population densities reach thousands of individuals per m 3 , at times even dominating<br />

the zooplankton community (Cabal et al., 1999; Fabry, 1989).<br />

Figure 9: Vertical distribution of<br />

thecocomes in western<br />

Subantarctic and Antarctic<br />

waters.<br />

From Lalli and Gilmer, 1989.<br />

3.4 Sensitivity to changes in pH and carbonate<br />

Very little is known about the pteropods reaction to elevated CO 2 concentrations and the resulting<br />

effects. Up to today there are no long-term observations. However, there have been a few studies<br />

looking at the reaction of the aragonite shells to increased carbon dioxide concentrations. Shells of<br />

pteropods cannot persist in water undersaturated with respect to aragonite. Shells collected from<br />

sediment traps below the aragonite saturation depth show extensive surface roughening and etching<br />

(Byrne et al., 1984). In recent experiments live pteropods have been subjected to elevated CO 2<br />

concentrations and consequent undersaturated conditions (Orr et al., 2005; Feely et al., 2004) as the<br />

IPCC ‘business as usual’ scenario for CO 2 emissions (IS92a) would induce in the Southern Ocean.<br />

The exposure resulted in pitting, peeling back of the exterior layer, and extensive erosion (Figure<br />

10).<br />

- 14 -


Figure 10: Shell dissolution in a live pteropod. a-d, Shell from a live pteropod, Clio pyramidata,<br />

collected from the subarctic Pacific and kept in water undersaturated with respect to aragonite for 48<br />

h. The whole shell (a) has superimposed white rectangles that indicate three magnified areas: the shell<br />

surface (b), which reveals etch pits from dissolution and resulting exposure of aragonite rods; the<br />

prismatic layer (c), which has begun to peel back, increasing the surface area over which dissolution<br />

occurs; and the aperture region (d), which reveals advanced shell dissolution when compared to a<br />

typical C. pyramidata shell not exposed to undersaturated conditions (e). From Orr et al., 2005.<br />

Conclusions are that the pteropods will not be able to produce their shells and thus to survive under<br />

conditions undersatured with respect to aragonite and will be restricted to the shrinking latitudinal<br />

and vertical expansion of saturated waters. If the Antarctic species will be able to migrate to and<br />

survive in the warmer waters of lower-latitude oceans, which will stay supersaturated, is unknown.<br />

Elevated carbon dioxide concentrations can further affect marine organisms directly in their<br />

physiology. Acidification of body fluids through gills and body surface reduces the bloods ability to<br />

transport oxygen. Some organisms react with decreased egg production or loss of sperm motility.<br />

Effects on embryos and larvae have also been observed. However, there have so far been no studies<br />

conducted assessing such impacts on pteropods.<br />

There are no further studies assessing the response of pteropods to changes in parameters that they<br />

will most likely face during the next century. The higher CO 2 concentrations will affect the<br />

pteropods indirectly through the induced changes in the animal’s ecosystem. The pteropod’s main<br />

food source, the phytoplankton, may be affected in various ways. Elevated CO 2 concentrations can<br />

have an effect on the assimilation of inorganic carbon. And the lower pH affects the speciation and<br />

bioavailability of nutrients and micronutrients. These two processes influence growth rates and<br />

productivity of the phytoplankton and hence the food abundance for pteropods (The Royal Society,<br />

2005). But none of these influences has been assessed in studies.<br />

- 15 -


4 Impacts of ocean acidification on pteropods: Discussion<br />

4.1 Effects of elevated CO 2 on calcification<br />

Since there are no studies examining the calcification rate of pteropods under elevated CO 2<br />

concentrations, results from other calcifying organisms may help to make assumptions. There are<br />

several patterns after which groups of organisms react. Kleypas et al. (2006), summarised results of<br />

calcification rates of various organisms.<br />

i) In the case of the examined corals it seems that calcification does not only rely on<br />

supersaturated water, but also on the state of saturation (Ω). Calcification rates were reduced with<br />

decreasing saturation state, although waters were still supersaturated with regard to aragonite<br />

(Figure 11 a, dashed line). Calcification stopped completely in undersaturated water. If pteropods<br />

reacted in the same manner, they would not be able to survive in undersaturated regions of the<br />

oceans. However, there is the possibility that calcification can be maintained through cellular<br />

mechanisms. Imaginable are ion pumps that can keep carbonate ion concentrations higher inside the<br />

cells to enable calcification. The exact mechanisms how pteropods secrete their shells are not<br />

known. If such techniques exist, the reaction of calcification might rather look like the solid line in<br />

Figure 11 a. Depending on the state of undersaturation at which calcification stops, pteropods might<br />

be able to compensate for a certain rate of shell dissolution as observed in Figure 10 through<br />

continuing calcification. But even if they could – if they really respond according to this pattern -<br />

they would already be affected now as the saturation state is still above 1 but decreasing.<br />

ii) The examined foraminifera secrete calcite and show a different behaviour. Their<br />

calcification rates remained rather unchanged over a wide range of Ω but declined as soon as the<br />

water became undersaturated with respect to calcite (Figure 11 b). The slope of the decline is again<br />

dependent on the presence of mechanisms that sustain calcification even in undersaturated water. If<br />

pteropods reacted after this scenario, a decreasing saturation state would not affect them until it<br />

sinks below 1.<br />

Figure 11: Schematics of calcification rate versus saturation state.<br />

After whatever pattern pteropods react to elevated CO 2 , there seems to be no doubt that their<br />

calcification is reduced in waters undersaturated with respect to aragonite. Models and studies have<br />

also convincingly shown that the Southern Ocean will be first to suffer undersaturation all the way<br />

up to the surface. The deeper dwelling species Clio sulcata and Clio Antarctica will be first to meet<br />

such conditions, followed by those further up in the water column. Whether they can keep on<br />

- 16 -


calcifying and compensate for the erosion of their shell is unknown, but is very doubtful if<br />

carbonate ion concentrations in the Southern Ocean keep on dropping after 2100. Adaptation to<br />

lower carbonate ion concentrations is possible but would have to happen within this century, which<br />

is an extremely short time in evolutionary terms. And it is further aggravated by the pteropods<br />

relatively long generation time. I have doubts that the pteropod species endemic to the Antarctic and<br />

Subantarctic will be able to change over from their cold habitat to warmer lower-latitudinal waters.<br />

Ocean currents would first have to allow their dispersal to the temperate zone. Their physiology<br />

would have to be able to adapt to temperature increases of up to 10° C (Lalli and Gilmer, 1989).<br />

Furthermore, they would have to find a niche in an alien ecosystem. Overall, it seems unlikely that<br />

the Antarctic species will be able to evade extinction if the predicted CO 2 scenarios apply.<br />

4.2 Effects on ocean carbon system<br />

Due to the rather small contribution of pteropod shells to the global CaCO 3 flux, a change in<br />

pteropod abundance will likely affect the global ocean carbon system less than it affects the<br />

Antarctic ecosystem. The contribution of aragonite produced by pteropods is not huge but certainly<br />

not negligible. A back-of-the-envelope calculation for the Southern Ocean can be made by the<br />

following assupmtions: Aragonite secreting corals have shown a reduction in calcification within a<br />

range of 13 to 83 % under [CO 2 ] of 840 ppm (Kleypas et al., 2006). If we assume that the average<br />

decrease in calcification of these organisms (42 %) roughly applies to pteropods, that the [CO 2 ] will<br />

rise according to the IS92a scenario, and that pteropods make up for half of the calcium carbonate,<br />

then the decrease in export of CaCO 3 to the deep Southern Ocean by 2100 will be in the order of 20<br />

%. The local ecosystem is far more affected by the decline of the pteropod population than the<br />

global CaCO 3 flux.<br />

4.3 Cascading effects<br />

The decline or even disappearance of pteropod populations in the Southern Ocean is certainly going<br />

to affect the ecosystem. Predators not entirely relying on pteropods will probably be able to<br />

compensate for the lost food source with other species. But this results in increased predation<br />

pressure on any alternative prey. Any predator feeding exclusively on pteropods will most probably<br />

share the fate of its prey, either redistributing along with the pteropods or facing extinction (Royal<br />

Society, 2005). Discriminating calcifying organisms will probably lead to a shift in the ecosystem<br />

structure in favour of non-calcifying organisms. If there is less aragonite exported to deeper water,<br />

the community of deep sea species may be affected. Deep-sea biodiversity and ecology has been<br />

found to be dependent on calcifying planktonic organisms in near-surface waters (Kleypas et al.,<br />

2006).<br />

4.4 Further effects<br />

• The pH decrease used by studies that observed direct mortality or decreased reproduction in<br />

marine organisms is in most cases much higher than what is expected during the 21 st<br />

century. I therefore assume that calcification in pteropods is inhibited long before these<br />

other effects appear. Early life stages seem to be most vulnerable to pH changes. To draw a<br />

final conclusion, effects of lower pH on larval stages of pteropods would therefore have to<br />

be investigated.<br />

• Phytoplankton will surely be affected by the ocean acidification and the global climate<br />

change. But indirect impacts through the changes in phytoplankton have not been assessed<br />

to an extent that would allow conclusions on the consequences for pteropods.<br />

• Climate change increases sea temperatures. Direct effects on the pteropods’ physiology are<br />

not known, but since the shoaling of the aragonite saturation depth already constrains the<br />

- 17 -


pteropods towards warmer lower-latitude waters an additional rise in temperature will<br />

probably increase worsen their situation.<br />

4.5 Summary of effects on pteropods<br />

Pteropods will be most affected by decreased calcification. Other effects of pH decline and<br />

temperature rise may add to the negative impact but are secondary. It is unlikely that pteropods in<br />

the Southern Ocean will survive the 21 st century. Their disappearance will have a fatal impact on<br />

the ecosystem, especially on the organisms relying heavily on pteropods as a food source. The loss<br />

in calcium carbonate flux to the deep sea is not irrelevant but of minor concern.<br />

5 Future Research<br />

Only recently have scientists recognised the threat posed by ocean acidification to aragonite<br />

excreting organisms in the high latitude oceans. There is a substantial need for more research:<br />

• Intensive monitoring should deliver reliable data about the absolute abundance of pteropods<br />

in the Southern Ocean and the latitudinal distribution pattern of aragonite export to the deep<br />

sea and how that changes with time. This would allow estimating the consequences of<br />

reduced aragonite production by pteropods.<br />

• The response in calcification rate of pteropods to elevated CO 2 concentrations, as they are<br />

expected until the end of this century, should be quantified. This would require observation<br />

over longer periods. Additionally the calcification mechanisms of pteropods should be<br />

determined.<br />

• Long term studies could possibly answer the question of how reduced calcification affects<br />

the survival of pteropods, its population dynamics, and how their ecology changes (Kleypas<br />

et al., 2006).<br />

• Given the experimental data up to date about their reaction to undersaturated water, one has<br />

to contemplate the disappearance of pteropods altogether from the Southern Ocean.<br />

Therefore, it should be examined how the ecosystem reacts to an absence of pelagic snails.<br />

• Examination of pteropod fossils and reconstruction of their evolutionary pathway may allow<br />

some predictions about their ability to adapt to the changes in their ecosystem.<br />

- 18 -


6 References<br />

Berger, W.H., 1977. Deep-sea carbonate: pteropod distribution and the aragonite compensation<br />

depth. Deep-sea research, 25, p.447-452.<br />

Byrne, R.H., Acker, J.G., Betzer, P.R., Feely, R.A., Cates, M.H., 1984. Water column dissolution<br />

of aragonite in the Pacific ocean. Nature, 312, p.321-326.<br />

Cabal J.A., Alvarez-Marques F., Acuna J.L., Quevedo M., Gonzalez-Quiros R., Huskin<br />

I., Fernandez D., del Valle C.R., Anadon R., 2000. Mesozooplankton distribution and grazing<br />

during the productive season in the Northwest Antarctic Peninsula (FRUELA cruises). Dee-sea<br />

research, 49, p.869-882.<br />

Caldeira and Wickett, 2003. Anthropogenic carbon and ocean pH. Nature, 425, p.365.<br />

Cao, L., Caldeira, K., Jain, A.K., 2007. Effects of carbon dioxide and climate change on ocean<br />

acidification and carbonate mineral saturation. Geophysical research letters, 34.<br />

Fabry, V.J., 1989. Aragonite production by pteropod molluscs in the subarctic Pacific. Deep-sea<br />

research, 36, p.1735-1751.<br />

Feely, R.A., Sabine, C.L., Lee, K., Berelson, W., Kleypas, J., Fabry, V.J., Millero F.J., 2004.<br />

Impact of anthropogenic CO 2 on the CaCO 3 system in the oceans. Science, 305, p.362-366.<br />

IPCC, 2000. Emission scenarios. Special report, found at<br />

http://www.grida.no/climate/ipcc/spm<strong>pdf</strong>/sres-e.<strong>pdf</strong>.<br />

IPCC, 2001. Climate change, 2001: The scientific basis. Contribution of working group I. Found at<br />

http://www.grida.no/climate/ipcc_tar/wg1/index.htm.<br />

Kleypas, J.A., Feely, R.A., Fabry, V.J., Langdon, C., Sabine, C.L., Robbins, L.L., 2006. Impact of<br />

ocean acidification on coral reefs and other marine calcifiers. Workshop report.<br />

Lalli and Gilmer, 1989. Pelagic snails. Stanford university press, California.<br />

Orr, J.C., Fabry, V.J., Aumont, O., Bopp, L., Doney, S.C., Feely, R.A., Gnanadesikan, A., Gruber,<br />

N., Ishida, A., Joos, F., Key, R.M., Lindsay, K., Maier-Reimer, E., Matear, R., Monfray, P.,<br />

Mouchet, A., Najjar, R.G., Plattner, G.K., Rodgers, K.B., Sabine, C.L., Sarmiento, J.L., Schlitzer,<br />

R., Slater, R.D., Totterdell, I.J., Weirig, M.F., Yamanaka, Y. and Yool, A., 2005. Anthropogenic<br />

ocean acidification over the twenty-first century and its impact on calcifying organisms. Nature,<br />

437, p.681-686.<br />

Riebesell, U., Zondervan, I., Rost, B., Tortell, P.D., Zeebe, R.E., Morel, F.M.M., 2000. Reduced<br />

calcification of marine plankton in response to increased atmospheric CO 2 . Nature, 407, p.364-367.<br />

Sabine, C.L., Feely, R.A., Gruber, N., Key, R.M., Lee, K., Bullister, J.L., Wanninkhof, R., Wong,<br />

C.S., Wallace, D.W.R., Tilbrook, B., Millero, F.J,; Peng, T., Kozyr, A., Ono, T., Rios, A.F., 2004.<br />

The oceanic sink for anthropogenic CO 2 . Science, 305, p.367-371.<br />

Sarmiento and Gruber, 2006. Ocean biogeochemical dynamics. Princeton university press,<br />

Princeton.<br />

- 19 -


Seibel and Dierssen, 2003. Cascading trophic impacts of reduced biomass in the Ross Sea,<br />

Antarctica: Just the tip of the iceberg? Biological bulletin, 205, p.93-97.<br />

The Royal Society, 2005. Ocean acidification due to increasing atmospheric carbon dioxide. Policy<br />

document, found at www.royalsoc.ac.uk.<br />

- 20 -


Review of Zero Valent Iron and Apatite as reactive materials for<br />

Permeable Reactive Barrier<br />

Author: Luca Geranio<br />

Tutor: Dr. Evert Elzinga<br />

Term Paper SS 07/08, major in Biogeochemistry and Pollutant Dynamics<br />

Department of <strong>Environmental</strong> Sciences<br />

<strong>ETH</strong> Zürich<br />

June 2007<br />

Abstract<br />

Permeable reactive barrier (PRB) is a technology developed recently in the last years. It has obtained<br />

promising results in the removal of several contaminants present in the groundwater. This Term paper<br />

focuses the attention on two reactive materials, Zero valent iron and Apatite, employed in the PRB system,<br />

giving an overview of the reactions and types of pollutants treated to date. The pollutants removal from<br />

groundwater by these two reactive materials is based on different processes, that is, reduction of organic or<br />

inorganic contaminants in the case of zero valent iron and immobilization of inorganic pollutants in the case<br />

of Apatite. Zero valent iron acts as reductant either reducing directly the contaminants in a less harmful form<br />

or also reducing pollutants which can subsequently precipitate. At the moment, Zero valent iron is the<br />

material most frequently used in the field installations and it is particularly effective in the chemical<br />

degradation of persistent chlorinated compounds into non-toxic and harmless by-products. In general<br />

perhalogenated hydrocarbons tend to be reduced faster than hydrocarbons less halogenated and also the<br />

dechlorination is more rapid at saturated carbons (e.g. CCl 4 ) centers than at unsaturated carbons (e.g.<br />

TCE)[15]. Like anions, inorganic cations are reduced by Zero valent iron and precipitate as meagrely soluble<br />

solids. Zero valent iron seems to have effect in the remediation of heavy metals such as chromium, arsenic,<br />

technetium, selenium, copper, mercury and uranium.<br />

Apatite II is a particular form of apatite (natural waste of fish industry) that can immobilize and sequester a<br />

broad range of metals into new phosphate minerals and other low-solubility phases for a geologic period of<br />

time. The apatite II provides a low but sufficient concentration of PO4 3- in solution in order to exceed the<br />

solubility of the metal-apatite that rapidly precipitate, but only in the presence of an existing apatite structure<br />

which acts as nucleating site or seed crystal. Apatite acts also as a material for non-specific adsorption of<br />

most cationic metals from solution and is also an excellent buffer for neutralizing acidity through PO 4<br />

3-<br />

, OH - ,<br />

and substituted CO 3<br />

2-<br />

, exerting control over chemical activities of other species leading to the precipitation of<br />

oxihydroxide- and carbonate-metal phases. Metals in solution are immobilized on the apatite mineral by<br />

surface sorption (main mechanism for most metals), precipitation (main mechanism for U, Pu, Pb,<br />

lanthanides) or co-precipitation (transition metals). The relative contribution of adsorption and precipitation<br />

to metal removal depends upon the environmental conditions, the mineral phases present, and the metal<br />

concentration in solution [16] [14].


Table of contents<br />

1. INTRODUCTION..........................................................................................................................ii<br />

1.1 Permeable reactive barriers: the basic idea................................................................................ ii<br />

1.2 Site characterization ................................................................................................................. iv<br />

1.3 Choice of reactive media (RM) and laboratory tests.................................................................iv<br />

2. GEOCHEMISTRY OF BARRIER MATERIALS..................................................................... v<br />

2.1 Zero Valent Iron......................................................................................................................... v<br />

2.1.1 Reactions and types of pollutants treated ........................................................................... v<br />

2.1.2 Treatment of halogenated organic compounds with Zero Valent Iron.............................. vi<br />

2.1.3.1 Chromium ................................................................................................................... viii<br />

2.1.3.2 Technetium, Selenium, Arsenic ................................................................................... viii<br />

2.1.4 Zero valent iron and inorganic cations ............................................................................viii<br />

2.1.5 Precipitation problems........................................................................................................ix<br />

2.2 Apatite ...................................................................................................................................... ix<br />

2.2.2 Apatite II..............................................................................................................................x<br />

2.2.2.1.1 Heterogeneous nucleation............................................................................................ xi<br />

2.2.2.1.2 pH buffering................................................................................................................ xii<br />

2.2.2.1.3 Surface chemi-adsorption............................................................................................xii<br />

2.2.2.1.4 Biological stimulation................................................................................................. xii<br />

2.2.2.2 Case study: use of apatite(II) in groundwater remediation contaminated with heavy<br />

metals by mine waste in Idaho,USA ......................................................................................... xii<br />

2.2.2.3 Benefits of use of Apatite II ......................................................................................... xiii<br />

3. CONCLUSIONS AND REMAINING RESEARCH QUESTIONS....................................... xiv<br />

4. AKNOWLEDGEMENT .............................................................................................................xv<br />

5. REFERENCES............................................................................................................................. xv<br />

ii


1. INTRODUCTION<br />

1.1 Permeable reactive barriers: the basic idea<br />

Permeable reactive barrier (PRB) is a technology developed beginning from the 90s as a remediation for<br />

polluted groundwater. It is an implementation consisting of a permeable zone which cleans up a<br />

contaminated plume through immobilization or transformation of the pollutants in a less harmful form. In the<br />

subsurface the flow of the water is intercepted by a perpendicular “wall” of reactive materials that can<br />

degrade, precipitate, sorb or exchange contaminants which can so reach the innocuous or legal concentration<br />

downgradient the barrier [1][2][8]. The principle of applying PRB's in remediating contaminated ground<br />

water is illustrated in Figure 1. This treatment technology is so called “in situ passive method” because<br />

typically exploits the natural gradient of the flow allowing the water but not the contaminants to pass across<br />

the barrier [2][8][23]. It is a new valid alternative to traditional Pump and Treat systems due to its low cost<br />

and mantenance once installed and its potential long duration and effectiveness.<br />

A benefit of its application is the large number of pollutants that can be treated often bringing their<br />

concentration below the detection limit. Moreover the site on the surface above the treated aquifer is<br />

available for other activities and can be economically re-used once the installation is concluded and during<br />

the remediation process. There is the possibility to treat waste plumes that are heterogeneous in composition<br />

and concentration and a reduction of costs (~50%) and energy compared to Pump and treat (P&T)<br />

methodology could be achieve. In addition PRB has lower impact to the rate of groundwater flow compared<br />

to P&T. Finally it could be a strong potential application in urban areas. [2][8]<br />

One of the mains drawbacks for the utilization of this technology is that only the part of plume moving<br />

downstream from the typically immobile source across the reactive materials can be treated.<br />

Another drawback is that the barrier is permanent and fixed and can not be shifted if there is a deviation in<br />

the movement of plume. PRB technology needs careful study and characterization of the site prior the<br />

installation in order to avoid this drawback. All the possible subsurface changes must be taken into account<br />

and the configuration and the size of the barrier must be able to respond to them.<br />

Other requirements are the extensive knowledge of hydrology in the aquifer and the precise localization and<br />

description of the polluted plume. Furthermore PRB is applicable only for shallow plumes ( not deeper than<br />

50 feet down the ground surface). In addition to these hassles a long process of remediation is needed if the<br />

aquifer has a low hydraulic conductivity. Finally a possible lessening of permeability of the PRB due to<br />

corrosion, clogging and fouling of the reactive media could happen after a certain time. Unfortunately few<br />

field data concerning the longevity of the reactivity of the PRB are available. [2][8][23]<br />

The PRB is emplaced digging a trench in the ground and subsequently filled with adapted reactive media in<br />

accordance with the hydrogeology characteristics of the site and the pollutant to treat.<br />

Figure 1. Principle of groundwater remediation by using PRB [8]<br />

Basically there are two main types of configuration for the installation of the PRB that are used for the field<br />

application: the continuous PRB and the Funnel-and-Gate Design.<br />

iii


In the continuous scheme the plume encounters a wall of reactive media for all its width and height. The<br />

reactive zone such as in Funnel and Gate configuration has permeability equal or bigger than that of the<br />

aquifer and so the groundwater changes very little or does not change its flux velocity and natural gradient. It<br />

also does not deviate around the reactive media. It is good norm to place the inferior part of the barrier into<br />

impermeable strata in order to prevent the contaminant underflow phenomena.<br />

In the Funnel and Gate design the groundwater is directed by means of a impermeable funnel (commonly<br />

sheet pilings or slurry walls) towards the permeable zone or “gate” constituted to the media. The cross<br />

sectional area of the gate is usually rectangular and much smaller than that of the plume in the aquifer and so<br />

the flow velocity within the reactive site will be higher [23].<br />

1.2 Site characterization<br />

A complete understanding of the site destined to PRB implementation is compulsory. You have to<br />

characterize the stratigraphy, its variation in fracturing and permeability, and the local position and extent of<br />

plume. Naturally the aquifer location, the groundwater flow direction, flow velocity and contaminant<br />

concentrations are also fundamental in the appraisal and characterization of the site.<br />

The reactive zone of PRB must be large enough that the entire plume will pass through, moving under the<br />

natural ground-water gradient, also considering the recharge and seasonal variation.<br />

It is also necessary to place PRB in order to avoid that the contaminant plume migrates partially beyond site<br />

boundaries. Microbial activity can have beneficial or negative effects. Microbes can degrade contaminants<br />

but can also biofoul and diminish the permeability of the barrier [23].<br />

1.3 Choice of reactive media (RM) and laboratory tests<br />

The chemical or physical processes, involved in the treatment with PRB, comprise reduction, sorption,<br />

precipitation and biochemical degradation (aerobic or anaerobic) of contaminants.<br />

Sorption includes adsorption, absorption and ion exchange to reactive media. In general, adsorption is the<br />

adhesion of vapour or dissolved matter to the surface of a solid by physical and/or chemical forces,<br />

absorption is the incorporation of one substance into or through another of a different state (e.g., liquids in<br />

solids, gases in liquids) [31] [32] [8]. Remediation based on sorption phenomena usually use media like<br />

activated carbon, zeolite, peat for organic compounds and heavy metal removal.<br />

In the precipitation the contaminants pass from the soluble forms into insoluble solid states which are<br />

detained. In the degradation the pollutants are transformed in less harmful compounds by chemical or<br />

biological reactions. The type or types of processes ,mentioned above, that actually occur in PRBs and<br />

remove pollutants from solution, depend on both the pollutant and the barrier material itself [8][23].<br />

Once obtained the information from the site characterization it has to be chosen a suitable reactant.<br />

This information is extracted based on laboratory experiments.<br />

The reactive materials may be mixed with sand to facilitate the passage of the water through the barrier and<br />

its amount vary proportionally to the mass flux of contaminants requiring remediation [2][8]. Among all the<br />

factors that influence the choice of an appropriate media, the chemical composition of the contaminant is the<br />

main and most important. You have to consider if the reactive medium reacting with the detrimental<br />

compounds in the water promotes the formation of toxic by-products. The medium has to be known in depth<br />

and the ideal one, beyond to be not a source of pollutant itself, has to be inexpensive and durable (i.e.<br />

reactive over a long time scale). It has to have a size of the particles that consents the passage of the flow<br />

without constrains and it has not to be much heterogeneous, avoiding clogging [2][8][23].<br />

In addition the environmentally compatibility of reaction products and by-products has to be considered (e.g.<br />

Fe 2+ , Fe 3+ , oxides, carbonates) . In order to evaluate the suitable of the reactive materials laboratory tests<br />

concerning the rate and mechanism (including the formation of by-products) of pollutant removal are<br />

performed. These laboratory tests coupled with site characterization information are the base for the<br />

designing and the implementation of the PRB. Sometimes when there are a huge well-known data<br />

concerning the removal rate of the contaminant, the laboratory tests can be eliminated. This is not applicable<br />

when there is a mixture of pollutants.<br />

The tests should be carried out with the ground water coming from the plume.<br />

Batch studies: it is the test more appropriated for the selection of the reactive materials for the barrier. The<br />

rate in the remediation of pollutants and the longevity of different materials can be evaluated under<br />

iv


controlled condition. Typically, different samples are prepared with in each one a mixture of the reactive<br />

material to test and an aqueous solution containing dissolved contaminants. It is possible to test the reactivity<br />

of different materials simultaneously [23]. The mixtures react for a given period of time and the<br />

concentrations of the contaminants at the beginning and at the end of the contact time are measured [13].<br />

Column studies: the conditions of this test, like flow velocity, are more similar to those of the field. Based on<br />

this studies, you can obtain the residence time of the contaminant in the reactive zone that can be used , with<br />

the flow rate, to determine the thickness of the media [23]. Column tests are less cheap than batch tests but<br />

approximate better the reality and can be useful for the estimation of long term performance. In this method<br />

the reactive materials are packed in granular form into a columns fed with contaminated water [13].<br />

In synthesis laboratory tests serve to assess the effectiveness and rate of pollutants removal of potential<br />

barrier materials. In addition lab experiments evaluate the reaction products that are formed in the<br />

remediation process and their eventually toxicity.<br />

2. GEOCHEMISTRY OF BARRIER MATERIALS<br />

In the following sections, two often used barrier materials will be discussed in terms of the (geo)chemical<br />

processes that remove pollutants from solution. These materials are zero valent iron and apatite.<br />

The choice to focus the attention on these two medium is due to the fact that they engage in different types of<br />

geochemical processes leading to contaminant removal. Zero valent iron is the most used reactive medium in<br />

PRB remediation, whereas Apatite is a very promising and cheap media which can remove several metals<br />

from groundwater. Zero valent iron has the ability to degrade diverse organic and inorganic toxic<br />

compounds. Zero valent iron acts as reductant either reducing directly the contaminants in a less harmful<br />

form or also reducing pollutants which can subsequently precipitate.<br />

Apatite is an effective reactive material in PRB for the removal of toxic metal forms from solution [16][14].<br />

The apatite II provides a low but sufficient concentration of PO4 3- in solution (about 100 ppb PO 4<br />

3-<br />

or less<br />

resulting in no phosphate loading or eutrophication, particularly important in ecosystem restoration and<br />

maintenance) in order to exceed the solubility of the metal-apatite. The resulting and rapid precipitation of<br />

phases such as Pb-pyromorphite or U-autunite happens only in the presence of an existing apatite structure<br />

which acts as nucleating site or seed crystal. Apatite also acts as an excellent material for specific adsorption<br />

of most cationic metals from solution. Apatite is an excellent buffer for neutralizing acidity through PO 4<br />

3-<br />

,<br />

OH - , and substituted CO 3<br />

2-<br />

, exerting control over chemical activities of other species leading to the<br />

precipitation of oxihydroxide- and carbonate-metal phases.<br />

<strong>Environmental</strong> conditions, mineral phases present and metal concentration in solution determine the relative<br />

contribution of adsorption and precipitation to metal removal. The evaluation of which mechanism dominate<br />

at any particular site is possible with simple feasibility studies on the contaminated groundwater and soil<br />

under site conditions. [16][14]<br />

2.1 Zero Valent Iron<br />

2.1.1 Reactions and types of pollutants treated<br />

Zero valent iron (ZVI) has a demonstrated effectiveness against a broad variety of contaminants, especially<br />

towards the chlorinated aliphatic hydrocarbons (CAHs) [2][8][23].<br />

Zero valent Iron is the most common reactive medium used in PRB remediation. ZVI is instable under<br />

natural conditions and it has to be fabricated at high temperature. In the normal atmospheric oxygen<br />

condition and at low temperatures, the oxidation of ZVI is negligible by means of the formation of oxide<br />

films that act as inhibitors and do not enable the surface exposure. The standard potential of Fe 0 /Fe 2+ couple<br />

is -0.440V and this negative potential permits ZVI to act as an electron donor and reduce several redoxlabile<br />

compounds (oxidized species) [12]. The favourable thermodynamical electrochemical corrosion of<br />

