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Global Dialogue on Nanotechnology and the Poor ... - Nanowerk

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nanotechnology,<br />

water, & development<br />

‘‘<br />

Pressure-driven membrane technology is an ideal method for <strong>the</strong><br />

treatment of water to any desired quality.The integral part of <strong>the</strong><br />

technology is <strong>the</strong> membrane.The membrane is a barrier that<br />

separates two homogenous phases. It allows some solutes to pass<br />

through but rejects <strong>the</strong> permeati<strong>on</strong> of o<strong>the</strong>rs. It achieves <strong>the</strong><br />

separati<strong>on</strong> of solutes of a fluid mixture when a driving force is<br />

applied.The force could be a pressure difference (∆p),<br />

c<strong>on</strong>centrati<strong>on</strong> gradient (∆c), temperature difference (∆T), or<br />

electrical potential difference (∆E).The basic principle of operati<strong>on</strong><br />

is illustrated in Figure 3. Phases 1 <strong>and</strong> 2 are generally <strong>the</strong> feed water<br />

<strong>and</strong> <strong>the</strong> product water or permeate, respectively.The basis of<br />

separati<strong>on</strong> is that each membrane has unique characteristics<br />

for <strong>the</strong> selective permeati<strong>on</strong> <strong>and</strong> rejecti<strong>on</strong> of different solutes. 48<br />

Figure 3: Schematic Representati<strong>on</strong> of a Two-Phase System<br />

Separated by a Membrane<br />

Nanofiltrati<strong>on</strong> membrane<br />

technology is widely applied for<br />

removal of dissolved salts from<br />

salty water, removal of micro<br />

pollutants, water softening, <strong>and</strong><br />

’’<br />

wastewater treatment.<br />

Nanofiltrati<strong>on</strong> (NF) membrane technology is widely applied for<br />

removal of dissolved salts (i.e., desalinati<strong>on</strong>) from salty (i.e., brackish)<br />

water, removal of micro pollutants (e.g., arsenic <strong>and</strong> cadmium),<br />

water softening (i.e., removal of calcium <strong>and</strong> magnesium i<strong>on</strong>s),<br />

<strong>and</strong> wastewater treatment. RO membranes are also used for <strong>the</strong><br />

desalinati<strong>on</strong> of brackish water, ocean, <strong>and</strong> seawater. RO <strong>and</strong> NF<br />

water treatment plants typically c<strong>on</strong>sist of two types of treatment<br />

stages in series.These are <strong>the</strong> pre-treatment <strong>and</strong> membrane systems.<br />

The pre-treatment system removes particulate matter, in particular,<br />

suspended solids.The membrane removes some soluble substances<br />

<strong>and</strong> minute substances that were not rejected by <strong>the</strong> pre-treatment<br />

system. RO treatment plants reject all soluble <strong>and</strong> minutely insoluble<br />

substances but water.<br />

Source: Mulder, 1997. 49<br />

‘‘<br />

There are four pressure-driven membrane processes.These are<br />

microfiltrati<strong>on</strong> (MF), ultrafiltrati<strong>on</strong> (UF), nanofiltrati<strong>on</strong> (NF), <strong>and</strong><br />

reverse osmosis (RO).These processes may be distinguished by pore<br />

size, transport mechanism, applied pressure, <strong>and</strong> range of<br />

applicati<strong>on</strong>s.The pore sizes for MF, UF, NF, <strong>and</strong> RO are respectively<br />

0.05 10 µm, 1 – 100 nm, < 2 nm, <strong>and</strong> < 2 nm.The pore sizes<br />

decrease from MF to RO membranes.The pore sizes corresp<strong>on</strong>d to<br />

<strong>the</strong> size of molecules that are retained by <strong>the</strong> membrane. NF <strong>and</strong><br />

RO membranes are <strong>the</strong> most widely used membrane processes in<br />

water treatment. MF <strong>and</strong> UF membranes are generally used in pretreatment.The<br />

main advantages of <strong>the</strong> membrane process for water<br />

treatment is that it does not require chemicals, requires relatively<br />

low energy, <strong>and</strong> is easy to operate <strong>and</strong> maintain. 50<br />

Nanofiltrati<strong>on</strong> membranes…<br />

selectively reject substances…<br />

[which] enables <strong>the</strong> retenti<strong>on</strong> of<br />

nutrients present in water that are<br />

required for <strong>the</strong> normal functi<strong>on</strong>ing<br />

’’<br />

of <strong>the</strong> body.<br />

NF membranes, <strong>on</strong> <strong>the</strong> c<strong>on</strong>trary, selectively reject substances.The<br />

characteristic selectivity of NF has advantages in comparis<strong>on</strong> to RO<br />

because it enables <strong>the</strong> retenti<strong>on</strong> of nutrients present in water that<br />

are required for <strong>the</strong> normal functi<strong>on</strong>ing of <strong>the</strong> body. For example,<br />

calcium i<strong>on</strong>s are necessary for <strong>the</strong> healthy development of b<strong>on</strong>es. 51<br />

49<br />

B. Nicolaisen,“Developments in Membrane Technology for Water Treatment,” Desalinati<strong>on</strong>,Vol. 153, 2003, pp. 1 – 3, 355 – 360; <strong>and</strong> M. Mulder, Basic Principles of Membrane<br />

Technology, 2nd ed., Kluwer Academic Publishers, Dordrecht, 1997.<br />

49<br />

Mulder, op. cit.<br />

50<br />

Mulder, op. cit.; <strong>and</strong> J. L. Moitsheki,“Evaluati<strong>on</strong> of <strong>the</strong> Performance of Nanofiltrati<strong>on</strong> Membranes in Detrimental I<strong>on</strong> Rejecti<strong>on</strong> <strong>and</strong> To M<strong>on</strong>itor Fouling <strong>and</strong> Membranes with Their<br />

Subsequent Chemical Cleaning,” master’s <strong>the</strong>sis, Potchefstroom University, Potchefstroom, South Africa, 2003; <strong>and</strong> A. S<strong>on</strong>une <strong>and</strong> R. Ghate, “Developments in Wastewater Treatment<br />

Methods,” Desalinati<strong>on</strong>,Vol. 167, 2004, pp. 55 – 63.<br />

51<br />

Filtrati<strong>on</strong> Industry Analyst, op. cit.; <strong>and</strong> Mulder, op. cit.; <strong>and</strong> Moitsheki, op. cit.<br />

20

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