ZVI, which happens in the aqueous system, is necessary for the remediation of contaminants using this<br />

material [30]. There is a passage of electrons from the iron surface to the oxidized organic pollutant, which<br />

becomes reduced and completely or less harmful. At the same time there is a production of soluble cations of<br />

the metal. As long as electron acceptors are present, corrosion processes and electron transfer can<br />

continue[2][8][23].<br />

v


Fe 0 Fe 2+ + 2e -<br />

2H + + 2e - H 2(g)<br />

Fe 0 + 2H + Fe 2+ + H 2(g) Net reaction<br />

The surface area of Iron per unit volume of pore water, so called specific surface area, plays a determining<br />

role in the rate of degradation of the contaminants. It influences directly the number of active surface sites<br />

exposed to the groundwater plume that are very important for the initialization, mediation and degradation<br />

reactions, independently from the nature of the pollutant. However an elevated specific surface can lead to a<br />

lessening of the permeability of the barrier which should be much greater than that of the surrounding aquifer<br />

layer. Other intrinsic factors, for ZVI, like the grain size and shape, the manufacturing process, the content in<br />

alloying element (P, Ni, S, C, Cr), have an additional role. The chemistry of the groundwater and the<br />

consequent influence in the corrosion process is important too: for example many dissolved species like<br />

chloride, carbonate, sulphate enhance the corrosion processes and can lead to the formation of unstable<br />

minerals[23]. The mineral precipitation is a factor of great importance in the appraisal of the performances of<br />

a reactive permeable barrier in the long term [3]. If water contains a high amount of carbonates, there is an<br />

increase in calcite (CaCO 3 ) and siderite (FeCO 3 ) precipitates. It can moreover be observed the precipitation<br />

of iron oxides and hydroxides, among which the ferric hydroxide ( Fe(OH) 3 ), the ferrous hydroxide<br />

(Fe(OH) 2 ), the magnetite (Fe 3 O 4 ) and maghemite ( Fe 2 O 3 ); these are responsible of the ” effect<br />

coating”[15][23][12]. In field applications of PRBs iron is always used in mixture with sand to avoid a<br />

complete clogging[11].<br />

Table 1. Contaminant treatable by reactive material in PRBs[23]<br />

vi


2.1.2 Treatment of halogenated organic compounds with Zero Valent Iron<br />

ZVI is one of the reactive medium more used for the treatment of numerous organic compounds and some<br />

inorganic compounds present as contaminants in the groundwater (see Table 1). In the last years several<br />

researches have been focused above all to the degradation of chlorinated compounds like TCE and PCE, by<br />

means of reactions occurring on the Fe 0 surface. In general perhalogenated hydrocarbons tend to be reduced<br />

faster than hydrocarbons less halogenated and also the dechlorination is more rapid at saturated carbons (e.g.<br />

CCl 4 ) centers than at unsaturated carbons(e.g. TCE)[15].<br />

The degradation process of the chloroether derivates can involve three steps[15]:<br />

1. the contaminant adsorption on the reactive sites of the barrier;<br />

2. reaction on the ZVI surface reaction;<br />

3. final products desorption;<br />

Nowadays the reaction between Iron and Chlorinated solvents is considered as an abiotic reductive<br />

dehalogenation [23] which can take place based on three degradation mechanisms, according to the<br />

conditions of the groundwater ,such as the amount of oxygen. This reaction occurs at the surfaces of Fe(0)<br />

that, through their corrosion and donation of electrons, permits the chlorinated hydrocarbon’s reduction and<br />

dehalogenation to hydrocarbon (non-toxic product). The resulting chloride is then dispersed in the water<br />

phase[23].<br />

The three mechanisms are[15]:<br />

A)<br />

Fe 0 Fe 2+ +2e - Anodic reaction<br />

RCl + 2e - + H + RH + Cl - Cathodic reaction<br />

Fe 0 + RCl + H + Fe 2+ + RH + Cl - Net reaction<br />

The reduction happens for transferring electrons from surface metal to the chlorurated molecule adsorbed on<br />

it.<br />

B) The ferrous ions (Fe 2+ ) yielding through the ZVI corrosion by water are further oxidated to ferric<br />

ions(Fe 3+ ) and than the chlorinated compounds are reduced. The net reaction is:<br />

2Fe 2+ +RCl+H + 2Fe 3+ + RH + Cl -<br />

2Fe 0 +O 2 +2H 2 O 2Fe 2+ + 4OH -<br />

4Fe 2+ +4H + +O 2 4Fe 3+ + 2H 2 O<br />

C) H 2 produced through the iron corrosion by the water shifts its electron to the chlorurated substance.<br />

H 2 +RCl RH +H + + Cl -<br />

It is most likely that the dehalogenation proceeds via sequence A).<br />

When the compounds to treat, like the chlorinated aliphatic compounds, and the oxygen have similar oxiding<br />

potential, they can compete for being the favoured electrons acceptor. If the oxygen is sufficiently present,<br />

Fe 2+ is further oxidized to Fe 3+ and can precipitate as hydroxide or (oxy)hydroxides at the elevated pH in the<br />

reactive zone of the ZVI[12].<br />

Aerobic system[2][12]:<br />

2Fe 0 +O 2 +2H 2 O 2Fe 2+ +4OH -<br />

4Fe 2+ +4H + +O 2 4Fe 3+ +2H 2 O<br />

Fe 3+ +3OH - Fe(OH) 3(s)<br />

Under anaerobic conditions the corrosion reaction proceeds more slowly, yields an increase in the pH (due to<br />

the consumption of H + like in the aerobic condition) and leads to the formation of ferrous (oxy)hydroxides<br />

instead of ferric (oxy)hydroxides[2][12].<br />

Fe 0 +2H 2 O Fe 2+ + H 2 + 4OH -<br />

Fe 2+ +2OH - Fe(OH) 2(s)<br />

vii


2.1.3 Zero valent iron and inorganic anions or oxyanions<br />

Elements which can be in the oxyanion form under environmental conditions include selenium, arsenic,<br />

chromium, technetium, antimony, nitrate, phosphate, sulphate. The anionic species are very soluble in water<br />

and they are not attracted to the common negative surface of the minerals in aquifer [28]. This fact implies<br />

that these oxyanions can be potentially persistent in high concentration in ground water. These elements have<br />

in common that the reduced forms (which can be generated by the ZVI) are the immobile ones. The ZVI is<br />

then used in the barrier to reduce the oxidized species in the groundwater to the reduced forms which then<br />

precipitate out of solution and are thus removed from the groundwater[23].<br />

2.1.3.1 Chromium<br />

Cr can appear commonly in environment as Cr(VI) or Cr(III). Cr(III) is relatively a micronutrient, non–toxic<br />

is adsorbed by some minerals and forms scarcely soluble hydroxide precipitates . Hexavalent Cr, instead is<br />

carcinogenic, more soluble and then more persistent and mobile[23].<br />

Several researches have been done on Cr interactions with Fe(0), and actually there are PRBs that have been<br />

specifically designed to treat Cr-contaminated groundwater with Fe(0).<br />

2-<br />

In the ground water Cr(VI) usually appears in the CrO 4 form and it is not adsorbed by aquifer materials. In<br />

the ZVI system, the reduction of Cr(VI) to Cr(III) coupled with the oxidation of Fe(0) to Fe(II)and Fe(III)<br />

and the subsequent precipitation of Fe(III)-Cr(III) oxyhydroxides or hydroxides seems to be the main<br />

mechanism. Laboratory tests have investigated some materials containing reduced iron to see which was the<br />

most effective has been seen being in the Cr(VI) removal through reduction and precipitation: the most<br />

suitable medium was found to be Fe(0). Also column tests and field applications have shown a rate of Cr(VI)<br />

reduction and precipitation by Fe(0) suitable for ground water remediation system.<br />

Sequestration of Cr(VI) provokes a steep increase in pH from initial neutral condition(6,5100mV to Eh


2.1.4 Zero valent iron and inorganic cations<br />

Like anions, inorganic cations are reduced and precipitate as meagrely soluble solids. Industrial, mine and<br />

nuclear sites are the principal sources of Hg, Cu, Tc and complex such as UO 2<br />

2<br />

, responsible of their high<br />

concentration. Laboratory experiments have shown for mercury, technetium, uranium and copper treated<br />

with ZVI a reduction and a subsequent coprecipitation within secondary precipitates.<br />

For U(VI) the reaction proposed is the following[23]:<br />

Fe 0 +UO 2+ 2(aq)<br />

Fe 2+ +UO 2 (s)<br />

UO 2 (s) (uraninite) can be amorphous or crystalline precipitate and its solubility is in the range of 10 -8 mol/l in<br />

a pH range between 4 and 14. Its solubility can enhance under oxidising conditions and below pH 4.<br />

UO(VI) is reduced to U(IV) spontaneously by elemental iron[23].<br />

2.1.5 Precipitation problems<br />

Geochemical changes such as pH increases and oxygen elimination, occur in water passing a barrier of Fe<br />

(0). These changes can lead to precipitation of secondary minerals onto the reactive surface which can<br />

influence the reactivity and permeability of the ZVI system over the time[22]. These redox conditions<br />

permits precipitation of secondary minerals from ions typically present in ground water as well as some<br />

ground water contaminants [29]. The typically secondary minerals formed in PRBs are magnetite (Fe 3 O 4 ),<br />

hematite(α-Fe 2 O 3 ), goethite (α-Fe 3+ O(OH)), lepidocrocite ( ɤFeOOH) , calcite (CaCO3), aragonite (CaCO 3 ),<br />

siderite (FeCO 3),<br />

2+ 3+<br />

green rust ([Fe (1–x) Fe x (OH) 2 ] x+ [x/n A n–·m H 2 O] x– , where x is the ratio Fe 3+ /Fe tot ), ferrous<br />

hydroxide Fe(OH) 2 , ferrous sulfide (FeS 2 ), and marcasite (FeS 2 ). In general calcium carbonates and siderite<br />

are found close to the entrance of a PRB, while magnetite, ferrous hydroxide, green rust and iron<br />

oxyhydroxides generate throughout a PRB. Accumulation of secondary minerals is responsible of loss of<br />

pore space and reactive surface area of the medium in PRBs, which can alter flow paths, residence times, and<br />

effectiveness of a PRB treatment. Due to site-specific geochemical and hydrogeological conditions, and the<br />

relatively long period over which mineral deposition occurs, it is complicated developing a general<br />

assessment of mineral precipitation in PRBs using field and/or laboratory data [29].<br />

The effects that an implementation of a ZVI barrier produces intra-wall and down gradient are a loss of<br />

dissolved oxygen, decreasing Eh, reduction in carbonate alkalinity increasing in pH value up to 9 or 10 and<br />

in Fe 2+ that can also precipitate as oxyhydroxide colloids. Loss of cementation between the grains and<br />

precipitate formation can generate mobile colloidal particles that can transport toxic substances. Deeper<br />

explorations have to be carried out to know which type of geochemical characteristic of the plume can<br />

influence the liberation and mobilization of immobilized metals and the transportation of the colloidal<br />

materials. Iron hydroxides, with the proceed of the corrosion, can form a more and more thick passivating<br />

layer on the surface of iron grains. This phenomenon gradually occludes the Iron surface and reduces its<br />

reactivity [23]. Since Ferrous (oxy) hydroxide is thermodynamically unstable, it might be further oxidized to<br />

magnetite or goethite that is non-passivating and seems to allow sufficient contaminant degradation<br />

instalments over the years [23]. Under conditions of pH neutral, it can be formed a mixed valence<br />

(Fe 2+ /Fe 3+ )compound, said “green rust”, as intermediate product of magnetite (Fe 3 O 4 ) formation from iron<br />

hydroxide. The “green rust” is stable only at low grades of oxide reduction and its oxidation leads usually to<br />

the formation of maghemite (Fe 2 O 3 ) or lepidocrocite ( ɤ FeOOH), with a prevalence in the formation of the<br />

first compound compared to the second[7]. The maghemite, differently from the magnetite, is responsible for<br />

iron passivation. If ”effect coating” prevents the Ionian ferrous passage in solution, the surface of the iron is<br />

polarized by work of Fe 2+ ion and diminishes therefore the tendency of the iron to corrode itself. It has also<br />

been seen that, if the concentration of organic chlorinated compounds increases, the half life of the polluting<br />

agents increases too. That depends on the increasing of the passivated iron surface and on the emphasized<br />

saturation of the reaction site. The passivation phenomenon is influenced moreover from the composition of<br />

the iron [10]. The mineral precipitation can involve, at the same time of reactivity reduction, also various<br />

negative impacts on the hydraulic conditions of the barrier [3]. The filling of the pores can raise the<br />

heterogeneity inside the barrier, leading therefore to the formation of preferential paths [9], increasing of<br />

fluid speed and meaningful lessening of the time of residence inside of the PRB. Today there are studies<br />

describing the performances in the long term of the PRB containing zerovalent iron.<br />

ix


2.2 Apatite<br />

2.2.1 Structure<br />

Apatite is a microporous mineral described with general formula Ca 5 (PO 4 ) 3 (OH,F,Cl), or more accurately by<br />

the unit cell contents [Ca 4 ][Ca 6 ][(PO 4 ) 6 ][F] 2 . [Ca 4 ][Ca 6 ][(PO 4 ) 6 ][F] 2 is composed by CaO 6 columns linked<br />

together with PO 4 groups in order to form “a hexagonal network like a honeycomb with channels extending<br />

right through the structure in c direction “ [25].<br />

This one-dimensional tunnel structure is very stable and strong, and is chiefly due to the arrangement of<br />

calcium and phosphate. The structure can be considered a tunnel structure with walls composed of cornerconnected<br />

CaO 6 and PO 4 polyhedra as relatively invariant units. Compared to fluorapatite, in the hydroxyl<br />

apatites the presence of OH - , that is a little larger than F - , is responsible for the resulting expanded structure.<br />

The microporus structure with tunnels filled to Calcium and anions (OH,F) leads to an adjustment that best<br />

satisfies bond-length requirements [25]. Little changes in the ionic radii of the tunnel atoms cause the<br />

expansion or contraction of the channel. The channels can accommodate different contents, accepting large<br />

cations of different valence through the introduction of framework counter ions. Apatites are reversible ion<br />

exchangers for some anions and cations, are stable in the subsurface and do not induce microbial<br />

blooms[25].<br />

2.2.2 Apatite II<br />

2.2.2.1 Reactions of apatite and metals<br />

Apatite II has the general formula [Ca 10-x Na(PO 4 ) 6-x (CO 3 ) x (OH) 2 where x10 -20 [16] .<br />

Metals in solution are immobilized on the apatite mineral by surface sorption (main mechanism for most<br />

metals), precipitation (main mechanism for U, Pu, Pb, lanthanides) or co-precipitation (transition metals).<br />

It has particular characteristics that render it fit for optimal performance in the field, namely: its substituted<br />

2-<br />

CO 3 and sodium that destabilize the structure and make the material more soluble, no substituted F, low<br />

trace metal concentration, poor crystallinity (>90% amorphous) and high microporosity [6]. These properties<br />

influence the kinetics and solubility. F as minor constituent in the structure raises lattice stability and<br />

decreases solubility and dissolution rate. Instead carbonate has the opposite effect[16]. Differences in the<br />

performance among various apatite phases result from differences in those properties which influence the<br />

kinetics and solubility, e.g., crystallinity and minor element chemistry. A higher degree of crystallinity<br />

decreases solubility and dissolution rate, making the apatite less reactive and less effective, whereas lower<br />

crystallinity increases solubility. Thus, the amorphous form of the solid is the most reactive. The presence of<br />

F as a minor constituent in the apatite structure increases lattice stability, decreasing solubility and<br />

dissolution rate. The presence of carbonate as a minor constituent in the apatite structure decreases lattice<br />

stability, increasing solubility and dissolution rate[16].<br />

Phosphate-Induced Metal Stabilization (PIMS) is a remediation technology that stabilizes a broad range of<br />

radionuclides and metals like Pb, U, Cd, Zn, Cu, and Al which are bound into new phosphate minerals and<br />

low solubility phases. The metal–phosphate phase is very stable over geological time because of its low<br />

solubility products ( K sp ), as shown in table 2 [6][14]. These metal-phosphate products are<br />

thermodynamically stable over a broad range of environmental conditions, and precipitate rapidly, thus<br />

ensuring a stable and long term immobilization of metal pollutants. They have great durability, low solubility<br />

and are stable over a wide range of conditions [14].<br />

x


Table2-Solubility products of metal phosphates [27]<br />

Metals and apatite react very quickly ([17], [20], [26], [4], [5], [21])on molecular scale, but at a macroscopic<br />

dimension, limiting parameters like grain size, flow rate, barrier design, influence the efficiency with which<br />

dissolved metals come into contact with the surface of the reactive media. Apatite II has treated successfully<br />

contaminated soils, groundwater and wastewater for Pb, U, Cd, Zn, Al stabilizing between 5% and 50 % of<br />

its weight in metals depending upon the metal and the environmental conditions[16] . Pb,Cd, and Zn are<br />

sorbed by apatite with different mechanisms. Pb is primarily removed with this mechanism: the dissolution<br />

of the apatite that provides PO 4<br />

3-<br />

and the following precipitation of hydroxyl fluoropyromorphite on Apatite<br />

surface. Minor otavite (CdCO 3 ) precipitation was observed in the interaction of the apatite with aqueous Cd.<br />

However other sorption mechanisms, such as surface complexation, ion exchange, and the formation of<br />

amorphous solids, are primarily responsible for the removal of Zn and Cd [5].<br />

There are four general factors that aid in the effective sequestration of metals by apatite II, depending upon<br />

the type of metal and its concentration and the groundwater chemistry: 1) heterogeneous nucleation; 2)<br />

buffer acidity to pH 6.5 to 7; 3) surface chemi-adsorption; 4) biological stimulation; [21]<br />

2.2.2.1.1 Heterogeneous nucleation<br />

A small, but sufficient, amount of phosphate is provided to solution in order to overtake the solubility limits<br />

of the metal-apatites.<br />

The (K sp ) of the resulting metal-apatites is very low for the metals Pb, U, Cd, Zn, Cu and Al and in particular<br />

for Pb that is equal to K sp =10 -167 [21].<br />

Pb-pyromorphite can precipitate only through heterogeneous nucleation, namely, a seed crystal with the<br />

apatite crystal structure is necessary for the precipitation , unless Pb concentrations exceed about 10 ppm<br />

( not frequent in environmental conditions) [18][19].<br />

The Apatite II amorphous structure is relatively reactive and supplies a slight excess of phosphate ions to<br />

solution. The random nanocrystal inclusions of crystalline apatite, provide the seeds for nucleating the<br />

precipitates.<br />

Pb in the system precipitates only as microscope Pb-pyromorphite minerals which over the time will grow<br />

and join together eventually forming larger mineral bunches [22]. The presence of apatite II- supplied<br />

phosphate in this process ,that can take many years, keeps the concentration of Pb in solution extremely low,<br />


limits[16]. The degree of protonation, namely the number of hydrogen ions attached to the PO 4<br />

3-<br />

, in the<br />

intermediate reactions, depends upon the solution pH. The example above is for the range of acid soils or<br />

acid mine drainage, pH


phases by precipitation that it has resulted being a mixture of sphalerite and recrystallized apatite. Within the<br />

first few feet of the PRB Pb and Cd vanish completely from solution, Zn concentration instead diminishes<br />

continuously along the barrier, finally dropping to about 0.1 mg/L or below once exited from it.<br />

In order to understand which mechanisms are operating and how much time the barrier can last, analysis of<br />

material captured from barrier and geochemical modelling using MINTEQ and PHREEQ were performed.<br />

MINTEQ indicates that pyromorphite and sphalerite (ZnS) are the steadiest phases within the barrier for Pb<br />

and Zn. These results are based to the dates displayed in the table 3. The other metals such as Mn,Cu, Al and<br />

U are also being reduced from ppm/ subppm level to the pbb level or below detection. This indicates that<br />

biological reduction, pH buffering, precipitation and surface adsorption all act in the PRB. Cd can undergo<br />

adsorption onto the Apatite II or precipitate as a sulphide similar to Zn.<br />

Table 3- Changes in some groundwater constituents entering/exiting the Apatite II PRB in August 2002 [14]<br />

2.2.2.3 Benefits of use of Apatite II [6]<br />

The use of Apatite II is a new remediation technology that has several advantages.<br />

First at all Apatite II can sequester most heavy metals and radionucleotides for geologically long time<br />

periods. Many metals and radionuclide contaminants precipitate as mineral phases in which the metals are<br />

not bioavailable. Apatite II is one of the best non-specific surfaces sorbent for species that do not precipitate<br />

as a separate phase and is the most cost-effective reactive media for most metals and radionuclides, e.g.,<br />

immobilizes up to 20% of its weight in Pb, U, Pu and perhaps other metals.<br />

Apatite II can be mixed into contaminated soil or waste, emplaced in PRB or used as a disposal liner and can<br />

be combined with most other reactive media e.g., grout, bentonite, zero valent iron, and other remediation<br />

technologies, e.g., bioremediation, etc.<br />

xiii


3. CONCLUSIONS AND REMAINING RESEARCH QUESTIONS<br />

The feasibility of PRB’s installations depends on the chemical, geological and environmental settings of the<br />

PRB’s capture zone. The reactivity of the barriers can be impaired by the remediation processes themselves<br />

(e.g. oxidation), by the reaction products like for example precipitates and by exhaustion of sorption<br />

capacity[11]. The types of materials used in barriers are those changing redox potential (e.g. zero valent iron<br />

– degradation of chlorinated hydrocarbons), those causing precipitation, materials with high sorption<br />

capacity, those releasing nutrients/oxygen to enhance biological degradation [12];<br />

Zero Valent Iron is the reactive medium in Permeable Reactive Barrier system most used because of its vast<br />

capacity to remediate a large number of contaminants through its corrosion and donation of electrons for the<br />

reduction of the pollutants in a harmless state. Hence, are available numerous terms of comparison from<br />

which can be extrapolated the guide lines for the planning and the emplacement of new installations[15].<br />

ZVI is very effective towards the chlorinated aliphatic hydrocarbons acting as reductant and degrading them<br />

through a dehalogenation. For the contaminants in the form of inorganic cations and anions, their reduction<br />

and their consequent precipitation are the processes involved when is utilized the ZVI as reactant[23].<br />

To date the mechanisms of remediation of ZVI towards several compounds are fairly noted and they have<br />

been studied in depth. Not completely clear and requiring further studies are the long term effects of some<br />

precipitates like maghemite (Fe 2 O 3 ), ferric hydroxide ( Fe(OH) 3 ), ferrous hydroxide ( Fe(OH) 2 , a mixed<br />

valence (Fe 2+ /Fe 3+ )compound, said “green rust”, on the maintenance of the PRB’s functionality.<br />

Apatite II is a particular configuration of apatite that appears very suitable for the remediation of<br />

groundwater contaminated by metals, including uranium and plutonium [14].<br />

In the case study considered in this paper, apatite II has demonstrated high efficiency in the abatement of the<br />

heavy metals Pb, Cd and Zn. A not negligible benefit in the utilization of apatite II as medium in PRB is the<br />

fact that it has not environmental impacts and there is no phosphate loading to the environment due to its low<br />

solubility, K sp


4. AKNOWLEDGEMENT<br />

Particular thanks to my tutor who has supported me with patience in developing this term paper, giving me precious<br />

hints and councils. Further thanks to my reviewers.<br />

5. REFERENCES<br />

[1] A Citizen’s Guide to Permeable Reactive Barriers – EPA 542-F-01-005 – April 2001 – www.epa.gov/superfund/sites -www.<br />

cluin.org.<br />

[2]- Long-term Performance of Permeable Barriers used for the Remediation of contaminated Groundwater - PEREBAR EVK1-CT-<br />

1999-00035- 5 th Framework Programme Research and Technological Development Project – Literature Review: Reactive<br />

Materials and Attenuation Processes for Permeable Reactive Barriers by National Technical University of Athenes, Department of<br />

Mining And Metallurgical Engineering, laboratory of Mettallurgy, GR-157 80 Zografos, Athens, Greece- August 2000.<br />

www.perebar.bam.de/PereOpen/<strong>pdf</strong>Files/Review_Reactive_Materials.<strong>pdf</strong><br />

[3] Patricia D.Mackenzie, David P.Horney and Timothy M. Sivavec – Mineral precipitation and porosity losses in granular iron<br />

columns Journal of Hazardous Materials. Volume 68, Issues 1- 12 August 1999, Pages 1-17<br />

[4] Chen, X., J. Wright, J. L. Conca and L. M. Peurrung. 1997a. “Effects of pH on heavy metal sorption on mineral apatite.”<br />

Environ. Sci. Technol. 31: 624-631.<br />

[5] Chen, X., J. Wright, J. L. Conca and L. M. Peurrung. 1997b. “Evaluation of heavy metal remediation using mineral apatite.”<br />

Water, Air and Soil Pollution. 98: 57-78.<br />

[6] Conca, J. L., N. Lu, G. Parker, B. Moore, A. Adams, J. Wright and P. Heller. 2000. “PIMS–Remediation of Metal Contaminated<br />

Waters and Soils.” In G.B. Wickramanayake, A.R.Gavaskar, J.T. Gibbs and J.L. Means (Eds.), Remediation of Chlorinated and<br />

RecalcitrantCompounds, vol. 7. p. 319-326. Battelle Memorial Inst., Columbus, OH.<br />

[7] Cornell,R.M. and Schwertmann, U., 1996. The iron oxides. VCH Publishers: New York<br />

[8] D.Jirasko – Problems connected with use of permeable Reactive Barriers for groundwater treatment–Czech Technical<br />

University, Prague, Czech Republic – http://www.cgts.cz/5e_journal_documents/jirasko.<strong>pdf</strong><br />

[9] Eykholt, G.R., Elder, C.R., Benson, C.H., 1999. Effects of aquifer heterogeneity and reaction mechanism uncertainty on a<br />

reactive barrier. Journal of Hazardous Materials 68, 78-101.<br />

[10] Farrell, J., Kason, M., Melitas, N., Li, T., 2000. Investigation of the long-term performance of zero-valent iron for reductive<br />

dechlorination of trichloroethylene. <strong>Environmental</strong> Science Technology vol.34, n°3, 514-521.<br />

[11] Franz–Georg Simon, Tamás Meggyes and Torge Tünnermeier, Kurt Czurda, Karl Ernst Roehl – Long-term behaviour of<br />

permeable reactive barriers used for the remediation of contaminated groundwater - Radioactive Waste Management and<br />

<strong>Environmental</strong> Remediation – ASME 2001.<br />

[12] Franz – George Simon, Tamás Meggyes – Removal of organic and inorganic pollutants from groundwater using permeable<br />

reactive barriers – published in Land Contamination & Reclamation, Vol. 8, Issue 2, 103-116 (2000).<br />

[13] Gianluca Ambrosini – Reactive Materials for Subsurface Remediation through Permeable Reactive Barriers. Diss. <strong>ETH</strong><br />

No.15784 (2004).<br />

[14] James L. Conca, Judith Wright – An Apatite II permeable reactive barrier to remediate groundwater containing Zn, Pb and Cd<br />

– Applied Geochemistry 21 (2006) 2188-2200<br />

[15] Jenny Campagnol, Serena Ceola, Chiara Scarpa – Relazione: Le barriere reattive permeabili a ferro zerovalente - Corso di<br />

laurea specialistica in ingegneria per l’ambiente e il territorio, corso di bonifica dei terreni contaminati A.A. 2006-2007,<br />

professore: Raga Roberto – Facoltà di ingegneria, università degli studi di Padova (on – line)- www.image.unipd.it.<br />

[16] Wright, J., Rice, K. R., B. Murphy, and J. Conca (2004) “PIMS Using Apatite II: How It Works To<br />

Remediate Soil and Water,” in Sustainable Range Management-2004. Proceedings of the Conference on<br />

Sustainable Range Management, January 5-8, 2004, New Orleans, www.battelle.org/bookstore, ISBN 1-<br />

57477-144-2, B4-05.<br />

[17] Koeppenkastrop, D. and E. J. De Carlo. 1990. “Sorption of rare earth elements from seawater onto synthetic mineral phases.”<br />

Chem. Geol. 95: 251-263.<br />

xv


[18] Lower, S. K., P. A. Maurice, S. J. Traina and E. H. Carlson. 1998. “Aqueous lead sorption by hydroxylapatite: Applications of<br />

atomic force microscopy to dissolution, nucleation and growth studies.” American Mineralogist. 83: 147-158.<br />

[19] Lower, S. K., P. A. Maurice and S. J. Traina. 1998b. Simultaneous dissolution of hydroxylapatite and precipitation of<br />

hydroxypyromorphite: Direct evidence of homogeneous nucleation. Geochim Cosmochim. Acta. 62: 1773-1780.<br />

[20] Ma, Q. Y., T. J. Logan and S. J. Traina. 1995. “Lead immobilization from aqueous solutions and contaminated soils using<br />

phosphate rocks.” Environ. Sci. Technol. 29: 1118-1126.<br />

[21] Manecki, M., P. A. Maurice and S. J. Traina 2000. “Kinetics of aqueous Pb reaction with apatites.” Soil Science. 165(12): 920-<br />

933.<br />

[22] Morse, J. W. and W. H. Casey. 1988. “Ostwald processes and mineral paragenesis in sediments.” American Journal of Science.<br />

288: 537-560.<br />

[23] Robert M.Powell, Robert W. Puls, David W.Blowes, John L.Vogan, Robert W.Gillham, Patricia D.Powell, Dale Schultz,<br />

Timothy Sivavec, Rich Landis - Permeable reactive barrier technologies for contaminant remediation- <strong>Environmental</strong> Protection<br />

Agency, Office of research and development, Washington DC 20460, Office of Solid Waste and Emergency Response,<br />

Washington DC 20460, EPA/600/R-98/125, September 1998.<br />

[24] Ruby, M. V., A. Davis and A. Nicholson. 1994. “In situ formation of lead phosphates in soils as a method to immobilize lead.”<br />

Environ. Sci. Technol. 28: 646-654.<br />

[25] Tim White, Cristiano Ferris, Jean Kim and Srinivasan Madhavi – Apatite – An Adaptive Framework Structure – School of<br />

Materials Engineering, Nanyang Technological University, Singapore 639798 - 2004.<br />

[26] Wright, J. V., L. M. Peurrung, T. E. Moody, J. L. Conca, X. Chen, P. P. Didzerekis and E. Wyse.1995. In Situ Immobilization of<br />

Heavy metals in Apatite Mineral Formulations, Technical Report to the Strategic <strong>Environmental</strong> Research and Development<br />

Program, Department of Defense, Pacific Northwest Laboratory, Richland, WA, 154 p.<br />

[27] James Conca, Judith Wright, 2004 - PIMS-Apatite II treatment of Metal-Contaminated Water. Minutes of the Permeable<br />

Reactive Barriers Action Team. www.rtdf.org/PUBLIC/PERMBARR /minutes/102704/<strong>pdf</strong>/conca.<strong>pdf</strong><br />

[28] Werner Stumm, James J. Morgan – Aquatic Chemistry, Chemical Equilibria and Rates in natural waters – Third edition. John<br />

Wiley and Sons Inc. New York USA.<br />

[29] Li, L. and C. Benson, Univ. of Wisconsin-Madison– Reactive transport in the saturated zone: case histories for permeable<br />

reactive barriers - Water Encyclopedia, Vol 2: Groundwater. John Wiley and Sons, New York. ISBN: 0-471-73683-X, 23 pp,<br />

2005<br />

[30] Nichole Ott - Permeable Reactive Barriers for inorganics - 2000 National Network of <strong>Environmental</strong> Management Studies<br />

Fellow for U.S. <strong>Environmental</strong> Protection Agency - Office of Solid Waste and Emergency Response - Technology Innovation<br />

Office - Washington, DC - http://www.cluin.org<br />

[31] U.S. <strong>Environmental</strong> Protection Agency - 40 CFR Part 247 - Comprehensive Guideline for Procurement of Products Containing<br />

Recovered Materials; Proposed Rule - Federal Register / Vol 63. No. 165/ Wednesday. August 26 1998/ Proposed rules.<br />

http://www.epa.gov/fedrgstr/EPA-WASTE/1998/August/Day-26/f22793.<strong>pdf</strong><br />

[32] http://www.epa.gov/OCEPAterms/aterms.html<br />

xvi


Response of Coccolithophorids and Diatoms to Climate<br />

Change<br />

Term Paper in Biogechemistry and Pollutant Dynamics<br />

By Fabio Marconi<br />

Tutors: Dr. Jacqueline Flückiger and Prof. Nicolas Gruber<br />

Handed in: June 22. 2007<br />

Abstract<br />

Among other effects, climate changes induced by increased atmospheric CO 2 levels affect the<br />

species composition of marine phytoplankton. Most of the primary production of the phytoplankton<br />

resulted from the activity of two functional groups: coccolithophorids and diatoms. Public concern<br />

has risen about how the expected changes in environmental factors will affect the marine<br />

productivity. Therefore, impact of carbonate chemistry, nutrient and light availability on the<br />

ecophysiology of these two groups, have been widely assessed. This paper will focus on how<br />

ecophysiological differences between these two groups may lead to different responses in front of<br />

the climate change. A review of the literature shown that coccolithophorids may benefit from the<br />

environmental changes (principally the reduction of mixed layer depth) in particular in higher<br />

latitudes and become more competitive at the expense of diatoms, which was dominant at these<br />

latitudes. However, in tropics and mid-latitudes the marine phytoplankton composition will more or<br />

less remain the same and coccolithophorids continue to prevail on diatoms. Because of the<br />

important role of coccolithophorids in the marine carbon cycle, shift in ratio of this calcifying<br />

phytoplankton group versus non-calcareous primary producers seems to affect the partitioning of<br />

CO 2 between ocean and atmosphere having consequently important feedback on future climate<br />

change.<br />

Table of contents<br />

1. INTRODUCTION ........................................................................................................................................................................- 1 -<br />

2. GLOBAL CHANGES DUE TO RISING ATMOSPHERIC PCO 2 ON OCEAN WITH PARTICULAR ATTENTION ON<br />

TROPICS AND SUBPOLAR REGIONS.......................................................................................................................................- 2 -<br />

2.1 DIRECT EFFECT: CHANGES IN CARBONATE CHEMISTRY............................................................................................................... - 2 -<br />

2.2 INDIRECT EFFECT: INCREASED STRATIFICATION ......................................................................................................................... - 3 -<br />

2.2.1 Effects of climate warming in tropics and mid-latitudes compared to higher latitudes ..................................................- 4 -<br />

3. ECOPHYSIOLOGY OF DIFFERENT PHYTOPLANKTON SPECIES: COMPARISON BETWEEN<br />

COCCOLITHOPHORIDS AND DIATOMS.................................................................................................................................- 4 -<br />

3.1 GROWTH PROCESSES................................................................................................................................................................. - 5 -<br />

3.1.1 Light availability and growth..........................................................................................................................................- 5 -<br />

3.1.2 Nutrient supply and growth.............................................................................................................................................- 6 -<br />

3.1.3 Dissolved inorganic carbon (DIC) and growth...............................................................................................................- 8 -<br />

3.1.4 Temperature and growth...............................................................................................................................................- 10 -<br />

3.2 LOSS PROCESSES..................................................................................................................................................................... - 10 -<br />

4. RESPONSE OF COCCOLITHOPHORIDS AND DIATOMS TO PREDICTED GLOBAL CHANGES CONSIDERING<br />

THEIR SPECIFIC ECOPHYSIOLOGY .....................................................................................................................................- 11 -<br />

4.1 TROPICS AND MID-LATITUDES ................................................................................................................................................. - 12 -<br />

4.2 HIGHER LATITUDES................................................................................................................................................................. - 13 -<br />

4.3 ROLE OF GROWTH AND LOSS PROCESSES IN DETERMINING THE RESPONSE OF COCCOLITHOPHORIDS AND DIATOMS TO THE GLOBAL<br />

CLIMATE CHANGES ....................................................................................................................................................................... - 14 -<br />

4.4 EFFECTS ON BIOLOGICAL CARBON PUMP.................................................................................................................................. - 15 -<br />

5. CONCLUSION...........................................................................................................................................................................- 16 -<br />

6. LITERATURE............................................................................................................................................................................- 16 -<br />

7. ANNEX........................................................................................................................................................................................- 18 -


1. Introduction<br />

Since the industrial revolution rising atmospheric pCO 2 induced global changes in the environment.<br />

In the past 20 million years the CO 2 level in the atmosphere seems to have never exceeded 300 parts<br />

per million (ppm), fluctuating between 180 ppm during glacial periods and 280 ppm during<br />

interglacial periods (Rost and Riebesell, 2004). Today the pCO 2 level in the atmosphere reaches<br />

about 370 ppm and this concentration is expected to double until the end of this century. Due to<br />

these large-scale perturbations induced by human activities environmental condition change at an<br />

unprecedented rate. To predict impacts of these global changes on marine ecosystems (chapter 4),<br />

and more precisely on the phytoplankton composition and succession, a first requirement is to<br />

predict changes in abiotic factors in the ocean; like carbonate chemistry, nutrient supply and light<br />

availability, due to rising atmospheric CO 2 level (chapter 2). Secondly, to asses the response of<br />

phytoplankton to environmental changes, the physiological characteristics should be examined<br />

(chapter 3). The marine pelagic system is very complex and represents one of the largest<br />

ecosystems on our planet. Because the whole ecosystem consists of more than 5000 phytoplankton<br />

species it will be impossible to discuss all details and relevant key species have to be identified.<br />

Within all these species only few taxonomic groups are responsible for most of the primary<br />

production of the system (Rost and Riebesell, 2004). One of these so-called phytoplankton<br />

functional groups is represented by siliciers. To this group belong diatoms, one of the most<br />

successful eukaryotic algae in the contemporary ocean, which is responsible for around 40 % of the<br />

net primary production and 50 % of the organic carbon exported to deep sea (Falkowski et al.,<br />

2004). Diatoms dominate microphytoplankton (20-200 µm) and have a unique absolute requirement<br />

for orthosilicic acid used to form strong opal shells called frustules. The second important group<br />

considered in this term paper are calcifying phytoplanktons, which are dominated by<br />

coccolithophorids. These are smaller than diatoms and belong to nanophytoplankton (5-10 µm).<br />

They are characterized by an outer sphere of calcite plates known as coccoliths. Emiliania huxleyi is<br />

the most abundant coccolithophorids and also the most productive lime-secreting organism<br />

(Sarmiento and Gruber, 2006). Coccolithophorids, performing the calcification, can affect<br />

significantly the oceanic carbon cycle. Know their future abundance relative to non-calcifying will<br />

give important information on CO 2 partitioning between atmosphere and ocean and finally on<br />

carbon dioxide level in atmosphere.<br />

Figure 1 Phytoplankton functional<br />

groups considered in this term<br />

paper: silicifiers (diatom, left) and<br />

calcifiers (coccolithophorids, in<br />

this case Emiliania huxleyi, right).<br />

Pictures have not the same<br />

magnitude: the diameter of<br />

diatom is about 60 µm, while E.<br />

huxleyi is 10 times smaller<br />

(pictures are from:<br />

http://www.salem.k12.va.us/staff/j<br />

wright/vocabulary/diatom2.jpg;<br />

http://www.soc.soton.ac.uk/soes/st<br />

aff/tt/eh/pics/cocco9.jpg)<br />

- 1 -


2. Global changes due to rising atmospheric pCO 2 on ocean<br />

with particular attention on tropics and subpolar regions<br />

The effects of rising atmospheric pCO 2 on the surface ocean can be distinguished in direct and<br />

indirect effect. The former occur since the surface layer of the ocean and the atmosphere constantly<br />

exchange CO 2 and consequently change in the atmospheric CO 2 level will affect the surface ocean<br />

carbonate system. The latter are a consequence of the global warming caused by increase<br />

atmospheric CO 2 level, a greenhouse gas; and consist on changes in nutrients and light availability<br />

due to stratification of the upper ocean.<br />

2.1 Direct effect: changes in carbonate chemistry<br />

Carbon dioxide obeys Henry’s law, which means that an increase in the atmospheric pCO 2 will be<br />

reflected in the concentration of CO 2 in the surface oceans. Dissolved CO 2 combines with water<br />

forming carbonic acid (H 2 CO 3 ). This weak acid releases protons (H + ) into solution by dissociating<br />

in bicarbonate (HCO 3 - ) and to a lesser extent in carbonate ions (CO 3 2- ) according to the logarithm of<br />

acid dissociation constants (pK a -value). Also a small fraction of the carbonic acid as well as<br />

dissolved carbon dioxide remains in solution. The result of dissolving carbon dioxide in seawater is<br />

a decrease in pH. The pH of pristine water measures about 8-8.3 (Doney, 2006a). However, the<br />

uptake of anthropogenic CO 2 during the last 200 years (oceans seem to have absorbed half of the<br />

CO 2 produced by human activities) has caused a decrease of pH by 0.1 unit, which corresponds to a<br />

30 % increase in concentration of H + (Raven, 2005). If the global emission of anthropogenic CO 2<br />

continue to rise with the current trends the concentration of protons in the surface ocean will triple<br />

until 2100 and the pH will drop by 0.5 units (Raven, 2005). Changing pH also the speciation of<br />

carbonate species will be shifted: a decrease of pH in the range of pristine seawater will increase the<br />

fraction of dissolved CO 2 , decrease the fraction of carbonate ions (CO 3 2- ), while the large pool of<br />

bicarbonate (HCO 3 - ) remains more or less constant (Figure 2). More quantitative, considering the<br />

expected increase in atmospheric CO 2 until the end of this century, the concentration of CO 3<br />

2-<br />

will<br />

have dropped to the half while the dissolved CO 2 will triple relative to pre-industrial values (Figure<br />

2).<br />

Figure 2 Fraction of the three inorganic species of CO 2 dissolved in seawater versus pH (left, Raven, 2005);<br />

course of seawater pH, dissolved CO 2 and CO 3 2- concentrations assuming a “business as usual” anthropogenic<br />

CO 2 emission scenario until the year 2100 (dashed lines represent the changes in carbonate chemistry if CO 2<br />

emission decreased as prescribed in the Kyoto Protocol) (right, Rost and Riebesell, 2004)<br />

- 2 -


2.2 Indirect effect: increased stratification<br />

The density is the main parameter causing stratification of ocean and is a function of temperature,<br />

salinity and pressure (ρ = f(T, S, p)). In order to evaluate how the density of seawater pro<strong>file</strong> will<br />

change as a result of increasing atmospheric level of CO 2 one has to consider the modellingpredicted<br />

variations in sea temperature and salinity. Knowing the density pro<strong>file</strong> of the ocean,<br />

prediction on the stratification will be possible.<br />

Global warming increases the sea surface temperature (SST) at all latitudes (Figure 3a). The sea<br />

surface salinity (SSS, Figure 3b) response to global warming reflects the overall enhancement of the<br />

hydrologic cycle, due to the increased capacity of warmer air (Manabe, 1991; reviewed in<br />

Sarmiento et al., 2004). The high evaporation in subtropical regions causes an increase of the SSS,<br />

while at higher latitudes the greater rainfall (Sarmiento et al., 2004) and enhanced freshwater input<br />

from melting ice cover (Figure 3c) lower surface layer salinity. Assuming a rule of thumb, which<br />

establishes an increase in seawater density by one unit when temperature increases by 5 °C or when<br />

salinity increase by one unit (Sarmiento and Gruber, 2006), it can be assess that the changes in<br />

density (Figure 3) seem to be affected mainly by temperature.<br />

Figure 3 Response of the physical ocean-atmosphere system to climate change (warming simulation minus<br />

control) calculated with six different coupled climate models (called AOGCMs: Atmosphere-Ocean General<br />

Circulation Models). The figure shows averaged over the period 2040 to 2060 by different latitudes. a) sea<br />

surface tempature (SST) in °C, b) sea surface salinity (SSS) in practical salinity units (PSU), c) ice cover as the<br />

ocean area of maximum wintertime sea ice extent in 10 12 m 2 per degree, d) sea surface potential density (SSD), e)<br />

wintertime maximum mixed layer depth in m. For a extensive description of the parameters considered by each<br />

coupled climate model consult Sarmiento et al. (2004).<br />

Figure 4 Effects of increased<br />

atmospheric pCO 2 on the upper layer<br />

of the oceans. Increased stratification<br />

reduced mixing layer depth, which<br />

causes a reduction of nutrients input<br />

from deep ocean and an increased<br />

light availability (Rost and Riebesell,<br />

2004).<br />

- 3 -


The increased vertical stability of the ocean pro<strong>file</strong> reduces the mixed layer depth. Assuming that<br />

most of the nutrients (particularly macronutrients) are provided by cold, nutrient-rich, deep ocean, a<br />

shoaling of the upper mixed layer will reduce the nutrients supply (Sarmiento et al., 2004; Rost and<br />

Riebesell, 2004; Figure 4). Also the light availability will increased in response to changes in mixed<br />

layer thickness and in cloudiness (Sarmiento et al., 2004; Rost and Riebesell, 2004; Figure 4).<br />

2.2.1 Effects of climate warming in tropics and mid-latitudes compared to<br />

higher latitudes<br />

The tropics and the mid-latitude regions are<br />

already characterized by water columns, which<br />

are thermal-stratified and consequently are<br />

nutrient-limited because of reduced vertical<br />

mixed layer depth. Climate warming will<br />

further increase the stratification inhibiting<br />

vertical mixing and therefore reducing the<br />

nutrient supply coming from deeper nutrient-<br />

rich layers (Figure 5 a). At higher latitudes the<br />

mixing layer depth is often deeper than the<br />

euphotic zone, so that phytoplankton is carried<br />

to layers, where the light-limited conditions<br />

occur. The predicted global warming will<br />

increase the stratification due to rising sea<br />

surface temperature but also due to increased<br />

Figure 5 Effects of increased stratification due to precipitation and melting of ice, which reduced<br />

climate change in the tropics and mid-latitudes (a) the sea surface salinity. The shoaling mixed<br />

compared with them occurred at higher latitudes (b)<br />

layer depth at high latitudes may increase<br />

(Doney, 2006b).<br />

productivity of phytoplankton, because of<br />

reduced light limitation condition (Figure 5 b).<br />

At lower latitudes, on the other hand, phytoplankton productivity will decline substantially, as a<br />

result of increased nutrient limitation. (Doney, 2006b)<br />

3. Ecophysiology of different phytoplankton species:<br />

comparison between coccolithophorids and diatoms<br />

In order to asses the response of two plankton functional groups – calcifiers and silicifiers – with<br />

regard to the predicted global environmental changes, it is crucial to know the specific<br />

physiological characteristics of each plankton group. Local environmental factors select specific<br />

organisms affecting the competitive advantage of determinate groups or species of phytoplankton.<br />

With detailed information about the physiological and ecological characteristics of the individual<br />

phytoplankton species and predictions of the future environmental changes it is possible to<br />

speculate about changes in the distribution and succession of phytoplankton species.<br />

The ecological success of a phytoplankton species will be mainly determined by its ability to<br />

optimise the balance between growth and loss processes. Availability and optimal use of essential<br />

resources like light and nutrient (carbon, nitrogen, phosphorous and plus micronutrient such as iron<br />

and zinc) are the major factors controlling growth processes while loss processes can be caused by<br />

cell sinking, cell mortality due to grazing, viral and parasite infection as well as autolysis (Rost and<br />

- 4 -


Riebesell, 2004; Sarmiento and Gruber, 2006). This chapter is principally subdivided into these two<br />

processes.<br />

Before starting the description of the physiological issues of coccolithophorids (calcifiers) and<br />

diatoms (silicifiers) it is important to emphasize that most of the data on phytoplankton presented in<br />

this term paper are based on laboratory experiments, which are normally conducted on individual<br />

species easy to culture. One has to consider that data of singular species are not necessarily<br />

characteristic for a whole phytoplankton functional group (Le Quéré et al., 2005). Another<br />

important point is that experiments may not be really representative for the behaviour of a species in<br />

a complex community in the ocean consisting of many species (Sarmiento and Gruber, 2006). More<br />

in detail, Sarthou et al. (2005) reviewed many experiments on different diatoms species so that<br />

average data of this group of silicifiers are usually available. On the other hand for<br />

coccolithophorids lots of experiments are done on Emiliania huxleyi, but for other<br />

coccolithophorids the physiological characteristics are poorly described. As a result many<br />

coccolithophorids issues described in this paper are based principally on E. huxleyi, which is,<br />

however, the most important bloom-forming coccolithophorids in present geological period<br />

(Iglesias-Rodriguez et al., 2002).<br />

3.1 Growth processes<br />

3.1.1 Light availability and growth<br />

Vertical mixing of the upper layer of ocean modifies the light intensity. Phytoplankton species have<br />

consequently experienced high variability in light conditions. Differences in photosynthetic<br />

characteristics between phytoplankton species cause specific affinity to light or ability to deal with<br />

light irradiance variability. In order to evaluate the photosynthesis physiology and, more specific,<br />

the efficiency of light utilisation, photosynthetic rate versus irradiance curves (PI-curves) are widely<br />

used. PI-curves represent the response of photosynthesis at various light intensities. Typically these<br />

curves can be subdivided in three regions: light-limited, light-saturated and photoinhibition (Figure<br />

6). For light limitation, the photosynthetic rate increases asymptotically by increasing the light<br />

intensity from zero at a threshold light level, by which the photosynthesis is light-saturated and it<br />

reaches the maximal rate. At higher light irradiance than light-saturated condition photoinhibition<br />

occurs and the photosynthesis rate decrease by increasing light intensity (Figure 6). The slope of PIcurves<br />

in the light-limited condition representing the fraction between the maximal photosynthesis<br />

rate (V max ) and the light-saturation parameter (I k ) is called the affinity for light (Figure 6): a higher<br />

slope will mean a higher affinity (Le Quéré et al., 2005).<br />

Figure 6 Typical response<br />

curve of phytoplankton by<br />

increasing irradiance. The<br />

initial slope corresponds to<br />

the light affinity. At V max<br />

the photosynthesis is<br />

saturated by light. By high<br />

light<br />

irradiance<br />

photoinhibition occurs<br />

causing a decrease of the<br />

photosynthetic rate<br />

(Sarmiento and Gruber,<br />

2006)<br />

- 5 -


Comparing PI-curves of various phytoplankton groups clearly show that they have specific response<br />

of photosynthesis to varying light irradiance. Green algae (flagellates), which include also<br />

coccolithophorids, have the highest affinity to light and become light-saturated at lower light<br />

irradiance (Figure 7) than diatoms and dinoflagellates. Diatoms are less efficient than green algae,<br />

but more than dinoflagellates (Figure 7).<br />

Figure 7 Photosynthesis<br />

response at different light<br />

intensities (P-I curves) for<br />

different phytoplankton<br />

group (note that<br />

coccolithophores are<br />

included in the group of<br />

flagellates) (Sarmiento<br />

and Gruber, 2006)<br />

Another important characteristic of E. huxleyi is that this species of coccolithophorid does not show<br />

any sign of photoinhibition even at irradiances of 1700-2500 μmol -1 m<br />

-2 s -1 , which are equal or<br />

higher than light intensity by full sunshine (Paasche, 2002). The ability to survive in the dark is also<br />

a parameter which changes in different phytoplankton groups. Laboratory experiments have shown<br />

that silicifiers can survive for weeks without light supply, while calcifiers begin to die already after<br />

one day (unpublished data from R. Geider; reviewed in Le Quéré, 2005). This difference should be<br />

considered especially during winter, when the mixing depth is deeper than the euphotic zone.<br />

3.1.2 Nutrient supply and growth<br />

The response of the phytoplankton species to nutrient supply is another factor determining their<br />

competitive ability. Analogous to the determination of light affinity using light saturation parameter<br />

and maximal rate of photosynthesis, by the nutrient supply the affinity to a specific nutrient is<br />

quantified using the half-saturation constants (Ks). These are derived from Michaelis-Menten (Eq.<br />

1) and Monod (Eq. 2) saturation functions, which determine specific uptake rate (Vmax) and the<br />

specific growth rate (μ), respectively.<br />

[ Nut]<br />

[ Nut] Ks<br />

V<br />

V Nut<br />

= max Eq. 1<br />

+<br />

μ =<br />

μ max[ Nut]<br />

[ Nut] + Kμ<br />

Eq. 2<br />

- 6 -


Figure 8 Rate of nutrient uptake<br />

(example of nitrate) by increasing<br />

nutrient concentration. K N is the<br />

half-saturation constant of nitrate<br />

and is determined by the<br />

concentration of nitrate at which the<br />

uptake reaches the half of maximal<br />

rate V max (Sarmiento and Gruber,<br />

2006).<br />

Half-saturation constants are specific for a given nutrient and represent the concentration Ks of the<br />

nutrient that limits V Nut to the half of Vmax (Eq. 1) and the concentration Kμ of the nutrient that<br />

limits μ to the half of μmax (Eq. 2) (Sarthou et al., 2005; Figure 8). Species with a high halfsaturation<br />

for a determined nutrient need a higher concentration of a specific nutrient to grow.<br />

Coccolithophorids show an exceptional inorganic phosphorous (P) assimilation capability (Riegman<br />

et al., 2000;<br />

Table 1). One reason of this high affinity to P could be that coccolithophorids have many receptors<br />

for P (Le Quéré et al., 2005) and the availability of two types of alkaline phosphatase bound to the<br />

cell surface, which enables the coccolithophorids to use dissolved organic P (DOP; organic<br />

phosphate esters) at nM concentration level (Paasche, 2002; Rost and Riebesell, 2004). On the other<br />

hand diatoms have a higher half-saturation constant for P (<br />

Table 1), which means a higher requirement of P in comparison to coccolithophorids to grow.<br />

Table 1 Half-saturation constants of essential macro- (P and N) and micro- (Fe) nutrients for coccolithophorids<br />

and diatoms. Also represented are taxum-specific nutrients like orthosilicic acid for diatoms and dissolved<br />

organic phosphorous (DOP) for coccolithophorids ( ± Buitenhuis et al. (2002) ‡ Riegman et al. (2000): value found<br />

for E. huxleyi; ; † Le Quéré et al. (2005); Iglesias-Rodríguez et al. (2002) ).<br />

Phytoplankton<br />

group<br />

Ks (P)<br />

[nM] ±<br />

Ks (N)<br />

[μM]<br />

Kμ (Fe)<br />

[pM] ±<br />

Ks (Si)<br />

[μM] ±<br />

Other nutritional<br />

source<br />

Coccolithophorids 4 0.2 ‡ 20 - 1.9 DOP †<br />

Diatoms 75<br />

< 0.2 ‡<br />

> 0.2 120 2<br />

Considering N affinity some contradictions between scientists can be found. Riegman et al. (2000) describe E.<br />

huxleyi as not to a good competitor for nitrogen in contrast to phosphorous. Their experiments have shown a<br />

rather low maximal uptake rate of nitrate for E. huxleyi in comparison to most other algae species (also diatoms)<br />

and also the affinity for nitrate uptake was not extremely high (Riegman et al., 2000). Therefore the growth at N-<br />

limited condition of E. huxleyi is less exceptional than under phosphorous limitation. On the other hand Iglesias-<br />

Rodríguez et al. (2002) suggest that areas with sea surface presenting decreasing nitrate concentrations are<br />

selective for coccolithophorid blooms. Additionally they consider coccolithophorids as having an exceptionally<br />

high affinity for dissolved inorganic nitrogen, with half-saturation constants being approximately half that of<br />

diatoms of comparable size (<br />

Table 1).<br />

- 7 -


Iron and z inc are essential micronutrients for phytoplankton taxa. As well for these elements coccolithophorid E.<br />

huxleyi shows lower requirements and therefore a higher affinity in comparison to diatoms (Rost and Riebesell,<br />

2004;<br />

Table 1).<br />

The cell size of phytoplankton seems to play an importa nt role in the uptake and affinity for<br />

nutrients. Small planktons have a higher surface to volume ratio (S/V) than larger cells, which<br />

implies a better exchange of nutrients across the cell surface. The limitation in diffusion of nutrients<br />

uptake is consequenty lower for small plankton species than for larger ones (Sarthou et al., 2005).<br />

This theory could therefore explain the difference between diatoms and coccolithophorids in<br />

nutrient uptake and affinity: the cell size of coccolithophorids is in the range of 5-10 μm, while that<br />

of diatoms is between 20 and 200 μm (Le Quéré et al., 2005). Experiments have shown a significant<br />

relationship between size and growth within a plankton functional group (Sarthou et al., 2005),<br />

however considerations across different plankton functional groups do not necessarily be correct<br />

(Le Quéré et al., 2005). Actually different plankton species have developed specific adaptive<br />

strategies to overcome deficits in the nutrient uptake. For example diatoms can reduce their size<br />

(increasing their S/V ratio) in order to perform a better nutrient uptake (Sarthou et al., 2005).<br />

Another explanation of the difference in the ecophysiology between diatoms and coccolithophorids<br />

is based on the cellular design (Iglesias-Rodríguez et al., 2002). In diatoms a relative large fraction<br />

(approximately 35 %) of the cell volume is dedicated to storage vacuoles (Falkowski et al., 2004),<br />

which allow excess “luxury” uptake of macronutrients and their storage in the internal reservoirs.<br />

This mechanism allows to perform several cell divisions without the need of external input of<br />

nutrients (Iglesias-Rodríguez et al., 2002). In contrast the accumulation of macronutrients is lower<br />

for the smaller coccolithophorids than for diatoms (Rost and Riebesell, 2002; Iglesias-Rodríguez et<br />

al., 2002). Consequently growth rate in diatoms may be better buffered due to internal nutrients<br />

storage under changing nutrients supply (for example under unstable environment with pulsed<br />

nutrient supply), while by coccolithophorids the growth rate is directly coupled with the nutrient<br />

concentration in water. Because of the high nutrient uptake capacities, diatoms prevail under high<br />

nutrient conditions (mainly in spring and early summer) (Iglesias-Rodríguez et al., 2002; Sarthou et<br />

al., 2005). But under nutrient limiting conditions coccolithophorids out compete diatoms, as a result<br />

of their higher affinity to nutrients (Falkowski et al. 2004; Iglesias-Rodríguez et al., 2002; Paasche,<br />

2002; Riegman et al., 2000).<br />

3.1.3 Dissolved inorganic carbon (DIC) and growth<br />

In order to evaluate the potential response of coccolithophorids and diatoms to global changes and<br />

the related change in dissolved inorganic carbon supply it is also fundamental to consider the<br />

mechanism of carbon acquisition of both plankton groups and emphasize the differences between<br />

them. In comparison with other phytoplankton nutrients in seawater dissolved inorganic carbon is<br />

always in excess and for this reason in the last decades the role of inorganic carbon acquisition has<br />

been partially considered in phytoplankton ecology and evolution (Rost et al., 2003). However, the<br />

CO 2 fixation by the carboxylating enzyme RuBisCO (Ribulose-1,5-bisphosphate<br />

carboxylase/oxygenase) is restricted due to his low substrate affinity to CO 2 (half- saturation<br />

constant K M of 20-70 μmol L -1 ) (Rost and Riebesell, 2004). Because of the low seawater CO 2<br />

concentration ranging from 5 and 25 μmol L -1 , photosynthesis of marine phytoplankton may be<br />

limited by CO 2 (Rost et al., 2003). To overcome the limitation caused by the low affinity of<br />

carboxylating enzyme to CO 2 , most microalgae have developed mechanisms which increased the<br />

concentration of CO 2 at the site of carboxylation. These CO 2 concentrating mechanisms (CCMs)<br />

allow the active uptake of CO2 and/or HCO - 3 into the algal cell and/or in the chloroplast (Riebesell,<br />

2004). Another enzyme called carbonic anhydrase (CA) is coupled to CCMs and accelerates the<br />

rate of conversion between HCO - 3 and CO 2 (Rost et al., 2003). As a result of the CCMs and CA<br />

- 8 -


most marine phytoplanktons reach a high affinity for inorganic carbon and consequently<br />

photosynthetic carbon saturation under ambient CO 2 levels (Raven and Johnston, 1991; reviewed in<br />

Rost and Riebesell, 2004).<br />

Recent experiments considering various groups of phytoplankton indicate differences in CO 2<br />

senstivity. Rost et al. (2003) compares three marine bloom-forming microalgae: the diatom<br />

Skeletonema costatum, the coccolithophorids Emiliania huxleyi and the flagellate Phaeocystis<br />

globosa. The photosynthetic carbon fixation of diatom and flagellate considered in this experiment<br />

is close to CO 2 -saturation considering typical marine CO 2 concentration at present days of 5-25<br />

μmol L -1 (Figure 9). While coccolithophorid E. huxleyi has comparatively lower affinity and seems<br />

to be carbon limited at present CO 2 level (Figure 9).<br />

The low affinity of E. huxleyi for<br />

inorganic carbon has led to the<br />

hypothesis that this species of<br />

coccolithophorids may not rely on<br />

an active carbon uptake, but only on<br />

diffusive CO 2 supply for<br />

photosynthesis (Raven and<br />

Johnston, 1991; reviewed in Rost<br />

and Riebesell, 2004). Though recent<br />

studies have confirmed the presence<br />

of CCMs in E. huxleyi, but its<br />

efficiency appear to be lower than<br />

in other phytoplankton groups (Rost<br />

et al., 2003).<br />

Although intensive research on<br />

coccolithophorids the function of<br />

calcification (and consequently of<br />

coccoliths) is not well understood<br />

(Paasche, 2002). It has been<br />

Figure 9 Relative photosynthesis response at different CO 2 hypothesized that coccoliths protect<br />

concentration of the diatom Skeletonema costatum, the the cell from strong light or they are<br />

coccolithophorids Emiliania huxleyi and the flagellate Phaeocystis<br />

used to redirect light into the cell<br />

globosa. K 1/2 (CO 2 ) represents the half-saturation constant for<br />

CO 2 in μmol L -1 (Riebesell, 2004).<br />

(useful in light-limited condition)<br />

(Young, 1994; reviewed in Paasche,<br />

2002). But the removal of coccoliths did not confirm these hypothesises: no change of light<br />

inhibition by high irradiance and of light-saturation parameter (I k ; see Figure 6) has been found<br />

(Nanninga and Tyrrell, 1996). Experiments with 14 C-labeled DIC indicate that E. huxleyi makes the<br />

coccolith from bicarbonate (HCO - -<br />

3 ) rather than from carbonate or CO 2 and that both HCO 3 and<br />

CO 2 in the medium are used for photosynthesis (Paasche, 2002). These experiments seem to prove<br />

the close coupling between photosynthesis and calcification and to support a “trashcan function” of<br />

calcification, in which calcite (CaCO 3 ) precipitation serves as mechanism to facilitate the use of<br />

HCO - 3 in photosynthesis (Riebesell, 2004). According to the following reactions (Eq. 3 and Eq. 4)<br />

2+<br />

−<br />

Ca + 2 HCO3<br />

→ CaCO3<br />

+ CO2<br />

+ H<br />

2O<br />

2+<br />

−<br />

+<br />

Ca + HCO3<br />

→ CaCO3<br />

+ H<br />

Eq. 3<br />

Eq. 4<br />

the process of calcification is beneficial to photosynthesis since it releases CO 2 or protons (H + ),<br />

-<br />

which could be used directly in photosynthesis or in the conversion of HCO 3 to CO 2 , respectively<br />

(Rost and Riebesell, 2004; Paasche, 2002). However, non-calcifying cells of E. huxleyi seem also to<br />

- 9 -


e able to direct uptake of HCO 3<br />

-<br />

and this could mean that the use of bicarbonate is not tied to<br />

calcification (Rost and Riebesell, 2004). Experiments conducted by Riebesell et al. (2000) indicate<br />

that the rate of photosynthesis decreases with decreasing CO 2 concentration although a concomitant<br />

increase in the calcification rate. In conclusion the beneficial of calcification for photosynthesis is<br />

not yet clear, but what can be said is if the primary role calcification is the CO 2 supply for<br />

photosynthesis, this mechanism seems to be rather inefficient in comparison with CCMs of noncalcifying<br />

phytoplankton like diatoms (Rost et al. 2003).<br />

3.1.4 Temperature and growth<br />

Under ideal nutrient supply and light availability the maximal growth of phytoplankton is given by<br />

the temperature. However the growth rates found in laboratory experiment for different taxa seem<br />

not to change so much, and therefore a generic growth rate of 0.6 d -1 at 0 °C is widely used for<br />

phytoplankton (Banse, 1992; reviewed in Le Quéré, 2005). For example also in The Dynamic<br />

Green Ocean Model for all six plankton functional groups (picophytoplankton, nanophytoplankton,<br />

coccolithophorids, diatoms, phaeocystis and N 2 -fixers) is based on a maximum specific growth rate<br />

of 0.6 d -1 at 0 °C is used (Buitenhuis et al., 2002). For this reason temperature seems to be a factor,<br />

which does not differ significantly in coccolithophorids and diatoms.<br />

3.2 Loss processes<br />

Grazing by zooplankton is - like nutrient availability and light irradiance - another factor which can<br />

control or limit the growth of phytoplankton functional group. The plates of calcium carbonate<br />

called coccoliths covering the cell of coccolithophorids do not seem to provide a protection against<br />

various types of microzooplankton (Harris, 1994; reviewed in Rost and Riebesell, 2004). Whereas<br />

the frustules by diatoms seem to hold a more important role as mechanical protection against<br />

grazers (Hamm et al., 2003; reviewed in Riebesell and Rost, 2004). Also the smaller size of<br />

coccolithophorids makes them more susceptible to microzooplankton grazing in comparison with<br />

diatoms.<br />

Cell lysis is another important process influencing the plankton dynamic. Two types of cell lysis are<br />

recognized: the viral lysis and death due to nutrient stress. Against the viral lysis diatoms appear to<br />

be quite well protected. Autolysis rates determined through experiments are relatively low and<br />

therefore can significantly reduce net growth rate particularly under nutrient limitation when growth<br />

rates are low (Sarthou et al., 2005). While for coccolithophorids limited research has been<br />

performed on the cell lysis.<br />

Sinking rate of plankton is an additional loss processes. In low nutrient environment movement<br />

through the water could be essential for the survival. For phytoplankton species without motility<br />

apparatus a mechanism to compensate this lack is to regulate the sinking rate by changing their<br />

density or forming aggregate (Paasche, 2002; Sarthou et al., 2005). An overproduction of calcite<br />

coccoliths by coccolithophorids or a thickening of siliceous frustules increase the cell density in<br />

relation to water density and consequently increase the sinking rate. Because sinking rate is also a<br />

function of the size, the aggregation of cells has the purpose of increase the sinking rate too. For the<br />

reason that both mentioned phytoplankton species allow to similar properties, the sinking rate as<br />

loss process will to a less degree considered.<br />

- 10 -


Table 2 Summarizing and comparative table of physiological characteristics of coccolithophorids (C) and<br />

diatoms (D). For a more detailed description of each trait see the relative chapter about ecophysiology. ( <br />

Divergence between Riegman et al. (2000) and Iglesias-Rodríguez et al. (2002)).<br />

ocesses<br />

Growth pr<br />

Loss<br />

processes<br />

Coccolithoporids (C)<br />

vs Diatoms (D)<br />

C<br />

C < D<br />

Affinity (based on halfsaturation<br />

P<br />

C > D<br />

constant) N C > < D <br />

Nutrient<br />

supply<br />

Fe, Zn<br />

C > D<br />

Cellular design: storage Nutriment<br />

vacuoles<br />

uptake capacity<br />

C < D<br />

Diffusion limitation S/V ratio C < D<br />

Light saturation parameter (a lower value<br />

Light means a higher “affinity” for light)<br />

C < D<br />

Photoinhibition<br />

C < D<br />

Temperature Growth rate dependence to temperature C = D<br />

Sinking rate<br />

C ≈ D<br />

Grazing by zooplankton (depends on mechanical protection<br />

given by coccoliths (C) and frustules (D))<br />

C > D<br />

4. Response of coccolithophorids and diatoms to predicted<br />

global changes considering their specific ecophysiology<br />

Changes in seawater carbonate chemistry, affected directly by increasing atmospheric pCO 2 , have<br />

consequences on the availability of carbon for photosynthesis and calcification for<br />

coccolithophorids. At the present CO 2 levels, the rate of photosynthetic carbon fixation by E.<br />

huxleyi seems to be below saturation, in contrast to diatom species (e.g. Skeletonema costatum)<br />

which are more efficient in carbon uptake (Figure 9). Therefore coccolithophorids may benefit from<br />

the predicted increase in the dissolved CO 2 concentration in seawater fulfilling their higher carbon<br />

requirements. This implies that an increase in CO 2 availability may improve the resource utilisation<br />

of E. huxleyi and other coccolithophorids with similar physiological characteristics, causing an<br />

increase in their contribution to overall primary production. On the other hand, the continued<br />

acidification of the upper ocean due to increasing CO 2 leads to deteriorated conditions for biogenic<br />

calcification. Riebesell et al. (2000) observed a reduced calcite production at increased CO 2 levels<br />

in two bloom-forming coccolithophorids, E. huxleyi and Gephyrocapsa oceanica. Because of higher<br />

dissolved CO 2 concentration in surface seawater, these species of coccolithophorids have no to<br />

compensate relatively inefficient CO 2 concentrating mechanisms by performing calcification (Eq.<br />

3), which release carbon dioxide for photosynthesis. This theory could explain the observed<br />

coccoliths under-calcification and malformation in both natural environments and under laboratory<br />

conditions. Although the role of CaCO 3 formation in coccolithophorids is not clear, reduced<br />

calcification seems to affect both resource utilization and cellular protection with possible adverse<br />

effects on the competitive fitness of coccolithophorids.<br />

Although under natural conditions CO 2 limitation seems to be less important compared to other<br />

limiting resources for E. huxleyi (Riebesell, 2004), which should be more CO 2 -sensitive than<br />

- 11 -


diatoms because of higher requirements. Consequently, additional possible limiting factors have to<br />

be considered to asses the potential changing fitness of coccolithophorids and diatoms due to<br />

climate change. As explained before, raising atmospheric pCO 2 has not only direct effects on<br />

carbonate chemistry of surface seawater, but also indirect effects that are correlated with changing<br />

climate due to increased carbon dioxide levels. A first effect is the enhanced stratification of surface<br />

ocean equivalent to an increase in vertical stability of the water pro<strong>file</strong>, thus decreasing nutrient<br />

supply. In the previous chapter half-saturation constants for major macronutrients (P and N) as well<br />

as micronutrients like iron are illustrated. Considering P or Fe half-saturation the difference in the<br />

affin ity of coccolithophorids and diatoms are significant. For<br />

nitrogen some contradictions between<br />

scientists can be found. Riegman et al. (2000) referred to the coccolithophorid E. huxleyi as a poor<br />

competitor with regard to nitrogen. Whereas Iglesias-Rodríguez et al. ( 2002) indicate areas with sea<br />

surface presenting decreasing nitrate concentrations as selective for coccolithophorid blooms and<br />

consider coccolithophorids as having an exce ptionally high affinity for dissolved inorganic<br />

nitro gen, with half-saturatio n constants being approximately half that of diatoms of comparable<br />

size.<br />

To simplify the assessment of the response of the considered phytoplankton groups to changes in<br />

nutrients supply, no different iation between different nutrients will be made. A value for the affinity<br />

to nutrients of coccolithophorids and diatoms as a whole should be taken into account to determine<br />

their response to global changes. Assuming that P is the limiting factor in seawater of many regions,<br />

the half-saturation constant for P is taken as an approximation for the whole nutrient supply. This<br />

w ill mean that an enhanced stratification occurring on a global scale and the resulting reduced<br />

nutrient supply mainly increases the competitive ability of coccolithophorids, which can take up<br />

nutrients at very low concentrations. This assumption is also supported if micronutrients like Fe or<br />

Zn are considered. For this class of nutrients, Coccolithophorids also display lower half-saturation<br />

constants, which indicates better affinity. Finally, considering the more recent paper of Iglesias-<br />

Rodríguez et al. (2002), evidence suggests that coccolithophorids are also more competitive at low<br />

nutrients supply in regard to N.<br />

Enhanced stratification due to global climate change and subsequently shoaling of the mixed layer<br />

depth seems to occur globally in oceans. However, the strength and the impact of this process<br />

change by considering different latitudes, as a result of already different conditions characterizing<br />

these areas today. For example mid-latitudes or tropics are nutrient-limited because of a highly<br />

thermal-stratified surface seawater pro<strong>file</strong>. Whereas at higher latitudes the mixed layer depth is<br />

often deeper than the eutrophic zone and phytoplankton species are transported down to layers<br />

where the light does not penetrate, hence phytoplankton is mainly light-limited at higher latitudes at<br />

present. A shoaling mixed layer depth and the consequently reduced nutrient supply at these two<br />

latitudes will therefore have a different impact on the present conditions. These changed<br />

environmental conditions could affect the composition, distribution and succession of<br />

phytoplankton species.<br />

4.1 Tropics and mid-latitudes<br />

The predicted enhanced stratification in the tropics and mid-latitudes decreases the already low<br />

nutrient supply and consequently, surface seawater will be even more nutrient-limited. The<br />

planktonic composition of these areas should therefore not change so much in the next decades.<br />

Low mixed layer depths in these regions allow the plankton species to colonize the shallow<br />

superficial layer, which is characterized by high solar irradiance and low nutrient supply. Both<br />

parameters are selective for coccolithophorids, species showing a higher affinity to nutrients and no<br />

or little photoinhibition. The mixed layer depth and thus the nutrient supply vary little at these<br />

latitudes, because of relatively constant temperatures during the year. Even in winter, when the<br />

mixed layer depth reaches its maximum, low nutrient supply and high light intensities are not<br />

favourable conditions for diatoms. The fraction of the sediments dominated by CaCO 3 at these<br />

- 12 -


latitudes could confirm the planktonic composition prevailed by coccolithophorids (see annex,<br />

Figure A 1).<br />

Because of increased nutrient limitation, marine productivity in the tropics and mid-latitudes seems<br />

to decrease substantially. Bopp et al. (2001) investigated the response of the productivity of<br />

phytoplankton to global warming using coupled atmosphere-ocean general circulation models and<br />

ocean biogeochemical schemes. At doubled atmospheric pCO 2 (700 ppm) Bopp et al. indicate a<br />

decline in productivity in the tropics reaching -15 to -20 %.<br />

4.2 Higher latitudes<br />

At higher latitudes phytoplankton are not nutrient limited but light limited. This is due to the water<br />

columns being less stabilized by thermal stratification and, consequently this low density gradient in<br />

surface seawater causes the mixed layer depth to be large. This factor does not allow an efficient<br />

light use, since phytoplanktons are carried to deeper depths with prohibitive light condition for<br />

photosynthesis. The maximal mixed layer depth occurs in winter when the surface water pro<strong>file</strong> is<br />

minimally stabilized. Warming of the surface water during the year increases his stratification and<br />

so decreases the mixed layer depth. The nutrient supply course during the year follows mainly the<br />

mixed layer depth. Assuming that nutrients come from the deep ocean, a higher mixed layer depth<br />

in winter leads to higher nutrient supply and higher concentrations in the surface layers. Analogous,<br />

shoaling mixed layer depth during spring and summer reduces the nutrient supply. These eutrophic<br />

conditions particularly at the beginning of the spring are favourable and selective for diatoms. This<br />

plankton species does not have a high nutrient affinity, but the evolution of nutrient storage<br />

vacuoles allows the cells to retain high concentrations of nutrients. Comparison experiments with<br />

diatoms also indicate a good ability to survive in the dark for several weeks (unpublished data from<br />

R. Geider; reviewed in Le Quéré, 2005). These two features allow competitive advantage of<br />

diatoms compared to coccolithophorids, which are better adapted to oligotrophic condition and<br />

show a poor ability to survive in the dark (die after one day without light; unpublished data from R.<br />

Geider; reviewed in Le Quéré, 2005).<br />

The predicted increasing stratification in higher latitudes due to global warming will mean a better<br />

photosynthetic efficiency during spring and summer. Because of a shallow mixed layer depth<br />

phytoplanktons experience lower light limited conditions and this implies better as well as longer<br />

light utilization in the euphotic zone. The shallowing of the mixed layer occurs earlier in the year<br />

and the deepening occurs later, resulting in an expansion of the growing season length. At present<br />

and under global warming conditions diatoms bloom earlier in the growing season than<br />

coccolithophorids, because of the high survival ability in the dark, which allows them to maintain<br />

relatively high biomass over the winter months. During spring and summer the mixed layer depth is<br />

expected to shallow more than at present. As a result of high nutrient sequestration by diatoms at<br />

the beginning of the season and of reduced mixed layer depths, which also limit the nutrient supply;<br />

surface seawater becomes progressively more nutrient limited. Diatoms seem to partially adapt<br />

themselves to these conditions reducing their size, in order to increase the surface to volume ratio<br />

and consequently meliorate their nutrient uptake in oligotrophic conditions. However the lower<br />

mixed layer depth in late spring or early summer and the subsequently low nutrient availability<br />

could be favourable conditions for coccolithophorids. Due to their higher affinity to nutrients these<br />

calcifiers may out compete other phytoplankton species. In this way, under climate warming, the<br />

productivity at higher latitudes could increase in comparison to today. This poleward shift of<br />

phytoplankton production is also observed in the simulation performed by Bopp et al. (2001), who<br />

estimates an increase in productivity in subpolar regions (south of 50°S and north of 60°N) by more<br />

than 10 %.<br />

At higher latitudes the fraction of opal, which can be used as an indicator for diatoms, dominates<br />

the sediment content. Although, due to melioration of abiotic factors in regard to coccolithophorids<br />

physiological characteristics and the migration of this phytoplankton group to higher latitudes, the<br />

opal to calcite ratio in the sediment may decrease during the next decades (see annex, Figure A 2).<br />

- 13 -


4.3 Role of growth and loss processes in determining the response of<br />

coccolithophorids and diatoms to the global climate changes<br />

In the determination of the competitive ability and selective advantages of coccolithophorids and<br />

diatoms considering changing abiotic factors, not all growth and loss processes seem to have the<br />

same relevance. Generally one can say that the larger the difference for a physiological trait<br />

between coccolithophorids and diatoms, the more relevant is the considered characteristics to assess<br />

their response to global changes. Considering the affinity to nutrients of these two groups a<br />

significant difference in the values of half-saturation constants principally for P and Fe can be<br />

observed (<br />

Table 1). On the other hand coccolithophorids and diatoms do not show large difference in their<br />

“affinity” to light. For example, in The Dynamic Green Ocean Model the “affinity” for light of<br />

coccolithophorids in relationship with that of diatoms slightly differs and the ratio is 3:2. In<br />

comparison, the ratio for affinity of P and Fe is 19:1 and 6:1, respectively. So the different affinities<br />

for nutrients exhibited by these two phytoplankton groups seem to be more relevant. However,<br />

specific characteristics like survival ability in the dark or photoinhibition as well as availability of<br />

storage vacuoles in the cell, which increase the nutrient uptake capacities without changing their<br />

affinity to nutrients, should not be neglected, since they complete/influence significantly the affinity<br />

value for nutrients and light.<br />

In order to assess a shift in composition and succession of coccolithophorids and diatoms due to<br />

global changes, composition of the nutrient supply is not taken into account in this term paper and<br />

for nutrients as a whole the half-saturation of P will be considered in the assessment. However not<br />

all oceans are P-limited. In addition, considering only P, an extreme scenario will be found, due to<br />

extremely high P affinity by coccolithophorids compared to diatoms. The predicted changes in<br />

composition and succession in this term paper will not change significantly considering also iron.<br />

But, if diatoms have a better affinity to N as reported by Riegman (2000) and for these oceans<br />

which are N-limited, an enhanced stratification and consequent reduction of nutrient supply (also N)<br />

will change considerably the future predictions. Another factor which should be taken into account<br />

to obtain a more realistic scenario, is the supply of orthosilicic acid. Diatoms are unique among<br />

photoautotrophic taxa, which have an absolute requirement for orthosilicic acid to form shells called<br />

frustules (Falkowski et al., 2004). Silica is introduced into oceans by continental weathering but<br />

also from deep ocean. How an enhanced stratification affects the silica availability is still not well<br />

known.<br />

The loss processes are also determinant in assessing the ecological success of a phytoplankton<br />

species, which is principally determined by the ability of a species to optimise the balance between<br />

growth and loss processes. For many of these processes little information is known and further<br />

research will be useful for better assessment of competitive ability. In the considerations above<br />

about the response of coccolithophorids and diatoms at different latitudes to global changes loss<br />

processes are not taken in account.<br />

Mortality rate is a function of temperature. So the predicted climate warming may increase<br />

mortality rate of both coccolithophorids and diatoms. Another loss process is sinking rate. Diatoms<br />

are generally larger than coccolithophorids and in addition they form agglomerates. Both reasons<br />

lead to the conclusion that diatoms may have a higher sinking rate. However coccolithophorids, and<br />

likely diatoms, can raise their density by an overproduction of coccoliths and increase the sinking<br />

rate. For this process it is difficult to weigh its specific importance in both phytoplankton groups.<br />

Against autolysis and viral lysis diatoms seem to be quite well protected, but for coccolithophorids<br />

limited research has been performed on this topic. Among all loss processes grazer control by<br />

higher trophic level may mostly influence the composition and seasonal succession of<br />

phytoplankton groups. While frustules in diatoms seem to serve as an effective mechanical<br />

protection against various predators, coccoliths of coccolithophorids may not provide the same<br />

degree of protection. Zooplankton has the potential to propagate at similar rates as its prey and<br />

therefore reduces or impedes phytoplankton mass development. Also in The Dynamic Green Ocean<br />

- 14 -


Model zooplankton grazing is a point which is being worked on, because of the importance of this<br />

process in structuring the marine food web. Also other scientists like Rost and Riebesell set the<br />

understanding of the complex structure and regulation of marine pelagic ecosystem as a major<br />

challenge for marine sciences in the next decades.<br />

4.4 Effects on biological carbon pump<br />

In the previous chapter effects of changing climatic conditions on two important phytoplankton<br />

groups like coccolithophorids and diatoms have been described. In turn, their activity can have a<br />

direct impact on the climate. They can mitigate or amplify climate change by driving many of the<br />

global elemental cycles. Since CO 2 represents the most important greenhouse gas leading to global<br />

warming, knowing the role of phytoplankton for the oceanic carbon cycle is important. The effects<br />

of coccolithophorids on this cycle differ greatly from other phytoplankton species and seem to have<br />

a relevant feedback on climate. That is the reason why coccolithophorids are principally dealt in this<br />

chapter.<br />

The fixation of inorganic carbon through<br />

photosynthesis in the upper ocean and the<br />

subsequent transport of organic matter<br />

(“ideally” CH 2 O) to depth is termed the<br />

organic carbon pump (Figure 10). This<br />

process is performed by all primary<br />

producers and causes a net draw down of<br />

CO 2 from the atmosphere into the ocean.<br />

Additionally coccolithophorids produce<br />

calcite (CaCO 3 ) coccoliths through the<br />

reaction of calcification. The production and<br />

export of CaCO 3 to the deep sea binds<br />

dissolved inorganic carbon (DIC) in<br />

particulates and therefore reduces total<br />

dissolved carbon. This process also lowers<br />

alkalinity and changes the equilibrium Figure 10 Biological carbon pumps: organic carbon<br />

pump and carbonate counter pump. The strength of<br />

between different species of DIC, causing a<br />

these two processes determines the rain ratio, an<br />

net release of CO 2 to the atmosphere (Rost important parameter for ocean atmosphere CO 2<br />

and Riebesell, 2004; Figure 10). Because of exchange (Rost and Riebesell, 2004).<br />

the counteracting effect on the CO 2 flux, this<br />

process is called the carbonate counter pump (or also simply carbonate pump). The rain ratio gives<br />

the relative strength of these two biological carbon pumps and corresponds to the ratio of particulate<br />

inorganic carbon (CaCO 3 ) to organic carbon (C org) exported to the deep sea (Figure 10). This ratio<br />

assumes a non-negligible significance since it determines the biologically mediated partitioning of<br />

CO 2 between ocean and atmosphere.<br />

Coccolithophorids, and generally calcifying phytoplankton species, compared to non-calcifying<br />

primary producers are a smaller sink for CO 2 or could even act as a net source (Zondervan et al.,<br />

2001). Consequently, in determining the rain ratio it seems to be crucial to assess the proportion of<br />

calcareous to non-calcareous primary production. So that the marine phytoplankton composition<br />

and succession impact on carbon cycle and so on global climate. If the predicted reduced nutrient<br />

supply and the increase availability of dissolved CO 2 in surface seawater due to rising atmospheric<br />

pCO 2 are advantageous to coccolithophorids, causing an increase in their fraction among primary<br />

producers, calcification and then relative global export of calcite to the deep sea would increase.<br />

Increasing rain ratio, by increased calcification and more efficient carbon counter pump, would<br />

result in a positive feedback to rising atmospheric CO 2 . On the other hand, experiments conducted<br />

by Riebesell et al. (2000) have shown reduced calcification with increasing pCO 2 . This observed<br />

- 15 -


process may neutralise or even reverse the positive feedback described before into a negative one,<br />

leading to an increase in the CO 2 storage capacity of the surface ocean. A quantification of these<br />

two counteracting processes, increased abundance of coccolithophorids and decreased calcification,<br />

will help to predict the ocean atmosphere CO 2 exchange in the future and consequently also the<br />

atmospheric CO 2 level, which is finally a determinant for global climate changes. Further research<br />

is required on these processes and Riebesell (2004) confirms this need by claiming: “despite the<br />

potential importance of global change-induced biogeochemical feedback, our understanding of<br />

these processes is still in its infancy”.<br />

5. Conclusion<br />

In the determination of the response of coccolithophorids and diatoms to future climate change the<br />

nutrient supply may have the most important relevance among all considered parameters. Predicted<br />

enhanced stratification of the upper ocean due to global warming and consequently a shoaling<br />

mixed layer depth will reduce nutrient supply. The impact and the strength of this process will vary<br />

considering different latitudes. In the tropics and mid-latitudes the present conditions may change<br />

little and therefore the planktonic composition at these latitudes will remain dominated by<br />

coccolithophorids. However, at higher latitudes this process seems to lead to favourable conditions<br />

for coccolithophorids particularly by low nutrient availability in late spring or early summer. The<br />

increase in the fraction of calcifying phytoplankton like coccolithophorids among primary<br />

producers raises the rain ratio causing a net release of CO 2 to the atmosphere (positive feedback to<br />

rising atmospheric CO 2 ). However the observed reduced calcification with increasing pCO 2 could<br />

reverse the positive feedback into a negative one, which would mean an increase of CO 2 storage<br />

capacity of the surface ocean. A better quantification of these two counteracting processes could<br />

help to predict CO 2 partitioning between ocean and atmosphere in the future.<br />

6. Literature<br />

BOPP L. AND OTHERS (2001): Potential impact<br />

of climate change on marine export production.<br />

Global Biogoechemical Cycle, 15, 81-99.<br />

BUITENHUIS E. T., C. LE QUÉRÉ, O. AUMONT (2002): The Dynamic Green Ocean Model: 6<br />

plankton functional groups in an ocean global circulation model. Poster of workshop on “Global<br />

ocean productivity and the fluxes of carbon and nutrients: combining observation and models”,<br />

24.-27. June, Ispra (Italy). (http://ijgofs.whoi.edu/GSWG/Ispra_modelling/Buitenhuis.<strong>pdf</strong>)<br />

[13.06.2007]<br />

DONEY S. C. (2006a): The dangers of ocean acidification. Scientific American, March 2006, 58-<br />

65.<br />

DONEY S. C. (2006b): Plankton in a warmer world. Nature, 4447, 695-696.<br />

FALKOWSKI P. G., O. SCHOFIELD, M. E. KATZ, B. VAN DE SCHOOTBRUGGE, A. H.<br />

KNOLL (2004): Why is the land green and the ocean red? In: THIERSTEIN H. R., J. R.<br />

YOUNG (2004): Coccolithophores from molecular processes to global impact. Springer Verlag,<br />

427-453.<br />

- 16 -


IGLESIAS-RODRÍGUEZ M. D. AND OTHERS (2002): Representing key phytoplankton functional<br />

groups in ocean carbon cycle models: Coccolithophorids. Global Biogeochemical Cycles, 16,<br />

1100, doi: 10.1029/2001GB001454.<br />

LE QUÉRÉ C. AND OTHERS (2005): Ecosystem dynamics based on plankton functional types for<br />

global ocean biogeochemistry models. Global Change Biology, 11, 2016-2040.<br />

NANNINGA H. J., T. TYRRELL (1996): Importance of light for the formation of algal blooms by<br />

Emiliania huxleyi. Marine Ecology Progress Series, 136, 195-203.<br />

PAASCHE E. (2002): A review of the coccolithophorid Emiliania huxleyi (Prymnesiophyceae),<br />

with particular reference to growth, coccolith formation, and calcification-photosynthesis<br />

interactions. Phycologia, 40, 503-529.<br />

RAVEN J. AND OTHERS (2005): Ocean acidification due to increasing atmospheric carbon dioxide.<br />

The Royal Society, June 2005.<br />

RIEBESELL U., I. ZONDERVAN, B. ROST, P. D. TORTELL, R. E. ZEEBE, F. M. M. MOREL<br />

(2000): Reduced calcification of marine phytoplankton in response to increased atmospheric<br />

CO 2 . Nature, 407, 364-367.<br />

RIEBESELL U. (2004): Effects of CO 2 enrichment on marine phytoplankton. Journal of<br />

Oceanography, 60, 719-726.<br />

RIEGMAN R., W. STOLLTE, A. A. M. NOORDELOOS, D. SLEZAK (2000): Nutrient uptake<br />

and alkaline phosphatase (EC 3:1:3:1) activity of Emiliania huxleyi (Prymnesiophyceae) during<br />

growth under N and P limitation in continuous cultures. Journal of Phycology, 36, 87-96.<br />

ROST B., U. RIEBESELL (2004): Coccolithophores and the biological pump: responses to<br />

environmental changes. In: THIERSTEIN H. R., J. R. YOUNG (2004): Coccolithophores from<br />

molecular processes to global impact. Springer Verlag, 99-125.<br />

ROST B., U. RIEBESELL, S. BURKHARDT, D. SÜLTEMEYER (2003): Carbon acquisition of<br />

bloom-forming marine phytoplankton. Limnology and Oceanography, 48, 55-67.<br />

SARMIENTO J. L. AND OTHERS (2004): Response of ocean ecosystems to climate warming.<br />

Global Biogeochemical Cycles, 18, GB3003.<br />

SARMIENTO J. L., N. GRUBER (2006): Ocean biogeochemical dynamics. Princeton University<br />

Press.<br />

SARTHOU G., K. R. TIMMERMANS, S. BLAIN, P. TRÉGUER (2005): Growth physiology and<br />

fate of diatoms in the ocean: a review. Journal of Sea Research, 53, 25-42.<br />

ZONDERVAN I., R. E. ZEEBE, B. ROST, U. RIEBESELL (2001): Decreasing marine biogenic<br />

calcification: a negative feedback on rising atmospheric pCO 2 . Global Biogeochemical Cycles,<br />

15, 507-516.<br />

- 17 -


7. Annex<br />

Figure A 1 Fraction of calcite in surface sediments (% weight: mass calcite to mass total solid dry sediments)<br />

(Sarmiento and Gruber, 2006).<br />

Figure A 2 Fraction of opal in surface sediments (% weight: mass opal to mass total solid dry sediments)<br />

(Sarmiento and Gruber, 2006).<br />

- 18 -


Term paper, June 2007<br />

Mechanisms of oxidative vs. reductive nitrobenzene<br />

transformation by microorganisms<br />

Term paper in Biogeochemistry and Pollutant Dynamics,<br />

Master Studies in <strong>Environmental</strong> Sciences, <strong>ETH</strong> Zürich<br />

By<br />

Ivo Caravatti<br />

Tutor: Dr. Thomas Hofstetter<br />

Abstract<br />

Nitroaromatic compounds such as nitrobenzene (NB), are widespread environmental<br />

contaminants. In natural attenuation processes selected microorganisms are able to<br />

degrade nitrobenzene via two different pathways, that is oxidation of nitrobenzene to<br />

catechol and reduction to aniline, respectively. Since both processes occur under oxic<br />

conditions but the latter leads to products of similar toxicity than the initial<br />

contaminant, it is necessary to differentiate between the two reactions at contaminated<br />

sites. Using compound-specific isotope analysis (CSIA), it should, in principle possible<br />

to identify NB degradation pathways by measuring changes of stable isotope signature<br />

of the remaining NB during its degradation. This hypothesis relies on the different<br />

enzymatic mechanisms that have been reported for enzymatic nitrobenzene<br />

degradation. However, since data on isotope effect are lacking, this term paper reviews<br />

the elementary reaction steps of the competing enzymatic nitrobenzene transformation<br />

pathways on a molecular scale to obtain some estimates of the potential magnitude of<br />

carbon and nitrogen isotope effects. Oxidation of nitrobenzene by Comamonas sp.strain<br />

JS765, should result in a moderate C isotope effect. The magnitude of the isotope effect,<br />

however, depends on some elementary reaction steps in the dioxygenation mechanisms,<br />

which are not fully understood to date. In addition, depending on the reaction<br />

mechanisms, also a strong N isotope effect might be expected. On the other hand,<br />

reduction of NB by Pseudomonas pseudoalcaligenes strain JS45 is expected to result in<br />

negligible C and substantial N isotope fractionation. The theoretical evidence for<br />

isotope fractionation obtained in this term paper suggest that the two enzymatic<br />

nitrobenzene transformation pathways might be distinguished in the field on the basis<br />

of compound-specific isotope analysis.<br />

1. Introduction<br />

Nitroaromatic compounds (NACs) constitute a very important class of environmental contaminants.<br />

The stability of nitroaromatic compounds make them valuable as chemical intermediates in<br />

industrial chemistry (8). Nitroaromatic compounds are used especially for the production of<br />

pesticides, dyes, and polymers. On the other hand, nitroaromatic explosives, which are derived from<br />

nitration of toluene, constitute a big problem at sites of military explosive production, ammunition<br />

testing and storage. The widespread application NACs and their improper disposal has resulted in<br />

the release of NACs into the environment (10). Innumerable sites are contaminated worldwide. In<br />

1


Term paper, June 2007<br />

addition, NACs used as agrochemicals such as pesticides are spread deliberately into the<br />

environment (9).<br />

Fortunately, many nitroaromatic compounds accumulated in the environment are biodegraded by<br />

bacteria. Bioremediation can be defined as any process that uses microorganisms to return a<br />

polluted environment to its original conditions. Adding specific substrate is possible to induce or<br />

accelerate a determinate biodegradation process. This process is called stimulation. Since<br />

mechanical cleanup of nitroaromatic polluted areas is nowadays an economic issue, bioremediation<br />

is an important alternative (9).<br />

However, compounds like nitrobenzene (NB) have more than one biodegradation pathway.<br />

Comamonas sp.strain JS765 is able to oxidise NB, on the other hand Pseudomonas<br />

pseudoalcaligenes strain JS45 is able to reduce NB (14, 15). Fig 1 shows the main step of the NB<br />

degradation for both microorganisms. Although both degradation pathways lead to mineralization<br />

of the compound, some products of the reductive pathway are transient more toxic products<br />

(especially aniline) Many of this products are cytotoxic and/or mutagenic (20).<br />

NO 2<br />

A) Oxydation<br />

B)<br />

Reduction<br />

OH<br />

Catechol<br />

OH<br />

-<br />

CO 2 +NO 2<br />

NH 2<br />

CO 2 +NH 3<br />

Aniline<br />

Figure 1: Main steps of the degradation of NB: A) Oxidation leads to the formation of catechol; B)<br />

Reduction leads to the formation of transient more toxic products. Both pathways lead to the complete<br />

degradation of NB. Modified from (14, 15).<br />

It is important to determine which pathway occurs in the contaminated site. However, a direct<br />

measurement of the biodegradation products is labour intensive and not always conclusive for the<br />

distinction of the pathways. An increasingly important tool for qualitative and quantitative<br />

assessment of abiotic and enzymatic transformations of organic contaminants in the environment is<br />

the Compound Specific Isotope Analysis (CSIA)(6). CSIA is based on isotopic signature. Isotopic<br />

signature is determined through the relative isotopic compositions of a given element within a<br />

compound. Isotope signatures for a given element E is defined as follow (6):<br />

2


Term paper, June 2007<br />

⎛ ⎛<br />

⎜<br />

⎜<br />

⎜<br />

h ⎝<br />

δ E = ⎜<br />

⎜⎛<br />

⎜<br />

⎜<br />

⎝⎝<br />

h<br />

l<br />

h<br />

l<br />

E ⎞<br />

⎟<br />

E ⎠<br />

E ⎞<br />

⎟<br />

E ⎠<br />

sample<br />

reference<br />

⎞<br />

⎟<br />

⎟<br />

−1⎟<br />

⋅1000<br />

⎟<br />

⎟<br />

⎠<br />

(1)<br />

As isotope signature values are rather small, the number is converted into 0 / 00 . h E and l E represent<br />

the relative abundance of heavy and light isotope of element E, respectively, in the sample and in an<br />

international reference standard (4). If isotope signatures are studied on more than one element,<br />

information on specific reaction mechanisms can be derived.<br />

As during the course of a reaction (e.g. a bond breaking or formation) the isotopes of a given<br />

element E present in the substrate do not react with the same rate constant, one of the isotope can be<br />

enriched in the substrate. This effect is called Kinetic Isotopic Effect (KIE E ). Generally, the light<br />

isotope reacts faster than the heavy one, so that the heavy isotope is enriched in the substrate.<br />

Normally, this enrichment is independent of the concentration of the compound; therefore an<br />

enrichment factor for the element E (ε E ) can be calculated, ε E is commonly reported in per mil<br />

(‰)(6):<br />

h<br />

⎛ 1000 + δ E ⎞ ε<br />

E<br />

ln<br />

⎜<br />

= ⋅ ln<br />

h<br />

1000 E<br />

⎟<br />

⎝ + δ<br />

0 ⎠ 1000<br />

f<br />

(2)<br />

Where f is the fraction of compound that has not reacted (usually c(t)/c(t=0)), δ h E and δ h E 0 are the<br />

isotopic signatures of the compound for the element E at times t and zero, respectively. As<br />

explained above changes in isotope signature (∆δE) are due to different reaction kinetics of the<br />

isotopes. ε E -values can dependent on environmental conditions.<br />

Considering the reaction mechanisms it is possible to calculate an apparent kinetic isotope effect<br />

(AKIE E ). This can be directly derived from the experimentally observed ε E . AKIE E can be<br />

calculated as follow (6):<br />

AKIE E<br />

=<br />

l k obs<br />

h k obs<br />

=<br />

1<br />

1+ λ ⋅ε E<br />

1000<br />

If only one atom of the element E is present in the molecule and this atom is taking part to the<br />

reaction, λ is equal 1. If several atoms of the same element are present in a contaminant, those not<br />

taking part in the reaction will decrease the observable isotope fractionation and the corresponding<br />

ε E -value due to isotopic dilution (7). It is important to know the reaction mechanisms so that the<br />

element involved in the different biodegradation reactions can be defined. Bond cleavage or<br />

creation have different effects on KIE and therefore on ε E. Enrichment factors are directly dependent<br />

on reaction mechanisms (4). In addition, it is important to distinguish between primary isotope<br />

effects and secondary isotope effects. Primary isotope effects are observable on atoms involved in a<br />

bond cleavage or formation. Secondary isotope effects are observable on atoms that are not directly<br />

taking part to the cleavage or formation reaction. Normally primary isotope effects are bigger than<br />

secondary. Hydrogen has a big weight difference between its isotopes, so that often secondary<br />

isotope effects for this atom are experimentally accessible (4).<br />

(3)<br />

3


Term paper, June 2007<br />

Unfortunately, the exact values for the kinetic isotope effect for NB degradation reactions are not<br />

known yet. As point out above, the products of the NB biodegradation are not always conclusive<br />

for the distinction of the pathways; one of the advantages of using CSIA is that you measure only<br />

the change in isotopic signature in the substrate (NB).<br />

2. Goals<br />

Goal of this term paper is to asses the magnitude of isotope fractionation of the two alternative NB<br />

degradation pathways that is reductive and oxidative. This means to discuss the main elementary<br />

reactions steps that lead to a substantial isotope effect.<br />

In the following chapters, I review the elementary reaction steps, for NB oxidation and reduction,<br />

where bond are broken or bonding between the elements is changed significantly. In other words,<br />

this means that I try to identify where elementary reaction steps can cause a primary isotope effect.<br />

Since secondary isotope effects are usually one order of magnitude smaller and are more difficult to<br />

exploit for to the identification of isotope fractionation (4).<br />

Transport processes shows a negligible isotope effect and therefore masks isotope effect caused by<br />

bond cleavage if transport is limiting. In this work, we assume that transport processes do not limit<br />

the kinetic of NB transformation. Thus, I discuss isotope effects that are linked to bond cleavage<br />

and formation. The results of this research can than be applied for the design isotope fractionation<br />

experiment in laboratory and field.<br />

3. Results and Discussion<br />

3.1. Oxidative Pathway<br />

Comamonas sp.strain JS765 is able to oxidise NB: product of this reaction is catechol, whereas<br />

nitrite is released. Figure 2 gives an overview of the elementary reaction steps taken in<br />

consideration. First NB enter into the bacteria (1); second NB binds to the enzyme responsible for<br />

the oxidation (2). After the formation of the enzyme substrate complex, two atoms of oxygen are<br />

added (3), finally catechol is produced and nitrite is released (4). To understand how elementary<br />

reaction can influence isotopic enrichment factors and which kind of enrichment factors can be<br />

expected, a closer look at the processes influencing this reaction is necessary. Therefore one needs<br />

to understand enzymatic reaction.<br />

Figure 2: overview of the elementary reaction steps occurring until nitrite is released (breaking of the C-N<br />

bond). E = NBDO (Nitrobenzene dioxygenase), S = NB, P = Catechol. Elementary reaction steps: 1) NB<br />

4


Term paper, June 2007<br />

enters in to the bacteria and it is transported to the reactive-site of NBDO (E); 2) NB bind to the active site of<br />

NBDO, the complex “ES” is built; 3) Dioxygenase reaction: two atoms of oxygen are added 4) Catechol is<br />

produced, Nitrite is released.<br />

Unfortunately, less is known about the transport of NB into the bacteria as well as the transport to<br />

the active site. The rate constant of each elementary reaction step is important for determine isotope<br />

effects. The overall reaction rate for the dioxygenation is determined by the rate of the slowest step<br />

(18). In part 3.1.1. the effects of elementary reaction steps 3 and 4 on isotope fractionation are<br />

discussed in detail.<br />

3.1.1. Enzyme description, active-site and substrate binding<br />

In this chapter, a closer look to the elementary reaction step 2 in figure 2 will be taken.<br />

Nitrobenzene dioxygenase (NBDO) from Comamonas sp.strain JS765 is able to add two atoms of<br />

oxygen to NB. Two electron and two protons are consumed during this process. As result a<br />

dihydroxyl intermediate (EP in figure 2) is produced. Through spontaneous rearrangement a<br />

molecule of nitrite is released and a molecule of catechol (P in figure 2) is formed (5).<br />

NBDO from Comamonas sp.strain JS765 was molecularly characterised by Lesser et al.(2001) (13).<br />

Successful purification and characterisation of all enzyme components were reached by Parales et al<br />

(2005) (17). Based on gene order and degree of sequence similarity NBDO belongs to the<br />

naphthalene family of Rieske nonheme iron dioxygenases (RDOs) (13). Three main components, a<br />

reductase, a ferrodoxin and a dioxygenase, build the multicomponent enzyme system. NBDO (the<br />

dioxygenase component) is a hexamer composed of three α and three β subunits. The active site is<br />

in a α subunit. Figure 3 shows how the multicomponent enzyme system works. The dioxygenase<br />

reaction takes place only when the active-site iron is in the reduced form (5).<br />

Figure 3: Electron transfer chain in a Rieske nonheme iron dioxygenase (RDO) enzyme system. (Modified<br />

from (2)) Both the ferrodoxin component and the dioxygenase component contain a [2Fe2s] iron sulfur<br />

cluster responsible for the electron transfer. The dioxygenase contain also an iron atom in the active-site<br />

The active site, which has an oval-shaped form, is formed by seventeen amino acid residues. Most<br />

of them are hydrophobic and provide an appropriate environment for the binding of aromatic<br />

substrate (5). However only three residues distinguish the NBDO activity from the activity of the<br />

others RDOs. Those are: an aspargine whose amino group is able to form a hydrogen bond with the<br />

nitro groups of nitrobenzene, an isoleuctine and a phenylalanine which are important for the correct<br />

positioning of the substrate and the dimension of the active pocket (10, 12). The formation of the<br />

hydrogen bond is represented in figure 2 as “ES” after elementary reaction step 2.<br />

5


Term paper, June 2007<br />

NBDO has high similarity with other RDOs. For example naphthalene dioxygenase (NDO) has<br />

80% of sequence identity with NBDO (5) the reductase and ferrodoxin components of NBDO are<br />

identical of this of 2-Nitrotoluene Dioxygenase (2-NTDO) (13). This explain the ability of NBDO<br />

to use as substrate compound such as naphthalene, 2-nitrotoluene, 3-nitrotoluene, 2, 4-<br />

dinitrotoluene. Figure 4 shows the iron molecule in the active site and the hydrogen bond between<br />

NB and the amino group of aspargine.<br />

Figure 4: in red, the iron at the active site coordinated by two histidines, one aspargine and two molecule of<br />

water (not shown). The amino group of the aspargine is able to form a hydrogen bond with the nitro group of<br />

NB (Modified from (5))<br />

3.1.2. Reaction mechanism: dioxygenation and release of Nitrite<br />

Here elementary reaction 3 and 4 in figure 2 are discussed. Boyd et al (2005) (2) investigated the<br />

possible mechanisms for the dioxygenation of aromatic compounds. Figure 5 shows the two<br />

possible dioxygenation pathways for NB. It is demonstrate that both oxygen atoms come from the<br />

same oxygen molecule, so that two consequent monooxygenation reactions are to exclude (15). In<br />

case A oxygen atoms are added sequently, while in case B both atoms are added simultaneously. It<br />

is not known which of the two mechanisms is used by the enzyme; however since it is suggested<br />

that case B might be the used one (2), here isotopic fractionation consideration are based on case B.<br />

During the reduction reaction a C-C double bond is transformed to a C-C single bond, two O-C<br />

bonds are formed and a C-N bond is broken. For the analysis of the relevant elementary reaction<br />

steps the time of the release of nitrite plays a central role. It is not clear yet if nitrite is released from<br />

the dihidroxyl intermediate (ES in figure 2) during the addition of oxygen (case 1) or after the<br />

oxygen addition (case 2). However, the fact that the release of nitrite is involved in the limiting step,<br />

supports the thesis that nitrite is released during the addition of oxygen (15).<br />

If we assume that the C-N bond is broken during the addition of oxygen (case 1) primary isotope<br />

effect will be measurable for carbon and for nitrogen. On the other hand, if nitrite is released after<br />

the addition of oxygen (case 2), primary isotope effect will be observable only for carbon.<br />

Indicative substantial AKIE values for the cleavage of a double C-C bond is 1.01. AKIE value for<br />

the cleavage of a C-N bond is 1.03 for both elements (carbon and nitrogen) (4).<br />

Important to say is that hydrogen might undergo to an important secondary isotope effect.<br />

Hydrogen is not directly involved in a bond cleavage or formation reaction. However due to the big<br />

6


Term paper, June 2007<br />

difference in the weight between the two hydrogen isotopes, even a small isotope effect might leads<br />

to measurable enrichment factor.<br />

Figure 5: possible catalytic mechanisms for NB dioxygenation; case A: sequently addition of the O atoms,<br />

case B: simultaneously addition of the O atoms. In blue the dihidroxyl intermediate. (Modified from (2))<br />

3.2 Reductive Pathway<br />

Pseudomonas pseudoalcaligenes strain JS45 is able to reduce NB: a product of the reduction<br />

reaction is nitrosobenzene. As the formation of nitrosobenzene is the only step which cause a<br />

measurable isotope effect, only this reaction is here taken in consideration. Figure 6 shows the<br />

elementary reaction steps occurring until the first bond is broken (N-O bond). First NB enter into<br />

the bacteria (1); second NB binds to the enzyme responsible for the reduction (2). After the<br />

formation of the enzyme substrate complex, two electrons are added (3), finally nitrosobenzene is<br />

released (4) (14). In the same way as for the oxidative pathway, we assume that the rate limiting<br />

step is the step where a bond is broken. In this case elementary reaction steps 4. A primary isotope<br />

effect will so be observable only for two elements. Those are nitrogen and oxygen.<br />

7


Term paper, June 2007<br />

Figure 6: overview of the elementary reaction steps occurring until nitrosobenzene is produced (breaking of<br />

the N-O bond). E = nitrobenzene nitroreductase, S = NB, P = Nitrosobenzene<br />

Elementary reaction steps: 1) NB enters in to the bacteria and it is transported to the reactive-site of<br />

nitrobenzene nitroreductase; NB bind to the active site of nitrobenzene nitroreductase, the complex “ES” is<br />

built; 3) Reduction reaction: addition of two electrons; 4)The product nitrosobenzene is released.<br />

The reaction can be summarized as follow:<br />

Ar-NO 2 + 2e - +2H + ! Ar-NO + H 2 O<br />

3.2.1 Enzyme description: reaction mechanism<br />

Nitobenzene nitroreductase was purified and characterized by Somerville et al.(1995)(20).The<br />

enzyme does not have metal cofactors. It was found that two FMN (Flavin mononucleotide)<br />

molecule are bonded to the protein as cofactor (20). The reduction reaction is NADH dependent<br />

(14). Nitrobenzene nitroreductase belongs to the oxygen insensitive (type 1) enzyme (20). This<br />

category of enzyme uses a two electrons reduction. In contrast oxygen sensitive enzyme (type 2)<br />

catalyses a one electron reduction of the nitro group: a nitro anion radical is built. The radical reacts<br />

than spontaneously with oxygen building a superoxyde radical so that the nitro group is regenerated<br />

and no net reduction of the nitro group is observable (19). A two electrons reduction reduces the<br />

nitro group irrespective of the presence of oxygen.<br />

To figure out the mechanisms of the NB reduction scientists studied the reduction of NB by<br />

NAD(P)H nitroreductase by Enterobacter cloacae. Unfortunately the mechanism of two electrons<br />

reduction of nitroaromatics is not enough understood to provide any information about isotope<br />

fractionation (16). The nitro group is a facile electron acceptor. Many enzymes are able to catalyse<br />

the reduction of aromatic nitro group. For example cytochrome c reductase, cytochrome P-450<br />

reductase, glutathione reductase, hepatic NAD(P)H reductase and many others are able to catalyse<br />

the reduction. One should note that the physiological role of this enzyme is not the reduction of<br />

aromatic nitro group (20). Interestingly cytochrome P-450 reductase has analogously to<br />

nitrobenzene nitroreductase a FMN and a FAD (flavin adenin dinucleotide) molecules as cofactors.<br />

In fact both enzyme are flovoenzyme (11). NB is a substrate for cytochrome P-450 reductase (3).<br />

The proposed mechanisms for the reduction of NB for both enzyme is a ping pong mechanisms (1,<br />

3, 11). Figure 7 represents a possible mechanism. For cytochrome P-450 reductase is suggested that<br />

electrons transfer follows the pathway NADH! FAD ! FMN ! electrons acceptor. Probably the<br />

binding-site for NADH is a cysteine residue (3).<br />

8


Term paper, June 2007<br />

During the reductive degradation pathway of NB, Nitrosobenzene reacts fast to the next metabolite<br />

hydroxylaminobenzene (11, 14). Due to this fast reaction it is hypothesized that nitrosobenzene<br />

does not leave the enzyme and through the consumption of another NADH, nitrosobenzene is<br />

reduced to hydroxylaminobenzene (11).<br />

1)<br />

E + NADH E---NADH EH -<br />

E + S 1<br />

ES 1<br />

E 1<br />

2)<br />

EH - +ArNO 2<br />

EH - ---ArNO 2 E+ArNO<br />

E 1 + S 2<br />

E 1 S 2 E + P<br />

Figure 7: Possible mechanism for NB reduction: Ping Pong mechanism. (Modified from (1)). 1): The first<br />

substrate (NADH) binds to the enzyme and reduces it, conformational change occurs. 2): The reduced<br />

enzyme is now able to bind the second substrate (NB). After the reduction of NB and production of<br />

nitrosobenzene, the enzyme returns to the beginning state.<br />

Summarizing during the reduction of NB an N-O bond is broken. The N atom and the O atom will<br />

undergo to a primary isotope effect. Since we assume that elementary reaction step 4 in fig. 6 is the<br />

rate limiting step, the primary isotope effect will be measurable. Indicative substantial AKIE values<br />

for the cleavage of a N-O bond are about 1.03 for nitrogen and 1.04 for oxygen (4).<br />

3.3. Expected bulk enrichment factor for NB<br />

Using equation 3 it is possible to calculate the enrichment factors (ε E ) for atom E. Due to the<br />

different enzymatic reaction mechanisms, different dilution factors are expected.<br />

3.3.1. NB oxidation<br />

Parameters:<br />

C-C double bond transformation to C-C single bond:<br />

• Dilution factor: 3 (λ-value: 6/2)<br />

• AKIE C =1.01(4)<br />

•<br />

ε<br />

C<br />

≅ −10 0 00<br />

C-N cleavage:<br />

• Dilution factor for element C: 6 (λ-value:6)<br />

• AKIE C =1.03 (4)<br />

•<br />

ε<br />

C<br />

≅ −30 0 00<br />

• Dilution factor for element N: 1 (λ-value:1)<br />

• AKIE N =1.03 (4)<br />

• ε<br />

N<br />

≅ −30 0 00<br />

9


Term paper, June 2007<br />

Enrichment factor for carbon (ε C ):<br />

Case 1: nitrite is released during the addition of oxygen<br />

0 1 ⎛ 2<br />

10 0 ⎞<br />

ε 30<br />

00<br />

00<br />

⎟ ≅ −8 0<br />

C<br />

≅ − ⋅ + ⎜−<br />

⋅<br />

6 ⎝ 6 ⎠ 00<br />

Case 2: nitrite is released after the addition of oxygen<br />

2<br />

ε 0 3<br />

00<br />

0<br />

C<br />

≅ −10 ⋅ ≅ −<br />

6 00<br />

Enrichment factor for nitrogen (ε N ):<br />

Case 1: nitrite is released during the addition of oxygen<br />

1<br />

ε 0 30<br />

00<br />

0<br />

N<br />

≅ −30 ⋅ ≅ −<br />

1 00<br />

Case 2: nitrite is released after the addition of oxygen<br />

ε = 0<br />

N<br />

3.3.2. NB reduction<br />

Parameters:<br />

N-O bond cleavage:<br />

• Dilution factor for element N: 1 (λ-value:1)<br />

• AKIE N =1.03 (4)<br />

• ε<br />

N<br />

≅ −30 0 00<br />

• Dilution factor for element O: 2 (λ-value:2)<br />

• AKIE O =1.04 (4)<br />

• ε ≅ −40 0<br />

O<br />

00<br />

Enrichment factor for nitrogen (ε N ):<br />

1<br />

ε 0 30<br />

00<br />

0<br />

N<br />

≅ −30 ⋅ ≅ −<br />

1 00<br />

Enrichment factor for oxygen (ε O ):<br />

1<br />

ε 0 20<br />

00<br />

0<br />

O<br />

≅ −40 ⋅ ≅ −<br />

2 00<br />

4. Conclusion<br />

The results of this review show that a determination of the fate of NB in contaminated areas with<br />

CSIA should be possible. Different elements are involved in the oxidation and reduction reaction.<br />

ε C is expected to be between -8 0 / 00 and -3 0 / 00 for the oxidative pathway and 0 0 / 00 for the reductive<br />

pathway. ε N is expected to be about -30 0 / 00 for the reductive pathway. It is not possible to predict if<br />

nitrogen will be enriched in the oxidative pathway. If it is the case, the ε N value will be also of -<br />

30 0 / 00 . Oxygen is enriched in reductive pathway; unfortunately nowadays it is not possible to<br />

measure its isotopic signature with certainty. Therefore carbon is the best candidate for the<br />

determination of the pathway.<br />

10


Term paper, June 2007<br />

5. References<br />

1. Anusevicius, Z., A. Soffers, N. Cenas, J. Sarlauskas, M. Martinez-Julvez, and I.<br />

Rietjens. 1999. Quantitative structure activity relationships for the electron transfer<br />

reactions of Anabaena PCC7119 ferredoxin-NADP(+) oxidoreductase with nitrobenzene<br />

and nitrobenzimidazolone derivatives: mechanistic implications. Febs Letters 450:44-48.<br />

2. Boyd, D. R., and T. D. H. Bugg. 2006. Arene cis-dihydrodiol formation: from biology to<br />

application. Organic & Biomolecular Chemistry 4:181-192.<br />

3. Cenas, N., Z. Anusevicius, D. Bironaite, G. I. Bachmanova, A. I. Archakov, and K.<br />

Ollinger. 1994. The Electron-Transfer Reactions of Nadph-Cytochrome P450 Reductase<br />

with Nonphysiological Oxidants. Archives of Biochemistry and Biophysics 315:400-406.<br />

4. Elsner, M., L. Zwank, D. Hunkeler, and R. P. Schwarzenbach. 2005. A new concept<br />

linking observable stable isotope fractionation to transformation pathways of organic<br />

pollutants. <strong>Environmental</strong> Science & Technology 39:6896-6916.<br />

5. Friemann, R., M. M. Ivkovic-Jensen, D. J. Lessner, C. L. Yu, D. T. Gibson, R. E.<br />

Parales, H. Eklund, and S. Ramaswamy. 2005. Structural insight into the dioxygenation<br />

of nitroarene compounds: the crystal structure of nitrobenzene dioxygenase. Journal of<br />

Molecular Biology 348:1139-1151.<br />

6. Hartenbach, A., T. B. Hofstetter, M. Berg, J. Bolotin, and R. P. Schwarzenbach. 2006.<br />

Using nitrogen isotope fractionation to assess abiotic reduction of nitroaromatic compounds.<br />

<strong>Environmental</strong> Science & Technology 40:7710-7716.<br />

7. Hofstetter T., H. A., Tobler N. and Bolotin J. 2007. Labguide on the course Compound-<br />

Specific Isotope Analysis (CSIA). <strong>ETH</strong> Zürich.<br />

8. Hughes J.B., K. H. J., Nishino S.F., Spain J. C., and Zhongqi H. . 2000. Biodegradation<br />

of nitroaromatic compounds and explosives. Chapter 2, Strategies for Aerobic Degradation<br />

of Nitroaromatic Compounds by Bacteria: Process Discovery to Field Application.<br />

9. Hughes J.B., K. H. J., Spain J. C. 2000. Biodegradation of nitroaromatic compounds and<br />

explosives. Chapter 1, Introduction.<br />

10. Ju, K. S., and R. E. Parales. 2006. Control of substrate specificity by active-site residues in<br />

nitrobenzene dioxygenase. Applied and <strong>Environmental</strong> Microbiology 72:1817-1824.<br />

11. Koder, R. L., and A. F. Miller. 1998. Steady-state kinetic mechanism, stereospecificity,<br />

substrate and inhibitor specificity of Enterobacter cloacae nitroreductase. Biochimica Et<br />

Biophysica Acta-Protein Structure and Molecular Enzymology 1387:395-405.<br />

12. Lee, K. S., J. V. Parales, R. Friemann, and R. E. Parales. 2005. Active site residues<br />

controlling substrate specificity in 2-nitrotoluene dioxygenase from Acidovorax sp strain<br />

JS42. Journal of Industrial Microbiology & Biotechnology 32:465-473.<br />

13. Lessner, D. J., G. R. Johnson, R. E. Parales, J. C. Spain, and D. T. Gibson. 2002.<br />

Molecular characterization and substrate specificity of nitrobenzene dioxygenase from<br />

Comamonas sp strain JS765. Applied and <strong>Environmental</strong> Microbiology 68:634-641.<br />

14. Nishino, S. F., and J. C. Spain. 1993. Degradation of Nitrobenzene by a Pseudomonas-<br />

Pseudoalcaligenes. Applied and <strong>Environmental</strong> Microbiology 59:2520-2525.<br />

15. Nishino, S. F., and J. C. Spain. 1995. Oxidative Pathway for the Biodegradation of<br />

Nitrobenzene by Comamonas Sp Strain Js765. Applied and <strong>Environmental</strong> Microbiology<br />

61:2308-2313.<br />

16. Nivinskas, H., S. Staskeviciene, J. Sarlauskas, R. L. Koder, A. F. Miller, and N. Cenas.<br />

2002. Two-electron reduction of quinones by Enterobacter cloacae NAD(P)H :<br />

nitroreductase: quantitative structure-activity relationships. Archives of Biochemistry and<br />

Biophysics 403:249-258.<br />

17. Parales, R. E., R. Huang, C. L. Yu, J. V. Parales, F. K. N. Lee, D. J. Lessner, M. M.<br />

Ivkovic-Jensen, W. Liu, R. Friemann, S. Ramaswamy, and D. T. Gibson. 2005.<br />

11


Term paper, June 2007<br />

Purification, characterization, and crystallization of the components of the nitrobenzene and<br />

2-nitrotoluene dioxygease enzyme systems. Applied and <strong>Environmental</strong> Microbiology<br />

71:3806-3814.<br />

18. Rene P. Schwarzenbach, P. M. G., Dieter M. Imboden. 2003. <strong>Environmental</strong> Organic<br />

Chemistry, Chapter 13: Chemical Transformation I: Hydrolysis and Reactions Involving<br />

Other Nucleophilic Species.<br />

19. Schenzle, A., H. Lenke, J. C. Spain, and H. J. Knackmuss. 1999. Chemoselective nitro<br />

group reduction and reductive dechlorination initiate degradation of 2-chloro-5-nitrophenol<br />

by Ralstonia eutropha JMP134. Applied and <strong>Environmental</strong> Microbiology 65:2317-2323.<br />

20. Somerville, C. C., S. F. Nishino, and J. C. Spain. 1995. Purification and Characterization<br />

of Nitrobenzene Nitroreductase from Pseudomonas Pseudoalcaligenes Js45. Journal of<br />

Bacteriology 177:3837-3842.<br />

12


Biogenic manganese oxides:<br />

Formation mechanisms,<br />

mineralogy and environmental<br />

relevance<br />

Term paper: Biogeochemistry and pollutant dynamics<br />

Thomas Ulrich – 02 923 233<br />

tulrich@student.ethz.ch<br />

Tutor: Dr. Ruben Kretzschmar<br />

Submitted: 12.11.2007<br />

Abstract<br />

Biogenic manganese oxides can be a tool for soil remediation. Recent<br />

papers are reviewed to gather information on their formation mechanisms,<br />

mineralogy and environmental relevance. Characterisations of the manganese<br />

oxidation products of the bacteria groups Bacillus sp., Pseudomonas putida<br />

and Leptothrix discophora are described and compared. The biochemical pathways<br />

of bacterial manganese oxidation are discussed. It seems, that bacteria<br />

are able to produce a soluble Mn(III) complex, for use in redox processes and<br />

iron nutrition. The structures of the biogenic manganese oxides are in the<br />

nanoscale, with sizes around 4 to 100 nm and specific surface areas around 98<br />

to 224 m 2 /g. The biogenic oxides are phyllomanganates with mostly hexagonal<br />

and sometimes triclinic or pseudo-orthogonal structure. The potential of<br />

biogenic manganese oxides in heavy metal scavenging is considerable. Metal<br />

ions of Cd, Co, Hg, Ni, Pb, Zn and U can be adsorbed inexchangeable by biogenic<br />

manganese oxides, and thus become immobile. The adsorption range<br />

of biogenic manganese oxides lies, in the case of Pb, between 200 and 520<br />

mmol P b /mol Mn . The efficiency of adsorption are 2 to 5 times higher than<br />

that of synthetic ones. These differences originate from the poor crystallinity,<br />

small size, high surface area and vacant sites in the crystal structure of biogenic<br />

manganese products.


Contents<br />

1 Introduction 3<br />

2 Manganese oxides in soils 3<br />

2.1 Redox cycle of manganese in soils . . . . . . . . . . . . . . . . . . . . 6<br />

2.2 Relationship of manganese oxides and microorganisms in soils . . . . 7<br />

3 Mechanisms of biogenic manganese oxidation 8<br />

4 Structures of biogenic manganese oxides 11<br />

5 Role of biogenic manganese oxides in soil remediation 16<br />

6 Conclusion 19<br />

List of Figures<br />

1 Strains of manganese oxidising bacteria . . . . . . . . . . . . . . . . . 4<br />

2 Structure of manganese oxides . . . . . . . . . . . . . . . . . . . . . . 5<br />

3 Manganese cycle in the environment . . . . . . . . . . . . . . . . . . 6<br />

4 Manganese oxidation endproduct . . . . . . . . . . . . . . . . . . . . 10<br />

5 Crystal structure of biogenic and synthetic manganese oxides . . . . . 14<br />

6 Complexes of metal cations and manganese oxides . . . . . . . . . . . 16<br />

7 Efficiency of sorption on biogenic and synthetic oxides . . . . . . . . . 18<br />

8 Extractability of biogenic manganese oxides . . . . . . . . . . . . . . 18<br />

List of Tables<br />

1 Types of manganese oxides . . . . . . . . . . . . . . . . . . . . . . . . 5<br />

2 Manganese oxides by different bacteria . . . . . . . . . . . . . . . . . 14<br />

3 Comparison between biogenic and synthetic manganese oxides . . . . 15<br />

4 Comparison of specific surface area . . . . . . . . . . . . . . . . . . . 15<br />

5 Pb adsorption capacity of manganese oxides . . . . . . . . . . . . . . 17


3<br />

1 Introduction<br />

Biogenic manganese (in the following also called Mn) oxides can be good tool for<br />

soil remediation and heavy metal scavenging. The absorption efficiency of biogenic<br />

manganese oxides surpasses those of synthetic oxides and commercial manganese<br />

products (pyrolusite). Improvements in synchrotron based techniques like XANES 1<br />

and EXAFS 2 lead to more detailed information on the small scale properties of<br />

manganese oxides. In this review the specific structures of biogenic manganese<br />

oxides and also the intracellular processes are discussed, to give an understanding<br />

why they have better sorption properties.<br />

Manganese oxides can adsorb arsenic (As), cadmium (Cd), cobalt (Co), mercury<br />

(Hg), nickel (Ni), plutonium (Pu), uranium (U) and Zinc (Zn) cations. In addition<br />

to this, they are also capable of oxidising a lot of organic substances like pesticides.<br />

The production right at the contaminated site may be a further advantage. A major<br />

disadvantage is the oxidation of chromium (Cr) by manganese oxides, a reaction<br />

leading to a toxic product.<br />

Oxidation of manganese is known to be catalysed by a great number of bacteria<br />

and also fungi of different phylogenetic lineages (figure 1). Studies on biogenic<br />

manganese oxides have focused on four model organisms: Bacillus sp. strain SG1<br />

is gram positive and spore-forming. This marine bacterium oxidises Mn(II) on its<br />

spores. Leptothrix discophora strain SS-1: A sheet-forming β-proteobacterium, living<br />

in fresh water. Pseudomonas putida strain MnB1 and GB-1: A γ-proteobacteria<br />

forming biofilms and living in fresh water and soil. KR21-2: a ascomycete fungus<br />

strain.<br />

In the following, the relevance of natural manganese oxides in soils will be discussed.<br />

After that, the intracellular properties which lead to a specific biogenic<br />

product, will be analysed. To understand the potential of biogenic manganese oxides<br />

in contaminated soils, the environmental relevance of different products will be<br />

shown.<br />

2 Manganese oxides in soils<br />

Manganese is an important trace element in soils, which occurs at low concentrations<br />

(1/50 of Fe concentration). By weathering of igneous and metamorphic rock, Mn(II)<br />

is released. This Mn(II) is oxidised to Mn(III) and Mn(IV) in presence of oxygen.<br />

Manganese can form more than 30 known oxide and hydroxide minerals. Sometimes<br />

1 X-ray absorption near edge structure. The absorption spectra are analysed, to identify the<br />

species and their oxidation state.<br />

2 Extended X-ray absorption fine structure. The characteristics of atomic neighbours can be<br />

analysed.


4 Manganese oxides in soils<br />

Figure 1: Strains of bacteria which oxidise Mn(II). (Tebo et al., 2004).<br />

they also appear in combined valence forms, containing both Mn(III) and Mn(IV).<br />

Manganese oxides are characterised by open crystal structures, large surface areas<br />

and high negative charges (Tebo et al., 2004).<br />

Basically manganese oxides are MnO 6 octahedra. These octahedra can be corner-,<br />

edge- or face sharing and thus forming secondary structures like phyllomanganates<br />

and tectomanganates (figure 2). The phyllomanganates consist of layered sheets of<br />

edge-sharing MnO 6 octahedra. Between those sheets water or small cations can be<br />

stored in exchangeable form. Phyllomanganates exist in two forms, separated by the<br />

width of their interlayer: with 7Å (birnessite, chalcophanite and δ-MnO 2 ) and 10Å<br />

(lithiophorite or buserite) d-spacings. The structure with 10Å d-spacing contains an<br />

additional layer of water. 10Å manganese oxides collapse to 7Å phyllomanganates<br />

when they are protonated or dehydrated (Scheinost and Daniel, 2005; Tebo et al.,<br />

2004).<br />

Manganese oxides can also appear in chain/tunnel structures, called tectomanganates.<br />

An example is todorokite (figure 2). Tectomanganates differ in single chain


5<br />

(pyrolusite) to double or triple chains (like todorokite and hollandite). They consist<br />

of edge-sharing octahedra, which are linked by corner-sharing MnO 6 octahedra,<br />

forming tunnels or pseudo-tunnels (see Table 1).<br />

Figure 2: Structures of manganese oxides. Todorokite, ramsdellite and hollandite<br />

are chain/tunnel forms. Birnessite is a phyllomanganate. The barium ions in the<br />

central tunnels of hollandite and the Na, Ca and K cations are not shown. (Tebo<br />

et al., 2004).<br />

.<br />

Table 1: Types of manganese oxides and their structure. (Scheinost and Daniel,<br />

2005).


6 Manganese oxides in soils<br />

In semi arid soils, two forms of manganese oxide minerals are most common:<br />

birnessite and lithiophorite, which are both phyllomanganates. δ-MnO 2 is most often<br />

compared to biogenic manganese oxides (see also section 4). Biological conversions<br />

from phyllomanganates to other structures, like tectomanganates, may occur (Tebo<br />

et al., 2004; Webb et al., 2005b).<br />

2.1 Redox cycle of manganese in soils<br />

Manganese in soils is present in three oxidation states: Mn(II), Mn(III) and Mn(IV).<br />

In absence of oxygen, Mn(II) appears most often in solution or adsorbed to minerals.<br />

Whereas in presence of oxygen Mn(III) and Mn(IV) appear as solid oxides or<br />

hydroxides (Tebo et al., 2004).<br />

Figure 3: Manganese cycle in the environment. In the absence of oxygen Mn(II)<br />

is more abundant. In presence of oxygen, Mn(IV) is more abundant, followed by<br />

Mn(III). (Tebo et al., 2004).<br />

1/2MnO 2 + 2H + + e − −→ 1/2Mn 2+ + H 2 O (1)<br />

Mn 2+ + 1/2O 2 + H 2 O −→ MnO 2 + 2H + (2)<br />

Depending on the local environment manganese can be oxidised and reduced abiotically<br />

in soils. Figure 3 shows the redox cycle of the abiotic manganese oxidation.<br />

The oxidation of Mn(II) to Mn(IV) (equation (2)) is favourable under a high pH<br />

and the presence of oxygen. If the concentration of Mn(II) is low, the oxidation to<br />

Mn(IV) is enforced by the dissociation of the intermediate product Mn(III) (Tebo<br />

et al., 2004). Although the oxidation is thermodynamically possible, the kinetics of


2 Relationship of manganese oxides and microorganisms in soils 7<br />

this reaction are very slow with a half life in the order of hundreds of years. The<br />

rate limiting step is the oxidation of Mn(II) to Mn(III) (Webb et al., 2005a).<br />

The reduction process (equation (1)) is favourable under a low pH and in the<br />

absence of oxygen. Thermodynamically manganese oxides have after oxygen (O 2 )<br />

and nitrate (NO 3 ) one of the highest oxidation potentials. Regarding the kinetics,<br />

they even surpass oxygen. This makes manganese oxides one of the most important<br />

oxidants in soils (Tebo et al., 2004).<br />

2.2 Relationship of manganese oxides and microorganisms<br />

in soils<br />

Bacteria are capable of oxidising Mn(II) to Mn(III) and Mn(IV) (equation (2))<br />

enzymatically. The kinetics of this enzymatically catalysed reaction are a lot faster<br />

than the abiotic reaction, with a half life in the order of days (compared to hundreds<br />

of years). This process will be described in section 3.<br />

Also the reduction (equation (1)) can be catalysed enzymatically by bacteria.<br />

Mn(IV) is used as an electron acceptor in the anaerobic respiration by a lot of<br />

microorganisms. In the following, the focus will lie strictly on the oxidation of<br />

Mn(II) by bacteria.<br />

Observing biogenic manganese oxidation, one of the questions is, why bacteria<br />

oxidise Mn(II). There are assumptions, that manganese oxidation by bacteria is an<br />

accidental occurrence or an evolutionary remainder (Tebo et al., 2005). But there are<br />

also some indications, that bacteria can use manganese oxidation for their benefit.<br />

One possibility is, that bacteria use manganese oxidation to derive energy for<br />

chemolithoautotrophic growth. Oxidising Mn(II) to Mn(III) or Mn(IV) is thermodynamically<br />

favourable, but there is still no distinct evidence, that bacteria oxidise<br />

Mn(II) for ATP generation. Producing storage for an electron acceptor is a more<br />

likely option. Thus an electron acceptor could be stored, until carbon and energy<br />

become available again (Tebo et al., 2005).<br />

Another reason for biogenic manganese oxidation could be the use of manganese<br />

in cellular mechanisms. Manganese can be used as an antioxidant, protecting cells<br />

from reactive oxygen species (ROS). These are, e.g. the superoxide radical, hydroxyl<br />

radical, hydrogen peroxide or singlet oxygen. ROS can be produced by cells as<br />

by-products of respiration. With Mn(II) oxidation, bacteria are able to protect<br />

themselves, even if they do not posses a superoxide dismutase, which is the option<br />

most often used for ROS scavenging. An open question here is, whether the oxidation<br />

of Mn(II) is used intracellular or on the innermembrane, because the bacteria seem<br />

to precipitate manganese oxides extracellular. It was speculated, that the bacteria<br />

use manganese oxidation to protect themselves from oxidants in their environment<br />

(Tebo et al., 2005).


8 Mechanisms of biogenic manganese oxidation<br />

In addition to the mentioned gains of biogenic manganese oxidation, bacteria can<br />

protect themselves with a coating of manganese oxides. This could protect them<br />

from UV radiation, predation, viral attacks or heavy metal toxicity (Tebo et al.,<br />

2005).<br />

An other advantage of manganese oxidation is the ability of manganese oxides<br />

to degrade humic substances oxidatively to smaller compounds. These compounds<br />

can be used by the entire microbial community for growth. Evidence for this is the<br />

faster rate of biomass accumulation in a monoculture actively oxidising manganese,<br />

compared to a monoculture without manganese oxidation (Tebo et al., 2005).<br />

Also an option could be the usage of Mn(III) as competitor for Fe(III) on<br />

siderophores. Iron (Fe) is a critical micro nutriment for almost all bacteria. Some<br />

organisms, including plants, use siderophores to make Fe(III) in rocks bioavailable.<br />

To transport iron into the cell, it has to be released from the siderophore and reduced<br />

to Fe(II). Mn(III) could as well compete Fe(III) on siderophores, as reducing<br />

Fe(III) to Fe(II). This will also be discussed later in section 4.<br />

3 Mechanisms of biogenic manganese oxidation<br />

Basically, the oxidation of Mn(II) by bacteria could be reached by two ways. Bacteria<br />

can catalyse the oxidation indirectly by influencing chemical parameters or they<br />

can directly oxidise the manganese enzymatically. This review will focus on the<br />

enzymatic oxidation.<br />

It is most probable, that enzymes of the multi copper oxidase (MCO) family are<br />

involved in the oxidation of manganese. The MCO family includes a great number<br />

of proteins, which are copper dependent. They are found in prokarya as well as in<br />

eukarya. Where they are for example responsible in the oxidation of Fe. To prove<br />

that the oxidation step of manganese in Bacillus sp. is copper dependent, Francis<br />

and Tebo (Francis and Tebo, 2002) used the copper chelator o-phenanthroline at<br />

a concentration of 50 µM. After addition of o-phenanthroline the activities of all<br />

proteins were inhibited, showing that manganese oxidation is copper dependent.<br />

Tebo et al. (Tebo et al., 2004) found the MCO gene mnxG in Bacillus sp.. Very<br />

similar genes were also found in Pseudomonas putida and Leptothrix discophora and<br />

many other bacteria. This suggests that they all use a similar pathway for oxidising<br />

manganese, utilising enzymes from the multicopper oxidase enzyme family. However,<br />

the exact proteins involved in this process have not yet been purified (Tebo et al.,<br />

2004). Differentiation has to be made, between the direct catalysis of Mn(II) by<br />

MCO enzymes and their mere involvement in the pathway of Mn(II) oxidation.<br />

Proteins of the MCO family could be expressed as precursors or side effects of<br />

manganese oxidation without direct involvement in the oxidation step itself (Tebo<br />

et al., 2004).


9<br />

Three pathways of oxidising Mn(II) would be possible:<br />

Mn(II) enzymatic<br />

−−−−−−→ Mn(IV ) (3)<br />

Mn(II) enzymatic<br />

−−−−−−→ Mn(III) chemical<br />

−−−−−→ Mn(IV ) (4)<br />

Mn(II) enzymatic<br />

−−−−−−→ Mn(III) enzymatic<br />

−−−−−−→ Mn(IV ) (5)<br />

Enzymatic oxidation of Mn(II) to Mn(IV) in a two electron transfer step (equation<br />

(3)). Enzymatic oxidation of Mn(II) to Mn(III) in a single electron transfer<br />

step, followed by a chemical dissociation of Mn(III) into Mn(II) and Mn(IV) (equation<br />

(4)). Enzymatic oxidation of Mn(II) to Mn(III) in a one electron transfer step,<br />

followed by a second one electron transfer step to Mn(IV) (equation (5)).<br />

In antagonism to equation (3), Toner et al. (Toner et al., 2005) showed the<br />

presence of an Mn(III) intermediate in Pseudomonas putida. Webb et al. (Webb<br />

et al., 2005a) showed the presence of a Mn(III) intermediate in spores of Bacillus<br />

sp. strain SG-1. So the oxidation of manganese with a two electron transfer is<br />

improbable.<br />

Comparing equation (4) and (5) most authors support the pathway of two enzymatically<br />

catalysed one electron transfers (equation (5)) (Francis and Tebo, 2002;<br />

Tebo et al., 2004, 2005; Toner et al., 2005; Webb et al., 2005a). This pathway would<br />

also be analogous to the pathway, with which bacteria and eukarya are oxidising<br />

Fe(II). Evidence has also been found, that the second step of the Mn(II) oxidation<br />

works independently from the first step (Tebo et al., 2004).<br />

These findings lead to the question regarding speciation of the Mn(III) intermediate.<br />

Tebo et al. (Tebo et al., 2004, 2005) and Toner et al. (Toner et al.,<br />

2005) differ in their arguments. Toner et al. (Toner et al., 2005), who used XANES<br />

and STXM 3 , argue there is a membrane bound intermediate of Mn(III).Tebo et al.<br />

(Tebo et al., 2004, 2005) used a chemical trapping step with pyrophosphate, which<br />

complexes Mn(III) in solution. They argue that the Mn(III) phase is in solution as<br />

an intracellular Mn- enzyme- complex.<br />

Mn(II) oxidation seems to take place inside the cell and by a membrane bound<br />

process. The one-electron transfer process from Mn(II) to Mn(III) seems to take<br />

place inside the cell plasma. The oxidation of Mn(III) to Mn(IV) appears to be a<br />

membrane bound process and the final product precipitates around the cell (Toner<br />

et al., 2005). This would include proteins and enzymes for the transport of Mn(III)<br />

from cell plasma to the membrane. This proteins have not yet been found. The<br />

transport would also account for the fact, Tebo et al. (Tebo et al., 2004) found<br />

3 Scanning transmission X-ray microscopy. Used to study the spatial resolved characterisation<br />

of manganese oxides.


10 Mechanisms of biogenic manganese oxidation<br />

Mn(III) in solution. Mn(III) could be complexed by pyrophosphate, before it reaches<br />

the membrane by enzyme / pyrophosphate competition in this study. Perhaps bacteria<br />

even have some mechanisms to store Mn(III)-enzyme complexes in or at the<br />

membrane, to be released when needed. Considering the time, when the product is<br />

precipitated, several authors showed that first Mn(II) in solution is diminished and<br />

then Mn(III) and Mn(IV) concentration rises (Tebo et al., 2004; Toner et al., 2005).<br />

In the authors opinion, Mn(III) complexes produced by bacteria, could be very<br />

important for the environment. Mn(III) is a strong oxidant, which may be used to<br />

free Fe(III) from siderophores, using Mn(III) as a competitor for Fe(III) and thus<br />

making Fe(III) bioavailable (see section 2.2). It could also be used by bacteria in<br />

redox reactions. Thus Mn(II) oxidation may be a mechanism, developed by bacteria<br />

to produce Mn(III) in solution. The proteins responsible for this processes have not<br />

yet been found.<br />

Figure 4: Electron microscope pictures of the manganese oxidation endproduct of<br />

P.putida. A and B scanning electron microscope images of the aggregates (10 - 30<br />

µm). C and D show biogenic manganese oxide particles using transmission electron<br />

microscopy. (Toner et al., 2005).<br />

The final product of Mn(II) oxidation outside the cell seems to be almost pure<br />

precipitated Mn(IV), at least at low Mn(II) initial concentrations. An electron microscope<br />

picture of the final product can be seen in figure 4. After some time the<br />

concentration of Mn(III) in the precipitated product rises (Toner et al., 2005). It is<br />

likely, that only Mn(IV) precipitates are produced and later reduced in the presence<br />

of Mn(II) to Mn(III). Evidence for this could be, that at a higher initial Mn(II)


11<br />

concentration, Mn(III) is produced sooner and in higher concentrations (enzyme<br />

bound Mn(III) in solution should not be confused with Mn(III) in the precipitate.).<br />

The precipitation product after 48h consists of Mn(III) and Mn(IV) with an average<br />

oxidation number of 3.7 to 3.9 (Villalobos et al., 2003; Webb et al., 2005b).<br />

The average oxidation numbers are obtained with XANES analysis. Three or more<br />

species with known oxidation state are analysed, than the oxidation state of the<br />

sample is determined with a regression approach. The average oxidation state of<br />

the endproduct depends on the initial Mn(II) concentration.<br />

4 Structures of biogenic manganese oxides<br />

In this section, the structure of biogenic manganese oxides will be discussed. To obtain<br />

information about the structural properties, synthetic manganese oxides were<br />

compared to biogenic manganese oxides. δ-MnO 2 and acid birnessite were formed<br />

through reduction of permanganate in MnCl 2 respectively HCl (Villalobos et al.,<br />

2006). Webb et al. (Webb et al., 2005b) also synthesised triclinic birnessite and<br />

todorokite for comparison. These synthetic oxides were compared to biogenic manganese<br />

oxides produced by bacteria in culture. The manganese oxides were analysed<br />

with XANES, which gives a high resolution spatial characterisation of the elements<br />

and their oxidation state. EXAFS analyse lets determine the atomic neighbours of<br />

certain elements and the type of complexation. Synchrotron based XRD 4 gives high<br />

resolved information about the crystal mesh of the manganese oxide. The surface<br />

areas were measured by a N 2 specific BET 5 method in all cases.<br />

The biogenic manganese oxides produced by the model organisms (see section<br />

1) have general properties. All biogenic manganese oxides showed a very poor crystallinity<br />

(Villalobos et al., 2003; Webb et al., 2005b). Villalobos et al. (Villalobos<br />

et al., 2003) speak of “extremely defective layered compounds with turbotratic<br />

stacking and random stacking faults”. The primary manganese oxides are in the<br />

nanoscale, ranging from 4 to 100 nm (Kim et al., 2004; Nelson et al., 1999). The<br />

manganese oxides form aggregates outside the cell, as shown in section 3. These<br />

aggregates consist of Mn(II), Mn(III) and Mn(IV), where Mn(IV) seems to be the<br />

most frequent species (Webb et al., 2005b; Villalobos et al., 2006). Dependent on<br />

time and initial Mn(II) concentration (or the concentration of other species which<br />

could reduce Mn(IV)), the concentration of Mn(III) may rise in the aggregates. The<br />

most common structure of the aggregation is a hexagonal phyllomanganate (Villalobos<br />

et al., 2003, 2006; Webb et al., 2005b). The nanoscale size of the manganese<br />

oxides results in high specific surface areas of the aggregates in the range between<br />

98 and 224 m 2 /g (Nelson et al., 1999; Villalobos et al., 2005b).<br />

4 X-Ray diffraction. Gives information about the crystal properties.<br />

5 Brunauer-, Emmet-, Teller- theory of adsorption of gas molecules on solid surfaces


12 Structures of biogenic manganese oxides<br />

Biogenic manganese oxides have been compared to synthetic manganese oxides<br />

by several authors (Nelson et al., 2002; Villalobos et al., 2003, 2006; Webb et al.,<br />

2005b). Several synthetic manganese oxides were produced with the methods mentioned<br />

above. Webb et al. (Webb et al., 2005b) found a biogenic manganese oxide<br />

similar to δ-MnO 2 . Villalobos et al. (Villalobos et al., 2003, 2006) stated, that<br />

the physical and chemical attributes of the biogenic manganese oxides are between<br />

δ-MnO 2 and acid birnessite (see also Table 3). Villalobos et al. (Villalobos et al.,<br />

2003, 2006) paid special attention to vacant sites in the crystal. In synthetic triclinic<br />

structures the negative charge, which is responsible for the exchangeable binding of<br />

cations like Na + , Ca 2+ or water, derives from the content of Mn(III). The poor crystalline<br />

structure of biogenic manganese has its negative charge through vacant sites<br />

in the crystal structure (see figure 5) (Villalobos et al., 2003, 2006). Because of this<br />

vacant sites inside the crystal mesh, innersphere complexes can be promoted. They<br />

are responsible for the strong binding of heavy metals (Villalobos et al., 2003, 2006).<br />

The biggest differences between synthetic and biogenic manganese oxides are found<br />

by comparing specific surface areas. The specific surface area of biogenic manganese<br />

oxides is two to four times higher than that of synthetic oxides (Nelson et al., 2002;<br />

Villalobos et al., 2003). Nelson et al. (Nelson et al., 2002), who studied Leptothrix<br />

discophora, found a specific surface area of the biogenic product twice as high as<br />

that of Pseudomonas putida, studied by Villalobos et al. (Villalobos et al., 2003).<br />

See also tables 3 and 4.<br />

Discussing the appearance of manganese oxides in nature, it is of interest, whether<br />

the natural oxides are of biotic or abiotic origin. As shown in section 2.1 the kinetics<br />

of the abiotic reaction (equation (2)) are very slow (Tebo et al., 2004). Comparing<br />

biogenic manganese oxides in culture with manganese oxides found in nature, it is<br />

probable, that most of the natural manganese oxides are of biogenic origin. Products<br />

very similar to the biogenic manganese oxides produced in the laboratories,<br />

have been found in the oxic / anoxic transition zone in the sea and lakes (Granina<br />

and Callender, 2006; Webb et al., 2005b). This gives an evidence, that biogenic<br />

manganese oxides are abundant in nature. From primary biogenic oxides secondary<br />

manganese oxides can develop. This reaction depends on physical and chemical<br />

conditions. Secondary structures could also include tectomanganates (Webb et al.,<br />

2005b).<br />

In the following the more detailed results and the differences of diverse manganese<br />

oxide products will be discussed. In contrast to the hexagonal structure proposed<br />

above, Jurgensen et al. (Jurgensen et al., 2004), who studied Leptothrix discophora,<br />

found a triclinic oxide, which consists of a single octahedral layer of microcrystals<br />

composed of Mn(IV), Mn(III) and Mn(II). This product also showed a very high<br />

specific surface area of 224 m 2 /g (Jurgensen et al., 2004). The products of Leptothrix<br />

discophora were in the range of 4 nm to 100 nm (Kim et al., 2004). Kim et al. (Kim<br />

et al., 2004) suggested, there could be tectomanganates like todorokite, when they


13<br />

studied Leptothrix discophora. These results have later been challenged by Web<br />

et al. (Webb et al., 2005b) and Villalobos et al. (Villalobos et al., 2006), who<br />

stated that there are no primary biogenic manganese oxides with a tectomanganate<br />

structure. They argue, that the use of UV Raman techniques, applied by Kim et<br />

al. (Kim et al., 2004), are not capable of showing an evidence for todorokite, and<br />

the NEXAFS analysis alone showed no distinct evidence for todorokite. Tani et<br />

al. (Tani et al., 2004) however supported the hypothesis of Kim et al. (Kim et al.,<br />

2004).<br />

Webb et al. (Webb et al., 2005b) studied the structure of the manganese oxide<br />

of Bacillus sp.. The product they found, was a biogenic Ca-birnessite phyllomanganate.<br />

In addition to the hexagonal structure mentioned above, they also found a<br />

pseudo-orthogonal phase. After the first 12 h of the reaction, the hexagonal phase<br />

was the dominant form. After some additional time, more of the pseudo-orthogonal<br />

phase seemed to have been formed (Webb et al., 2005b). They assume for thermodynamically<br />

reasons, that secondary biogenic manganese oxides are formed from<br />

primary manganese oxides. In sea water samples both forms were found and supported<br />

to be of biogenic origin (Webb et al., 2005b). The difference between the two<br />

phases is, that pseudo-orthogonal birnessites consist of up to one third of Mn(III),<br />

whereas hexagonal forms mainly consist of Mn(IV) (Webb et al., 2005b). The oxidation<br />

state of manganese found in this study, was between 3.7 and 4.0. The spacing<br />

between the layers was 10Å in both forms (Webb et al., 2005b).<br />

Villalobos et al. (Villalobos et al., 2003, 2006) analysed the structure of the<br />

manganese oxide of Pseudomonas putida. In contrast to Webb at al. (Webb et al.,<br />

2005b), who studied Bacillus sp., they only found the hexagonal form of the oxide.<br />

All products had a very high content of Mn(IV). Triclinic or pseudo-orthogonal forms<br />

were not found. The d-spacing between layers was in this case 7.2 Å, the specific<br />

surface area was 98 m 2 /g. The oxidation state was 3.9 (all data: (Villalobos et al.,<br />

2003, 2006)). Villalobos et al. (Villalobos et al., 2006) showed that the crystals<br />

contained three to six randomly stacked layers. The residual layer charge is thereby<br />

balanced by Na + cations (0.15 per octahedra). The amount of interlayer H 2 O was<br />

three times the amount of interlayer alkali cations. Further, the presence of Mn(II)<br />

was found in the interlayer of the biogenic manganese oxide, propably a remainder of<br />

the Mn(II) substrate. A question not answered by Villalobos et al. (Villalobos et al.,<br />

2003, 2006) is, if the Mn(II) in the interlayer would reduce Mn(III) and Mn(IV).<br />

As shown in this section, the products of bacterial oxidised Mn(II) can differ in<br />

some parts, like the oxidation step (Bacillus sp.: 3.7, Pseudomonas putida: 3.9),<br />

the type of interlayer cations (Bacillus sp.: Ca 2+ ,Pseudomonas putida: Na + ), the<br />

number of layers (Leptothrix discophora: 1, Pseudomonas putida: 3 - 6), the content<br />

of manganese species and the structure (Leptothrix discophora: Mn(II), Mn(III),<br />

Mn(IV), Bacillus sp.: Mn(III) and Mn(IV) , Pseudomonas putida: Mn(II) and<br />

Mn(IV)). The results are summarised in table 2.


14 Structures of biogenic manganese oxides<br />

Figure 5: Idealised crystal structures of: a) Synthetic triclinic birnessite, b) biogenic<br />

hexagonal birnessite. Darkened octahedra: Mn(III) rich zones, balanced by hydrated<br />

cations (not shown). V: Vacancies. (Villalobos et al., 2005b).<br />

Table 2: Structures, physical and chemical properties of manganese oxides by different<br />

bacteria.


15<br />

Table 3: Comparison between biogenic and synthetic manganese oxides. (Villalobos<br />

et al., 2003).<br />

Table 4: A biogenic and synthetic (fresh abiotic) manganese oxide are compared regarding<br />

the specific surface area. Pyrolusite is commercial manganese oxide product.<br />

(Nelson et al., 2002).


16 Role of biogenic manganese oxides in soil remediation<br />

5 Role of biogenic manganese oxides in soil remediation<br />

Biogenic manganese oxides play a significant role in sorption of heavy metals in<br />

the environment. Their ability of inexchangeable sorption of heavy metals and<br />

oxidation of organic substances make them an usefull tool in soil remediation. As<br />

shown in section 4 biogenic manganese oxides have a greater specific surface area<br />

than synthetic manganese oxides. In this section the influence of vacant sites in the<br />

crystal mesh on sorption attributes will be discussed, as well as the general sorption<br />

properties of biogenic manganese oxides.<br />

Villalobos et al. (Villalobos et al., 2005a) ordered the types of possible sorption<br />

mechanisms into two different kinds: a) Adsorption in the interlayer, with about<br />

25 - 50% of the adsorbed metal cations and b) adsorption as surface complex at<br />

the particle edges, with 50 - 75% of the adsorbed metal cations. Later Tebo et al.<br />

(Tebo et al., 2004) suggested a third option: Incorporation into the vacant sites as<br />

substituent for manganese. Metal cations are able to form two different complexes<br />

with oxygen atoms of the crystal mesh. A double corner sharing bidentate complex<br />

or a triple corner sharing tridentate complex (see figure 6)<br />

Figure 6: Possible complexes of metal cations and manganese oxides. In this case<br />

the metal cation is a lead ion. Metal cations can form a) a tridentate, three corner<br />

sharing complex and b) a bidentate, two corner sharing complex. The distances<br />

were measured with EXAFS. (Villalobos et al., 2005a).<br />

Various studies have been conducted on the topic of heavy metal sorption by<br />

biogenic manganese oxides. As, Cd, Co, Hg, Ni, Pb, Pu, U and Zn were analysed<br />

concerning the sorption properties to manganese oxides. All showed very good<br />

sorption qualities. In almost all the cases the adsorption efficiency of manganese


17<br />

oxides exceeded those of iron oxides (reviewed in (Tebo et al., 2004)). Tebo et al<br />

studied the oxidation of U(IV) to U(VI), with following incorporation of U(VI) in<br />

the manganese oxide as a bidentate complex (reviewed in (Tebo et al., 2004)). U(VI)<br />

also showed internal changes in the biogenic manganese oxide, forming todorokitelike<br />

tunnel structures.<br />

Nelson et al. (Nelson et al., 1999) studied the Pb sorption characteristics of the<br />

manganese oxides of Leptothrix discophora. They compared biogenic manganese oxides<br />

to freshly synthesised ones and commercial manganese oxides for heavy metal<br />

sorption. The adsorption results of the abiotic oxides could approach the biogenic<br />

ones, but the biogenic manganese oxides still had about 2 to 5 times higher adsorption<br />

capacity (see Table 5). The adsorption of the biogenic products ranged from<br />

150 (mmol Pb/ mol Mn) to 250 (mmol Pb/ mol Mn) with a maximum of 520 (mmol<br />

Pb/ mol Mn). In comparison to the commercial product, they outperform them by<br />

orders of magnitude (see also Table 5) (Nelson et al., 1999, 2002).<br />

Table 5: Maximum adsorption capacities.<br />

manganese products. (Nelson et al., 2002).<br />

The pyrolusite oxides are commercial<br />

Tani et al. (Tani et al., 2004) analysed the oxidation product of fungus strain<br />

KR21-2 in terms of heavy metal sorption. They focused on Co(II), Ni(II) and Zn(II)<br />

sorption. The study showed, that the metal ions adsorbed to the biogenic product<br />

with higher efficiency than to the abiotic manganese oxides (figure 7). Co(II) and<br />

Ni(II) bound irreversibly to the oxide, while the adsorbed Zn(II) was exchangeable<br />

(figure 8). They used a two step extraction method with CuSO 4 on the manganese<br />

oxides. In a solution with a initial concentration of 0.1mM of biogenic manganese<br />

oxide, 20% of the adsorbed Co(II) and Ni(II) were released (figure 8). The same<br />

extraction with synthetic manganese oxides, released 70% of the metal ions (Tani<br />

et al., 2004). The adsorption efficiency thereby proceeded in the order Co(II) ><br />

Zn(II) > Ni(II) on the biogenic products (figure 7). It is possible that the metal<br />

ions are incoorporated into the crystal strucure of the manganese oxide (Tani et al.,<br />

2004).


18 Role of biogenic manganese oxides in soil remediation<br />

Figure 7: Efficiency of sorption of Co, Ni and Zn on biogenic and synthetic manganese<br />

oxides as a function solid manganese (all closed lines, closed symbols: biogenic,<br />

open symbols: synthetic) and specific surface area (synthetic only, dotted<br />

lines, closed symbols). (Tani et al., 2004).<br />

Figure 8: Extractability of manganese oxides with CuSO 4 . The grey bar gives<br />

the extractability in %. Colums A) B) and C) show special treatments. A: no<br />

treatments, B: 20mM HEPES buffer solution, C: 100 mM NaCl before injection of<br />

metal ions. Initial Mn(II) concentration: 0.2mM. (Tani et al., 2004).


19<br />

One big disadvantage of heavy metal scavenging with biogenic manganese oxides<br />

is oxidability of Cr(III). Cr(VI) is soluble and much more toxic than the insoluble<br />

Cr(III). Manganese oxides are known to be the only oxidants for Cr(III), they are<br />

capable of oxidising Cr(III) to Cr(VI). Additionally, they oxidise Cr(III) approximately<br />

up to seven times faster than synthetic manganese oxides. Manganese oxides<br />

are reduced to Mn(II), which makes the Mn(II) bioavailable again for manganese<br />

oxidation. Thus a small concentration of Mn(II), together with biogenic oxidation<br />

of manganese, can form a lot of soluble Cr(VI) in a cyclic process. When using<br />

biogenic manganese oxides for scavenging heavy metals, the toxicity of Cr(VI) in<br />

the soil has to be considered (Murray and Tebo, 2007; Wu et al., 2005).<br />

6 Conclusion<br />

Biogenic manganese products can be a useful tool in soil remediation since they<br />

can be produced right at the contaminated site and surpass commercial manganese<br />

oxides in the order of magnitudes regarding sorption. Before application of biogenic<br />

manganese oxides in soils the toxicity of chromium has to be analysed.<br />

To fully understand, how the application of manganese oxidising bacteria influence<br />

the soil environment, the following questions should be considered: The terms<br />

for big scale engineering should be analysed. Also more studies on the reversability<br />

of heavy metal sorption are needed. Bacteria, that oxidise manganese, can have a<br />

great impact on the redox environment in nature. The possibility of the storage of<br />

Mn(III) and Mn(IV) ions on the bacterial membrane should be analysed, including<br />

the possible proteins, responsible for storage and intracellular transportation. For<br />

further understanding of manganese oxidising bacteria, studies on manganese oxidising<br />

microbial systems directly in nature should be done. Also the efficiency of<br />

different bacteria strains in producing heavy metal sorbents should be discussed.


20 REFERENCES<br />

References<br />

Francis, C. A. and Tebo, B. M. (2002). Enzymatic manganese(ii) oxidation by<br />

metabolically dormant spores of diverse bacillus species. APPLIED AND ENVI-<br />

RONMENTAL MICROBIOLOGY, 68(2):874–880.<br />

Granina, L. Z. and Callender, E. (2006). The role of biological uptake in iron and<br />

manganese cycling in lake baikal. HYDROBIOLOGIA, 568:41–43.<br />

Jurgensen, A., Widmeyer, J. R., Gordon, R. A., Bendell-Young, L. I., Moore, M. M.,<br />

and Crozier, E. D. (2004). The structure of the manganese oxide on the sheath<br />

of the bacterium leptothrix discophora: An xafs study. AMERICAN MINERAL-<br />

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OF PAPERS OF THE AMERICAN CHEMICAL SOCIETY, 227:U1213–U1213.<br />

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Nelson, Y. M., Lion, L. W., Ghiorse, W. C., and Shuler, M. L. (1999). Production of<br />

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medium and evaluation of their pb adsorption characteristics. APPLIED AND<br />

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Nelson, Y. M., Lion, L. W., Shuler, M. L., and Ghiorse, W. C. (2002). Effect of oxide<br />

formation mechanisms on lead adsorption by biogenic manganese (hydr)oxides,<br />

iron (hydr)oxides, and their mixtures. ENVIRONMENTAL SCIENCE & TECH-<br />

NOLOGY, 36(3):421–425.<br />

Scheinost, A. C. and Daniel, H. (2005). Encyclopedia of Soils in the Environment,<br />

chapter Metal Oxides, pages 428–438. Elsevier, Oxford.<br />

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Sorption of co(ii), ni(ii), and zn(ii) on biogenic manganese oxides produced by<br />

a mn-oxidizing fungus, strain kr21-2. JOURNAL OF ENVIRONMENTAL SCI-<br />

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VIRONMENTAL ENGINEERING, 39(10):2641–2660.<br />

Tebo, B. M., Bargar, J. R., Clement, B. G., Dick, G. J., Murray, K. J., Parker, D.,<br />

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mechanisms of formation. ANNUAL REVIEW OF EARTH AND PLANETARY<br />

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Villalobos, M., Bargar, J., and Sposito, G. (2005b). Trace metal retention on biogenic<br />

manganese oxide nanoparticles. ELEMENTS, 1(4):223–226.<br />

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ICAN MINERALOGIST, 91(4):489–502.<br />

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JOURNAL, 22:161–170.


Carbon nanotube<br />

http://www.nccr-nano.org/ncc<br />

Mobility behaviour of<br />

anthropogenic<br />

nanoparticles in the<br />

hydrosphere<br />

Term paper in Biogeochemistry and<br />

Pollutant Dynamics<br />

arg<br />

arg<br />

http://ina.unizar.es/<br />

by Sarah Conradt<br />

Submission date: 22th June 2007<br />

Tutor: Prof. G. Furrer and Prof. B. Wehrli<br />

C 60 Fullerene<br />

Abstract<br />

Nanotechnology is often referred to as a key technology of the 21 th century. However few is<br />

known on the behaviour of nanoparticles and their potential risks to human health and the<br />

environment, especially to the aquatic environment. This paper deals with the mobility of<br />

nanoparticles in the aquatic phase. Mobility is crucial for determine the fate and finally the<br />

risk emanating from these particles. This review is based on current research on lab studies,<br />

which used silica beads in a column to simulate porous media and Erlenmeyer flasks to<br />

investigate the influence of natural organic matter (NOM) on nanotubes. NOM seems to<br />

stabilize suspended nanotubes to a great extent. The breakthrough behaviour of different<br />

nanoparticles was deviating. Particularly hydrophobicity, size and the special alignment<br />

behaviour seem to be influential parameters for deposition and aggregation of nanoparticles.


1. Introduction<br />

Small, smaller and even smaller – till nothing is visible anymore to the naked eye – but still<br />

smaller! A way down to the microcosm. Welcome in the world of dwarfs, welcome in the<br />

nano world!<br />

It was already in the year 1959 when Richard Feynman, an U.S. physicist and later Nobel<br />

price winner, declared: “There’s plenty of room at the bottom”! With this speech he outlined a<br />

vision of a miniaturized world, which plays at the very end of the size scale with new<br />

promising technical applications and possibilities. This miniaturization found its way into our<br />

daily life in many areas like chips, storage devices and integrated circuits. The scanning<br />

tunnelling microscope (1981) was one outranking step towards this little world, because it<br />

allowed a glance at the nanoscale and confirmed that there is not only room but plenty of it,<br />

as Feynman mentioned. Within this little world, the nano world and its constituent, the<br />

nanoparticle will be looked at in this paper.<br />

‘Nano’ stands for part in a billion, thus 1nm equals to 10 -9 m. To get a better idea of the size,<br />

here a short comparison: in only one human hair 50 000 particles of 1 nm size could be<br />

arranged abreast (SWR2). Size is often used as the only criterion to delineate nanoparticles<br />

from bulk materials and colloids are often used as a synonym (Lead and Wilkinson 2007:2).<br />

In compliance with the I<strong>UP</strong>AC definition, it is sufficient that only one dimension of a particle<br />

fulfills the size criterion (Table 1). As a consequence so called nanotubes, which consist of<br />

long tubes (nanoscale diameter but microscale length), are classified as nanoparticles.<br />

Hyung et al. (2007:179) described nanotubes as “pure carbon macromolecules consisting of<br />

sheets of carbon atoms covalently bonded in hexagonal arrays that are seamlessly rolled<br />

into a hollow, cylindrical shape with both ends rounded through pentagon rings inclusions”.<br />

Carbon nanotubes (CNTs) are further distinguished between single-walled nanotubes<br />

(SWNTs) and multi-walled nanotubes (MWNTs), whereas “the latter results from a coaxial<br />

assembly of the multiple SWNTs” (Hyung et al. 2007:179) . Another important form of carbon<br />

containing nanoparticles are the so called Buckminsterfullerenes (C 60 ). In contrast to<br />

nanotubes, fullerenes are arranged in a spherical configuration, containing both five and six<br />

carbon rings, with a total number of 60 C atoms (Cheng 2005). Fullerols are<br />

polyhydroxylated C 60 nanoparticles which are modified to increase the affinity to the aqueous<br />

phase. Often, nanoparticles are described to represent “an intermediate supramolecular<br />

state of matter between bulk and molecular material” (Moore 2006:967).Thereby<br />

nanoparticles are differentiated from bulk material by having not only a specific small size but<br />

also “novel properties”. Novel properties mean that new physical laws or properties of<br />

materials may evolve by making particles smaller and smaller (Table 1). This is a result of<br />

the increasing surface to volume ratio, which leads to extremely high reactivity as the contact<br />

area increases. For example aluminium in beverage cans is harmless but minimized to nano<br />

size, aluminium is an explosive matter which is used as catalyst for missiles (Technology<br />

Assessment).<br />

Colloids are ubiquitary; they are present in every environment and they can be either<br />

anthropogenic in origin or occur naturally. An example for the latter is the famous Lotuseffect,<br />

where a special nanostructure on the surface of the plant causes so small adhesion<br />

forces that the cohesion forces prevail, thus wetting cannot take place and the surface<br />

remains clean (Technology Assessment).<br />

In the following work only anthropogenic nanoparticles are considered. Released from e.g.<br />

industrial sites, they are transported via the atmosphere, are deposited on soils and water or<br />

enter directly the aquatic environment. Subsequent uptake of nanoparticles by endocytosis<br />

or other mechanisms into the aquatic biota is of major concern (Moore 2006).<br />

2


Table 1: Various definitions of nanoparticles and colloids<br />

Author Nanoparticles Main criterion<br />

(a) I<strong>UP</strong>AC<br />

(provisional<br />

recommendation)<br />

(b) British<br />

Standards<br />

Institution<br />

London<br />

(BSI) 2005<br />

“Microscopic particle whose size is measured in<br />

nanometers”.<br />

“Particle with one or more dimensions at the<br />

nanoscale”.<br />

Nanoscale: “having one or more dimensions of the<br />

order of 100 nm or less”.<br />

size<br />

size<br />

Frequently (small) colloids<br />

are used synonymously to<br />

nanoparticles which is also<br />

done in this work.<br />

Author colloids Main criterion<br />

(a) Filella 2007:18<br />

(b) I<strong>UP</strong>AC 1972<br />

(c) Leppard<br />

1992:233<br />

(d) Filella 2007:17<br />

(e) Lead and<br />

Wilkinson<br />

2006:160<br />

(f) Lead and<br />

Wilkinson 2007:2<br />

(g) Lead and<br />

Wilkinson 2007:2<br />

“Any material which can be brought into a colloidal<br />

solution is nowadays often referred to as a ‘colloid’.”<br />

Colloidal: “a state of subdivision, implying that the<br />

molecules or polymolecular particles dispersed in a<br />

medium have at least in one direction a dimension<br />

roughly between 1 nm and 1µm.”<br />

“An appreciable fraction of the molecules of a colloid<br />

is located at the boundary region between particle and<br />

aquatic milieu.“<br />

Particles are defined as colloids if their surface free<br />

energy dominates the bulk free energy, which requires<br />

a high surface to volume ratio.<br />

“The colloidal fraction can be considered as a<br />

discrete, non-aqueous phase for contaminant binding,<br />

which does not sediment over reasonable timescales<br />

in the absence of further aggregation”.<br />

Brownian motion is in general sufficient to keep<br />

aquatic colloids suspended in the water.<br />

Colloids: “any organic or inorganic entity large enough<br />

to have a supramolecular structure and properties that<br />

differ markedly from those of the aqueous phase<br />

alone, e.g. possibility of conformational changes or<br />

development of an electrical surface field.”<br />

(aqueous) solution<br />

size<br />

location<br />

energy regime<br />

(surface to volume<br />

ratio)<br />

stability<br />

stability (Brownian<br />

motion)<br />

new properties<br />

(surface to volume<br />

ratio)<br />

3


Nanoparticles are applied in many areas: in medicine, in common consumer products like<br />

sunscreens or cosmetics, as catalysts or reductants. Nevertheless, not much is known about<br />

nanoparticles in general. Most research in the past was concentrated on either aerosolic<br />

nanoparticle 1 or on the impact and toxicology of nanoparticles on human health. To do so, it<br />

is important to consider particle attributes like size, shape, structure, composition and<br />

homogeneity (Burleson 2004). As Moore (2006:967) bewails “release of manufactured<br />

nanoparticles into the aquatic environment is largely an unknown”.<br />

That’s why this work will deal with anthropogenic nanoparticles in the hydrosphere, with main<br />

focus not on toxicity but on the particle behaviour and its mobility.<br />

Mobility is an important factor to consider as it shows the affinity of particles to aggregate and<br />

settle down or to stay dispersed in solution. Thus, mobility determines the longevity of<br />

particles, which is a relevant criterion for subsequent toxicology assessment 2 . Natural<br />

organic matter (NOM) plays thereby a key role: “NOM is ubiquitous in natural aquatic<br />

systems and adsorbs on most colloidal particles. Adsorbed NOM (…) can have a significant<br />

effect on colloidal stability and consequently can affect the transport and fate of colloids in<br />

aquatic environments” (Filella 2007:24). NOM is one parameter whose influence on<br />

nanoparticles, namely nanotubes, will be considered in the following discussion in more<br />

detail.<br />

There exist many factors, which influence the behaviour of any particle in an aqueous phase.<br />

Filella (2007: 21ff) focuses on four central properties: particle size, charge, its ability to<br />

coagulate and porosity or the fractal dimension.<br />

First, bigger (aggregated) particles tend to settle down more easily. Thereby, they are<br />

removed from the aquatic system. It is assumed by Filella (2007:22) that the collision<br />

frequency in a nanosystem is substantially higher than for larger particles, thus unexpected<br />

aggregation of nanoparticles and subsequent settlement could diminish their dissolved<br />

aqueous concentration.<br />

Second, surface charge determines the attractive or repulsive interactions of particles. The<br />

charge of a surface can be measured via the zeta potential, which is connected with the<br />

electrophoretic mobility through the Henry equation (Figure 1).<br />

Third, the rate of colloid aggregation is dependent on the frequency and the efficiency of<br />

particle contact. This is associated with the electrostatic repulsion (Figure 1), which can be<br />

described by the Derjaguin, Landau, Verwey and Overbeek theory (DLVO). Assuming that<br />

particle stability depends upon the potential energy function (V T ), this theory takes the<br />

electric double layer repulsion (V R ) and the attractive van der Waals forces (V A ) into account.<br />

Particularly important for these interactions are parameters like zeta potential, particle size,<br />

electrolyte concentration or Hamaker constant (Elimelech et al. 1995). The interaction of<br />

these forces determines the characteristics of the energy curves like for example the<br />

appearance of a secondary minimum.<br />

Finally, particle or aggregation growth changes the density and composition of particles as<br />

fluid is taken into pores. An increase in the cross-section increases the contact between<br />

particles as well as the property of the whole aggregate.<br />

1 “A great deal of research over the last decade has been dedicated to studying the health effects of<br />

airborne ultrafine particles” (Burleson et al 2004:2708).<br />

2 For instance Colvin (2004:1166) argues that it is essential to characterize the expected concentration<br />

of engineered nanoparticles that may be present in the environmental compartment before interpreting<br />

toxicology data.<br />

4


Figure 1: Assumed relationship of some relevant values for aggregation and deposition of colloids.<br />

The Henry equation is defined as: U E =<br />

2 f(k a)<br />

3η<br />

U E = electrophoretic mobility; z = zeta potential; = dielectric constant; = viscosity; f(k a) = Henrys<br />

function (often approximated by 1 (Huckel) or 1.5 (Smoluchowski).<br />

In the following section, the used methods of the three key papers are explained. Afterwards<br />

the main results are shortly listed and summarized as an overview in Table 2. Then, these<br />

findings and observations are discussed in more detail and subsequent some conclusions<br />

are drawn.<br />

2. Reviewed literature and encountered experimental methods<br />

2.a Literature search<br />

This work will be based mainly on three papers, which were found via the Web of Science.<br />

After the first search it was obvious that there are only few papers dealing with nanoparticles<br />

in the hydrosphere. For example the search for “nanoparticle AND hydrosphere” yielded no<br />

results. Thus, a search strategy had to be worked out. Therefore, an excel sheet was<br />

prepared containing four columns: the entered search criterion, a column to be ticked if the<br />

search was restricted to the title, the number of hits and finally the references of potential<br />

interesting articles. This allowed a well-arranged search and reduces the risk to go round in<br />

circles. It turned out that on the one hand, the restriction to “title search” was in general not<br />

leading to results but on the other hand, the search criterion had to be more specific without<br />

this restriction. The combination of terms, like “nanoparticle* AND water AND (aquat* OR<br />

aqueou OR hydrosphere)” resulted in a manageable quantity of hits. After some papers were<br />

found, the references of these papers were also included in the further search.<br />

2.b Experimental methods<br />

All studies were conducted in lab experiments using synthetic and natural water. Hyung et al.<br />

(2007) used Erlenmeyer flasks in which the different MWNT solutions were analysed. The<br />

degree of suspended nanotubes was measured by using Thermal Optical Transmittance<br />

(TOT). This method is adjuvant as organic carbon, derived from NOM, exhibit different<br />

stability properties than the elementary carbon stemming from nanotubes.<br />

5


Lecoanet and Wiesner (2004b) and Brand et al. (2005) used batch systems in their<br />

experiments. Porous media was simulated by silica glass beads, which were filled in a<br />

cylindrical acryl column. The flow behaviour of a solute through a soil column varies,<br />

depending on the interaction of the soil matrix and the solute. Breakthrough curves (BTCs)<br />

provide information on this behaviour, whereas the relative concentration of the solute<br />

measured in the effluent is a function of the pore volume, which is the ratio of effluent volume<br />

to the total pore volume of a column (V/V p ) (Figure 2).<br />

Figure 2: Typical breakthrough curves (Modified after Scott 2000 und Hartge 1978).<br />

The dashed line one (1) represents only a theoretical line, requiring the same flow velocity in the whole<br />

pore system, a conservative 3 behaviour of the dissolved solute and assuming no dispersion. The<br />

effluent concentration remains zero until one pore volume is reached, where the relative concentration<br />

is discharged all at once. This type of flow cannot be observed in natural environments and is referred<br />

to as piston or plug flow (Scott 2000).<br />

Assuming further on a conservative behaviour but including the process of dispersion, results in line<br />

two (2). The solute can be detected in the effluent before one pore volume is discharged but does not<br />

reach the value of one at this point. The result is a S-shaped curve, whose slope decreases with<br />

decreasing velocity or increasing flow distance (Hartge 1978).<br />

If sorption occurs, the curve is retarded as shown by line three (3). When all possible sorption sites are<br />

occupied, the relative concentration reaches one.<br />

This is not the case if the solute is transformed or degraded or is precipitated (line four (4)) (Hartge<br />

1978).<br />

3. Results<br />

This review is based mainly on three papers, whose results are shortly summarized in the<br />

following section (Table 2).<br />

Lecoanet and Wiesner (2004b) compared the transport and deposition properties of two<br />

oxide nanomaterials in a porous media with three aqueous suspensions of fullerene-based<br />

nanomaterials.The porous media was simulated by a cylindrical column filled with spherical<br />

glass beads to which two different flow rates were applied. A theoretical approach for<br />

deposition was established. Colloidal particle are first transported to an immobile surface<br />

where they are attached. This process can be quantitatively described by a constant<br />

3 Conservative means that no sorption and no microbial or chemical transformation occurs (Scott<br />

2000).<br />

6


attachment efficiency factor 4 . Based on observations on particle behaviour in porous media<br />

and under a couple of assumptions, an equation to estimate this attachment efficiency factor<br />

was derived. It was assumed that higher velocity rates lead to a higher passage of<br />

particles.<br />

2d<br />

α = − ln( c / co)<br />

3(1 − ε ) η 0L<br />

α = attachment efficiency factor; d = diameter of a collector which is assumed to be spherical; c/co =<br />

concentration fraction of influent particles remaining; ε = porosity; η 0 = clean bed single-collector<br />

efficiency; L = length of porous media.<br />

Silica nanoparticle (for which retention by the media was marginal) and anatase nanoparticle<br />

complied with the theoretical deposition predictions. This was not the case for fullerenebased<br />

nanoparticle where no velocity dependency was observed and consequently an equal<br />

effluent value for both velocities was reached. For these materials, an affinity transition was<br />

detected during the second pore volume but only at higher Darcy velocity. Fullerol<br />

nanoparticles were only slightly retained by the porous media. To compare the results and to<br />

estimate the hydraulic characteristics of the column all experiments were repeated twice with<br />

a tracer, namely sodium chloride. In a further experiment, the influence of the initial influent<br />

concentration was investigated for fullerol and SWNT by adding once only about 1/3 of the<br />

initial concentration of 10 mg/L. Thereby it was observed that the affinity transition decreased<br />

with lower input concentration.<br />

Brant et al. (2005) investigated the origin of fullerene stability as well as the aggregation and<br />

deposition properties with varying ionic strength in an indifferent electrolyte solution. In pure<br />

water, the three different n-C 60 size fractions used showed only a marginal aggregation<br />

tendency. For the larger n-C 60 nanoparticle (size 168 nm), further investigations with varying<br />

ionic strength were carried out. Already a small addition of salt led to the formation of supraaggregates,<br />

qualified as m-(n-C 60 ), followed by increased settlement of these colloids.<br />

Stronger ionic strength even reinforced this effect. Particles remaining in suspension showed<br />

a narrow size distribution, whereby the average diameter increased with increasing ionic<br />

strength. A different picture arose for the highest investigated strength of 1 M NaCl. The size<br />

distribution was broader and two peaks were observed. By increasing the ionic strength the<br />

zeta potential of fullerenes decreased. Experiments in porous media, simulated by silicate<br />

glass beads packed in a column, point out that with increasing ionic strength, the retention of<br />

n-C 60 increased. Similar to the findings of Lecoanet and Wiesner (2004b), an enhanced<br />

retention affinity during the second pore volume was observed temporally, however<br />

retrogressive for higher ionic strength.<br />

Hyung et al. (2007) investigated the influence of NOM on the stabilization of MNTW in an<br />

aqueous solution. Therefore MWTN was added to three different samples: One sample<br />

contained natural river water with a high content of NOM (Suwannee River), another sample<br />

comprised a synthetic derived NOM solution to model natural NOM (referred to as SR-NOM)<br />

and for the last sample the surfactant sodium dodecyl sulphate (SDS) was applied. The<br />

concentration of suspended MWNT was quantified by using Thermal Optical Transmittance<br />

analysis. Hyung et al. observed a varying degree of MWNT stabilization among the different<br />

samples. The dispersion for samples containing SR-NOM or natural river NOM were similar<br />

but substantially higher compared to SDS. Further, the findings showed that higher amounts<br />

of NOM (natural derived or modelled) resulted in increased suspension of MWNT, which<br />

were present to a large extent in form of single tubes. Association of MWNT to NOM<br />

increased as the relative abundance of NOM increased.<br />

4 “The attachment efficiency is a function of numerous phenomena including van der Waals forces,<br />

electrical double-layer interactions, steric interactions, hydration forces, and particle/surface<br />

hydrophobicity”. (Lecoanet 2004: 5164).<br />

7


Table 2: Overview of the three key papers.<br />

Experimental Results<br />

methods<br />

Author<br />

and<br />

investigated<br />

materials<br />

Lecoanet and<br />

Wiesner<br />

2004b<br />

Silica<br />

Anatase<br />

Fullerene<br />

Fullerol<br />

SWNT<br />

(single-walled<br />

nanotubes)<br />

Brant et al.<br />

2005<br />

Fullerene<br />

Hyung et al.<br />

2007<br />

MWNT<br />

(multi-walled<br />

nanotubes)<br />

Appliance of two<br />

different flow<br />

velocities for a<br />

porous media<br />

simulated by a<br />

silicate glass filled<br />

column.<br />

Appliance of<br />

variable ionic<br />

strength to a<br />

porous media<br />

simulated by a<br />

silicate glass filled<br />

column using<br />

indifferent<br />

electrolyte solution.<br />

Investigation of the<br />

influence of NOM<br />

on nanoparticle<br />

behaviour.<br />

Use of three<br />

different samples:<br />

1) unaltered river<br />

water with a natural<br />

NOM content<br />

2) SDS solution<br />

3) modelled NOM<br />

(SR-NOM)<br />

• Oxide nanoparticles followed<br />

deposition theory but not so<br />

fullerene based materials.<br />

• C 60 particles showed a transitional<br />

enhancement in retention affinity<br />

during the second pore volume<br />

and deposition converged to a<br />

flow velocity independent level.<br />

• Increasing ionic strength reduced<br />

the zeta potential and induced the<br />

formation of supra-aggregates<br />

(m-(n-C 60 )), which resulted in<br />

enhanced settlement.<br />

• For ionic strength below 1 mg/l<br />

NaCl, suspended colloids showed<br />

are narrow size distribution.<br />

Above another behaviour was<br />

observed.<br />

• In the porous media a temporary<br />

increased deposition affinity was<br />

observed during the second pore<br />

volume.<br />

• River derived NOM and SR-NOM<br />

are better stabilization agent as<br />

SDS.<br />

• Suspension of MWNT as single<br />

tubes<br />

• Suspension of MWNT and<br />

association of NOM to MWNT<br />

increased with increasing NOM.<br />

Open questions and<br />

problems<br />

Discussion of several<br />

explanations for the<br />

deviant behaviour of<br />

fullerene-based material<br />

(e.g. transitional<br />

enhancement in affinity<br />

for the media).<br />

Uncertainty of the origin<br />

of colloidal charge.<br />

NOM is highly variable.<br />

Further research should<br />

take these differences of<br />

NOM composition into<br />

account.<br />

4. Discussion<br />

In the following section, some breakthrough curves of diverse nanoparticles determined by<br />

Lecoanet and Wiesner (2004b) and Brant et al. (2005) are analysed and compared to those<br />

of Figure 2.<br />

Silica<br />

The breakthrough curves of silica at both Darcy velocities were nearly similar to those of the<br />

tracer sodium chloride, meaning a marginal retention by the porous media. Already after two<br />

pore volumes, the relative concentration reached nearly 0.9 (Figure 3). Compared to Figure<br />

2, one should expect a steeper slope for the higher velocity, but this velocity effect was<br />

negligible as total removal was humble.<br />

Size is an important factor for the behaviour of any particle. Larger silica particles (135 nm)<br />

showed less mobility in experiments by Lecoanet et al. (2004:5167 Figure 4) and the effluent<br />

concentration reached after two pore volumes was about the half compared to the smaller<br />

silica particles (57nm). This result is consistent with DLVO theory because “interaction<br />

8


energies are directly proportional to particle size” (Elimelech et al. 1995:61 5 ). Thereby greater<br />

size implies stronger secondary energy effects, which favour aggregation. Additionally it can<br />

be also observed in Table 3 that the distance to reduce the relative concentration C/C in of the<br />

smaller silica particle to 0.1% was about 10 times longer than for the bigger silica particle.<br />

Thus, smaller particles have higher mobility.<br />

Figure 3: Breakthrough curve of silica at two Darcy velocities: “Slow” corresponds to a flow velocity of<br />

0.04cm/s, “Fast” to 0.14cm/s (Lecoanet and Wiesner 2004b).<br />

Anatase<br />

As expected, the slope was steeper for the higher Darcy velocity. The striking observation for<br />

these curves is that neither for the high nor for the low velocity, C/C in reached the value one<br />

during five pore volumes. Anatase has a low water solubility (Milnes and Twidall 1983) and<br />

thus a great affinity to the porous media. The small value of electrophoretic mobility (Table<br />

3), which implies less repulsion and a smaller energy barrier for attachment (Lecoanet and<br />

Wiesner 2004b), intensifies this affinity to the column material.<br />

Calculations were made to get an idea of the fraction of occupied porous volume V p through<br />

anatase (Figure 4b). After five pore volumes, less than 0.0014% of the total porous volume<br />

was engaged by the volume of anatase particles. Thus, it can be assumed that extending the<br />

experiment to substantial higher pore volumes, could lead to the same effluent and influent<br />

concentration (C/C in =1). This marginal increase of the C/C in ratio appears on Figure 4a as a<br />

“plateau” because only few pore volumes were discharged.<br />

Anatase:<br />

Data:<br />

V = 100 ml (selected input)<br />

V p = 0.02 l (Lecoanet and Wiesner 2004)<br />

C in = 10 mg/l (Lecoanet and Wiesner 2004)<br />

= 3.8 g/cm 3 (Table 3)<br />

V occ = ? (with anatase occupied volume)<br />

C in V = 1 mg<br />

V occ = m / = 2.63*10 -7 l → 0.0013%<br />

After 5 pore volumes, about 0.0013% of<br />

the porous volume is occupied by<br />

anatase.<br />

Figure 4a: Left: Breakthrough curve of anatase at two Darcy velocities: “Slow” corresponds to a flow<br />

velocity of 0.04 cm/s, “Fast” to 0.14 cm/s (Lecoanet and Wiesner 2004b).<br />

Figure 4b: Right: Calculation of occupied porous volume for anatase after 5 pore volumes.<br />

5 Although Elimelech referred this statement to particle being greater than about 1µm in diameter.<br />

9


Table 3: Some characteristics of the considered nanoparticles (Lecoanet et al. 2004a; Lecoanet and<br />

Wiesner 2004b)<br />

particles<br />

size (nm)<br />

density<br />

(g/cm 3 )<br />

electrophoretic<br />

mobility<br />

10 -8 (m 2 s -1 V -1 ) pH zpc log <br />

distance to<br />

reduce C/ C in<br />

to 0.1% (m) b<br />

fullerol 1.2 1.69 not detectable 2.3 -3.98 14<br />

SWNT<br />

0.7-1.1 c * 80-200<br />

( dh = 21 nm d ) 1 -3.98 2.2 -2.89 10<br />

silica 57 2.65 -1.95 2 -2.1 2.4<br />

silica 135 -2.58 -0.77 0.2<br />

n-C 60 168 1.41 -1.99 2.3 -0.52 0.1<br />

anatase 198 3.8 -0.27 6.1 -0.47 0.1<br />

b Conditions assumed for calculations: T) 15 °C, H) 10-20 J, Darcy velocity = 0.003 cm/s, porosity = 0.30, mean<br />

sand grain diameter = 350 µm.<br />

c According to the model cross-section of an individual fullerene nanotube encased in a close-packed cylindrical<br />

surfactant micelle, the outer diameter of this nanomaterial is close to 4 nm with a specific gravity of approximately<br />

1.0.<br />

d Average hydrodynamic diameter.<br />

Fullerene-based materials<br />

Fullerenes are extremely hydrophobic, thus prone to interact with the porous media and<br />

unlikely to be dispersed in the aqueous phase. The plateau value of C/Cin = 1 was not<br />

reached during five pore volumes. This observation can be explained in a similar way as for<br />

anatase above. The influence of hydrophilicity on the mobility in the aqueous phase can be<br />

seen well in Figure 5. The comparison of the distance to reduce the relative concentration to<br />

0.1% was substantially higher for fullerols (14 m) than for fullerenes (0.1 m), yielding a factor<br />

of 140 of increased mobility for the more hydrophilic fullerols.<br />

Three striking differences from Figure 2 can be observed for all three fullerene-based<br />

materials: First, during the first and second pore volume a transitionally increased affinity to<br />

the porous media was discovered. Second, a similar plateau value was observed for both<br />

velocities. Third, the effluent concentration at high Darcy velocity was (nearly) all the time<br />

lower than those at lower Darcy velocity.<br />

Lecoanet and Wiesner (2004b) explained this latter observation by the special structural<br />

alignment of SWNTs, comparable to a “rope”. This implies an ideal velocity, for which the<br />

arrangement can be formed optimally. According to this, above und below this “ideal”<br />

velocity, alignment of nanotubes should be retarded. A similar process is conceivable for<br />

fullerene. Transmission electron microscopy suggests that C 60 growths through the formation<br />

of crystalline structures (Chen 2006, Brant et al. 2005). This “crystalline growth” could also<br />

imply an optimal flow velocity for proper alignment. According to this, the “Fast” velocity<br />

(Figure 5) was more close to this assumed “ideal” velocity.<br />

Lecoanet and Wiesner (2004b) discuss three explanations why a similar plateau for both<br />

velocities was reached: First, they assumed that the size of aggregates changed with<br />

velocity. This assumption contradicted with measurements and was rejected. Second, they<br />

supposed that the attachment efficiency factor increased with velocity in order to get the<br />

same effluent concentration. Thereby the fluid flow should transfer forces to the particle to<br />

overcome an assumed attachment barrier. As possible forces are rather small, this seems to<br />

be unlikely. Finally, Lecoanet and Wiesner (2004b) proposed that deposition was not mass<br />

10


transport limited, however another step limited the attachment rate. They assumed the highly<br />

ordered growth of nanotubes and fullerenes to be limiting. This explanation would<br />

correspond to the above mentioned “crystalline growth” of fullerene and “rope” like alignment<br />

of nanotubes. To reason from these findings, the structural growth of nanoparticles seems to<br />

be essentially important.<br />

The dip during the second pore volume could not be explained satisfactorily. As this effect<br />

occurred not before the discharge of one pore volume, it can be suggested that the<br />

nanoparticles itself alter the collector surface in a way that further attachment is favoured.<br />

Consideration of the forces between the media and fullerene and fullerene to fullerene<br />

support this assumption. The Hamaker 6 constant between the nanoparticles itself was<br />

calculated to be 10 times higher than the Hamaker constant of fullerene-silica-water 7 . The<br />

degree of nanoparticle coverage of the collector was calculated by Lecoanet and Wiesner<br />

(2004b) after the discharge of one pore volume. The result was just about 1% modified<br />

surface, which was not sufficient to explain the drop in the curves. Additionally, it does not<br />

explain why the phenomenon was not observed at lower Darcy velocity. Perhaps this<br />

phenomenon was also a consequence of the “ordered alignment” or specific growth<br />

behaviour of these nanoparticles. However, this was neither further investigated nor<br />

discussed in the paper by Lecoanet and Wiesner (2004b).<br />

Figure 5: Breakthrough curve of fullerene (left) and fullerol (right) at two Darcy velocities: “Slow”<br />

corresponds to a flow velocity of 0.04cm/s, “Fast” to 0.14cm/s (Lecoanet and Wiesner 2004b).<br />

Brant et al. (2005) made similar column experiments using two ionic strengths (0.001 M and<br />

0.1 M) 8 (Figure 6). The breakthrough curve of lower NaCl concentration was at all times<br />

above the curve of higher ionic strength, meaning that for the former less deposition<br />

occurred. This detection is conformable with DLVO theory. As shown in the inset of Figure 6,<br />

greater ionic strength intensifies the appearance of a stronger secondary minimum. A strong<br />

(secondary) minimum is favourable for aggregation. This can be explained by the balance of<br />

power of involved forces: Higher ionic strength reduces electrical repulsion (meaning lower<br />

energy barrier), thus fosters the convergence of particles which favours the attractive Van<br />

der Waals forces to dominate (Elimelech et al. 1995) (Figure 1). It can also be seen in Figure<br />

6 that the transitional affinity was reduced by applying a higher NaCl concentration. To<br />

conclude from these observations, electrostatic repulsion could be limiting for low ionic<br />

strength conditions, where the retention is transitionally increased (Brant et al. 2005).<br />

6 “The Hamaker constant characterizes the resonance interactions between electronic orbitals in two<br />

particles and the intervening medium” (http://www.erpt.org).<br />

7 Hamaker constants: fullerene-silica-water = 2.76*10 -20 J; fullerene-fullerene = = 2.35*10 -19 J<br />

(Lecoanet and Wiesner 2004: 4380).<br />

8 Lecoanet and Wiesner (2004) applied in their experiments an ionic strength of 0.01 M.<br />

11


Figure 6: Breakthrough curve of C 60 for two different NaCl concentration (0.001M and 0.1M),<br />

applied Darcy velocity probably 0.14 cm/s 9 . The inset on the left shows the DLVO interaction energy<br />

pro<strong>file</strong>s between n- C 60 cluster and the spherical glass collector for three different ionic strength<br />

(IS) = 01, 0.01, 0.001 M. The interaction energy is plotted versus the surface-to-surface separation<br />

distance h in nm. (Modified after Brant et al. 2005).<br />

Chen and Elimelech (2006) showed that divalent CaCl 2 (Ca 2+ ) electrolyte solutions were<br />

even more effective in reducing the energy barrier between particles than monovalent<br />

solutions (Na + ). Thus the electric repulsion or electrophoretic mobility decreased to a higher<br />

extent by using Ca 2+ electrolyte concentration and aggregation was reinforced (Figure 1).<br />

In further experiments, Lecoanet and Wiesner (2004b) investigated the influence of the initial<br />

concentration at the higher Darcy velocity (0.14 cm/s) for fullerol and SWNTs. Thereby the<br />

affinity transition to the collector surface decreased at lower concentration (3.5 mg/l instead<br />

of 10 mg/l) (Figure 7). This observation supported the presumption that initial nanoparticle<br />

deposition favoured subsequent attachment and was responsible for the drop in the effluent<br />

concentration. According to this, lowering the initial concentration would reduce these special<br />

aligned growing sites and consequently reduce the affinity transition.<br />

Figure 7: Breakthrough curve of fullerol at high Darcy velocity, meaning 14 cm/s, for two different<br />

initial concentrations (Lecoanet and Wiesner 2004b).<br />

9 It was not clear which Darcy velocity was finally applied. Brant et al. (2005) specified on page 547 an<br />

applied Darcy velocity of 0.04 cm/s whereas in the caption of the figure 7 on page 550 a Darcy velocity<br />

of 0.14 cm/s was mentioned. These velocities correspond to “Slow” and “Fast” in the figures of<br />

Lecoanet and Wiesner (2004b). The authors replied not yet to the made inquiry.<br />

12


It can be concluded from these findings that aggregation and subsequent deposition could<br />

limit the mobility and hence the risk emanating from nanoparticles. It was stated by Brant et<br />

al. (2005:545) that through the formation of large aggregates the “risk presented by n-C 60<br />

toxicity due to a reduced potential for exposure” is (partially) offset. This conclusion was<br />

relativised further on by referring to natural environments because they contain compounds<br />

with the capability to mobilize other compounds. One important class of these substances is<br />

natural organic matter (NOM) as it plays a key role in natural environments. It is abundant,<br />

influences surface properties and the stability of particles, affects transport and the fate of<br />

colloids. Thus, it is important to investigate as well the effect of NOM on nanoparticles in the<br />

aqueous phase. As nanoparticles are a heterogenic and broad class of substances, the<br />

influence is exemplarily discussed for nanotubes by referring mostly to the paper of Hyung et<br />

al. (2007), who studied the impact of NOM on multiple walled carbon nanotubes (MWNT).<br />

The influence of natural organic matter<br />

Nanotubes are expected to aggregate to a large extent as they are highly hydrophobic and<br />

form strong Van der Waals forces due to the fact that their axial length can exceed the<br />

micrometer range (Hyung et al. 2007).<br />

Hyung et al. (2007:182f) observed two striking effects of MWNT suspension and association:<br />

First, suspended MWNT increased either by increasing the NOM content or by increasing the<br />

addition of MWNT itself, while conserving the initial NOM content.<br />

Second, MWNT association to NOM increased either by increasing the dose of NOM or<br />

decreasing the initial concentration of MWNT. This means that association between NOM<br />

and MWNT was superior if the relative abundance of NOM was increased.<br />

What are possible reasons, which explain that NOM enhanced MWNT suspension?<br />

Filella (2007:25ff) suggests that adsorption to NOM, bearing a high content of acidic groups,<br />

can produce negative surface charge to the colloids. Electrostatic repulsion and formation of<br />

repulsive double-layer forces by this charge may stabilize particles in natural waters.<br />

Additionally, some NOM have a bulky form and high molecular mass. Hence, stability of<br />

adsorpt nanoparticles may be enhanced through steric repulsion. Hyung et al. (2007:182f)<br />

concluded that for the formation of MWNT-NOM suspension, two aspects have to be<br />

considered: First “the physical dispersion of MWNT added to solution” and second the<br />

association or “dynamic equilibrium processes, similar to adsorbate-adsorbend interactions”<br />

of NOM to MWNTs “rendering them stable in aqueous phase”. In his study, Hyung et al.<br />

(2007) compared the adsorption efficiency of SDS, a surfactant, with modelled and natural<br />

organic matter. The data suggests that SDS is less effective in formation of dispersed<br />

nanotubes than both other (natural and model) forms of NOM. Accordingly, divers properties<br />

of the surfactant and NOM must provoke this difference in stabilization capability. SDS is an<br />

aliphatic substance whereas NOM contains aromatic groups. The – electrons<br />

interactions of these aromatic parts and MWNT could lead to a stabilization effect (Hyung et<br />

al. 2007). Nanotubes are stabilized intramolecularly by having delocalized -electrons over<br />

the whole molecule. These -electrons can interact weakly with aromatic parts of NOM. The<br />

sum of many such weak polarization interactions could lead to considerably stabilized<br />

aggregates of NOM and nanotubes. Futher, NOM could shield the hydrophobic nanotubes<br />

from contact with water by directing outwards to the aqueous phase their polar tails.<br />

“However, the exact mechanism for CNT interaction with NOM will depend on both NOM<br />

characteristics including aromaticity, charge density, and size as well as CNT characteristics<br />

such as aspect ratio (e.g., SWNT) and functional derivatization (…)” (Hyung et al. 2007:183).<br />

Thus, a variety of parameters determine the degree of NOM and nanoparticle interaction and<br />

the extent of CNT suspension in a complex manner. In this context, it must be stated that<br />

NOM does not equal NOM: depending on the environmental compartment and the origin of<br />

NOM, the characteristics (e.g. size, molecular mass, electric charge) and abundance of NOM<br />

vary widely.The composition of NOM for example is important as fulvic compounds tend to<br />

stabilize colloids whereas rigid biopolymers have the opposite effect (Buffle et al.<br />

1998:2887). To take all these into account and to characterize more precisely NOM will be<br />

13


ather challenging and a way of doing so in a feasible manner will be the task for further<br />

investigations.<br />

Nevertheless, NOM seems to stabilize nanotubes in the aqueous phase. Thus, aggregation<br />

and adjacent settlement of nanotubes in the present of NOM will be reduced and the<br />

longevity of these nanoparticles increased. Hyung et al. (2007:179) concludes that “dispersal<br />

of carbon-based nanomaterials in the natural aqueous environment might occur to an<br />

unexpected extent following a mechanism that has not been previously considered in<br />

environmental fate and transport studies”.<br />

5. Conclusions<br />

Nanoparticles are produced through many anthropogenic or natural processes, for example<br />

through vulcano explosions or industrial combustion processes. Released to the<br />

environment, nanoparticles can be transported via the atmosphere, settle down on soils or<br />

enter the hydrosphere. In the aquatic environment, the propensity to aggregate is one<br />

important characteristic of nanoparticles. Aggregation leads to increased particle size which<br />

enhances the tendency of settlement and thus the degree of particle removal from the<br />

aquatic phase. Other important parameters are shape, hydrophilicity, charge, the<br />

composition of nanoparticles or the environmental conditions like ionic strength, the presence<br />

of potential collector surfaces and the pH conditions. All these parameters are linked in a<br />

complex manner and determine the form and amount of present nanoparticles. These<br />

parameters influence also the bioavailability and toxicity of nanoparticles. For example it can<br />

be assumed that smaller particles are taken in unintentionally to a greater extent than<br />

particles of bigger size. For environmental risk assessment one should consider both: the<br />

amount produced and released to the environment and the potential threat (e.g. longevity) or<br />

toxicitiy emanating from the different class of nanoparticles.<br />

As it was shown by experiments of Lecoanet and Wiesner (2004), the breakthrough curves<br />

of fullerene-based nanoparticles varied compared to silica and anatase breakthrough curves.<br />

The observation of the enhanced affinity of these molecules to the porous media could be an<br />

indication that the structural dimension or the proper alignement of the fullerene-based<br />

nanoparticles could be an important factor for deposition behaviour. Another relevant<br />

property is hydrophilicity as can be deduced from the experimental findings of Lecoanet and<br />

Wiesner (2004). Hydrophobic fullerenes were considerably more prone to deposition and<br />

about 140 times less mobile than their more hydrophilic counterparts, the fullerols (Figure 5,<br />

Table 3). A further important parameter is the ionic strength. It was shown by Brant et al.<br />

(2005) that increased ionic strength reduces the surface charge and thereby reduces the<br />

barrier for attachment. Chen and Elimelech (2006) observed that the divalent solution of<br />

CaCl 2 (Ca 2+ ) was much more efficient in reducing this energy barrier between particles than<br />

the monovalent solution of NaCl (Na + ) . Regarding the environment, this is important as Ca 2+<br />

is present in some aqueous environment in such a concentration that it could exert an<br />

influence of the aggregation behaviour of present nanoparticles 10 . Calcium rich aqueatic<br />

environment are, according to this, less threatened by nanoparticles as aggregation and<br />

subsequent settlement could reduce their longevity. It should be mentioned that settlement<br />

does not eliminate all risks of nanoparticles. Change in environmental conditions could<br />

resuspend settled nanoparticles or organisms living or feeding on sediments could be<br />

threatened as well. Natural organic matter, which is (nearly) omnipresent in the environment,<br />

is reported to stabilize dispersed nanotubes (Hyung et al. 2007). Hence eutrophic aquatic<br />

environments are more endangered by potential risks emanating from nanotubes than less<br />

active and NOM poor ones. The enhanced degradation of organic matter in an eutrophic lake<br />

e.g. could lead to a release of the stabilized NOM-nanotubes assemblies and accelerates<br />

settlement. In this context, it is important to consider that NOM is also highly variable<br />

10 The calcium concentration of Lake Zürich was reported to be about [Ca 2+ ] = 1.2*10 -3 mol/l (Filella<br />

2007:28).<br />

14


(different NOM origin, composition, functional groups etc.). To make more reliable<br />

predictions, the influence of the different NOM constituents should be considered separatly.<br />

Further, NOM is only one constituent in the environment and does not allow to draw<br />

conclusions to the influence of other organic compounds such as nitrilotriacetatate (NTA) on<br />

nanoparticles. Also other potential collector surfaces like minerals are not considered in this<br />

work.<br />

It should be emphasised that nanoparticles are a broad substance class with many different<br />

characteristics and properties as it could be seen by consideration of the varying deposition<br />

behaviour in the porous media. Thus it cannot be assumed that NOM stabilizes other<br />

nanoparticles to the same extent or the same manner than it does for carbon nanotubes. For<br />

this reason no conclusions can be drawn form the behaviour of one nanoparticle class to<br />

another and environmental impacts should be addressed rather on a case-by-case basis<br />

(Lecoanet et al. 2004a:5168). Further, for all these experiments, it should be beared in mind<br />

that they are lab experiments. Natural behaviour may be different to the observed behaviour.<br />

Filella (2007:25) stated that for example the DLVO theory may not be applicable as natural<br />

systems are too heterogeneous. Particle size and distribution, pore distribution and rough<br />

matrix surfaces are some examples which lead to discrepancies to theoretical behaviour and<br />

restrict the application of this theory. Additionally, the spatial heterogeneity may make the<br />

measurement of the average surface charge (expressed by the zeta potential) useless for<br />

mobility consideration (Filella 2007:24). In nature, conditions may change very rapidly. For<br />

example a rainfall event could abruptly alter the water composition and influence the<br />

deposition or aggregation behaviour of nanoparticles (Chen 2006). It should be also kept in<br />

mind that columns containing silica beads are just an attempt to represent mineral surfaces<br />

in groundwater. Probably this approach is sufficient for most of the groundwater systems but<br />

digressive soil composition, like high content of clays, could lead to totally different<br />

breakthrough curves. The transfer of lab observations to the “real“ natural environment is<br />

often restricted as the environment is exposed to complex interactions of numerous<br />

influencing factors.<br />

6. References<br />

Brant, J., H., Lecoanet, and M.R. Wiesner. 2005. Aggregation and deposition characteristics of<br />

fullerene nanoparticles in aqueous systems. Journal of Nanoparticle Research. 7:545-553.<br />

Burleson, D.J., M.D. Driessen, and R.L.Penn. 2004. On the characterization of environmental<br />

nanoparticles. Journal of <strong>Environmental</strong> Science and Health. 39(10):2707-2753.<br />

Chen, K.L., M. Elimelech. 2006. Aggregation and deposition kinetics of fullerene (C 60 ) nanoparticles.<br />

Langmuir. 22:10994-11001.<br />

Derjaguin, B.V. 1989. Theory of Stability of Colloids and Thin Films. Consultants Bureau, New York<br />

and London, 91-98 p.<br />

Elimelech, M., J. Gregory, X. Jia, and R.A.Williams. 1995. Particle Deposition and<br />

Aggregation : Measurement, Modelling and Simulation. Oxford, Butterworth-Heinemann, 33-67 p.<br />

Filella, M. 2007. Colloidal properties of submicron particles in natural waters. Chapter 2:17-93. In: K.J.<br />

Wilkinson, and J.R. Lead (eds.), <strong>Environmental</strong> Colloids and Particles: Behaviour, Separation and<br />

Characterisation. John Wiley & Sons, Ltd., Chichester.<br />

Hartge, K.H. 1978. Einführung in die Bodenphysik. Ferdinand Enke Verlag, Stuttgart, 335-340 p.<br />

Hyung, H., J.D. Fortner, J.B. Hughes, and J. Kim. 2007. Natural organic matter stabilizes carbon<br />

nanotubes in the aqueous phase. <strong>Environmental</strong> Science and Technology. 41:179-184.<br />

Lead, J.R. and K.J. Wilkinson. 2006. Aquatic colloids and nanoparticles: Current knowledge and future<br />

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Lead, J.R. and K.J. Wilkinson. 2007. <strong>Environmental</strong> Colloids and Particles: Current Knowledge and<br />

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Colloids and Particles: Behaviour, Separation and Characterisation. John Wiley & Sons, Ltd.,<br />

Chichester.<br />

Lecoanet, H.F., J. Bottero, and M.R. Wiesner. 2004a. Laboratory assessment of the mobility of<br />

nanomaterials in porous media. <strong>Environmental</strong> Science and Technology. 38:5164-5169.<br />

Lecoanet, H.F. and M.R. Wiesner. 2004b. Velocity effects on fullerene and oxide nanoparticle<br />

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Leppard, G. 1992. Evaluation of electron microsope techniques for the description of aquatic colloids.<br />

Chapter 6: 231-289. In: J. Buffle and H.P. van Leeuwen (eds.), <strong>Environmental</strong> Particles. Volume 1,<br />

International Union of Pure and Applied Chemistry, Lewis Publishers.<br />

Milnes, A.R. and C.R. Twidale. 1983. An overview of silicification in Cainozoic landscapes of arid<br />

central and southern Australia. Australian Journal of Soil Resources. 21:405.<br />

Moore, M.N. 2006. Do nanoparticles present ecotoxicological risks for the health of the aquatic<br />

environment? Environment International. 32:967-976.<br />

Scott, H.D. 2000. Soil <strong>Physics</strong> Agricultural and <strong>Environmental</strong> Applications. Iowa State University<br />

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Technology Assessment (TA Swiss). 2006. Nanotechnologien und ihre Bedeutung für Gesundheit und<br />

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Zhang, W. 2003. Nanoscale iron particles for environmental remediation: An overview. Journal of<br />

Nanoparticle Research. 5:323-332.<br />

Divers:<br />

British Standards Institution (BSI). 2005. Vocabulary-Nanoparticles. Public Available Specivication<br />

(PSA):71, London.<br />

http://www.bsi-global.com [11. June 2007].<br />

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Emails correspondance: Conradt, S. (2007) email send to Wiesner, M.R. by 16 th June. No answer till<br />

22th June.<br />

Feynman, R. 1959. There’s Plenty of Room at the Bottom.<br />

http://www.zyvex.com<br />

http://www.zyvex.com/nanotech/feynman.html [29. May 2007].<br />

International Union of Pure and Applied Chemistry (I<strong>UP</strong>AC). http://www.iupac.org/dhtml_home.html<br />

[29 May 2007].f<br />

Nelson, R.D. 2002. Dispersions powders in liquids. Educational Researches for Particle Technology.<br />

http://www.erpt.org<br />

http://www.erpt.org/024Q/nelsb-08.htm [14. June 2007].<br />

Südwestradio 2 (SWR) Aula. 13. May 2007. Podcast. Klein aber effizient.<br />

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