25.12.2014 Views

Abstract Booklet 2006 - Swanson School of Engineering - University ...

Abstract Booklet 2006 - Swanson School of Engineering - University ...

Abstract Booklet 2006 - Swanson School of Engineering - University ...

SHOW MORE
SHOW LESS

You also want an ePaper? Increase the reach of your titles

YUMPU automatically turns print PDFs into web optimized ePapers that Google loves.

5-5<br />

Enhanced Hydrogen Production with in-situ CO 2 Capture<br />

in a Single Stage Reactor<br />

Liang-Shih Fan, Mahesh Iyer, Shwetha Ramkumar, Danny Wong, The Ohio State<br />

<strong>University</strong>, USA<br />

Enhancement in the production <strong>of</strong> high purity hydrogen from fuel gas, obtained from coal<br />

gasification, is limited by thermodynamics <strong>of</strong> the Water Gas Shift Reaction which is used to<br />

shift the carbon monoxide towards hydrogen. However, this constraint can be overcome by<br />

concurrent water-gas shift (WGS) and carbonation reactions to enhance H 2 production by<br />

incessantly driving the equilibrium-limited WGS reaction forward and removing the CO 2<br />

product from the fuel gas mixture in-situ. This not only improves the H 2 yield but also<br />

augments the purity <strong>of</strong> the product by removing the CO 2 co-product and achieving near<br />

complete conversion <strong>of</strong> the CO reactant. This process developed at the Ohio State <strong>University</strong><br />

can effectively and economically produce a pure H 2 stream, at high temperature and<br />

pressure, via coal gasification while integrating capture <strong>of</strong> CO 2 emissions, for its subsequent<br />

sequestration. The enhanced water gas shift reaction for H 2 production with insitu<br />

carbonation was studied using the commercial High Temperature Shift (Iron Oxide) catalyst<br />

and calcium sorbents in an integral fixed bed reactor setup. We have identified a high<br />

reactivity patented, mesoporous calcium oxide sorbent for the in-situ CO 2 capture. The<br />

morphological properties <strong>of</strong> our patented precipitated calcium carbonate sorbent (PCC) can<br />

be tailored using surface modifiers to demonstrate a high CO 2 capture capacity <strong>of</strong> about 70%<br />

by weight (~700g <strong>of</strong> CO 2 /kg sorbent ) at elevated temperatures (600-700°C). Experimental<br />

evidence clearly shows that this proprietary calcium sorbent (PCC) performance dominates<br />

over that <strong>of</strong> commercial limestone sorbents at any given time. Thus, product gas<br />

composition analyses demonstrate complete carbon monoxide conversion as well as CO 2<br />

removal during the initial part <strong>of</strong> the breakthrough curve, thus demonstrating the synthesis <strong>of</strong><br />

pure hydrogen.<br />

6-1<br />

SESSION 6<br />

GLOBAL CLIMATE CHANGE:<br />

GEOLOGIC CARBON SEQUESTRATION – 1<br />

Effects <strong>of</strong> CO 2 and Aquifer Brine on Well Plugging Cements<br />

Steve Gerdemann, G.E. Rush, Bill O’Connor, NETL, USA<br />

General consensus is that CO 2 at injection pressures in a saline environment will degrade<br />

portland based well plugging cements. Long term exposure, years or decades are typical<br />

time frames mentioned and modeled. Actual cement samples from CO 2 environments such<br />

as oil fields in which CO 2 has been used to extend field production are rare, and actual<br />

brackish to saline aquifer rock with CO 2 exposure still less common. Laboratory experiments<br />

to simulate the saline environments were run with interesting results.<br />

6-2<br />

Using Pinnate Well Patterns for CO 2 Sequestration in<br />

Allison Unit Reservoir Simulation Study<br />

Jalal Jalali, Shahab Mohaghegh, West Virginia <strong>University</strong>, USA<br />

Concerns about rising concentrations <strong>of</strong> carbon dioxide (CO 2 ) in the atmosphere and the<br />

necessity <strong>of</strong> reducing greenhouse gas emissions has led to consideration <strong>of</strong> large-scale<br />

storage <strong>of</strong> CO 2 in subsurface. Carbon dioxide is injected into unminable coal seams for<br />

enhancing the coalbed methane recovery, which also has the extra advantage <strong>of</strong> long-term<br />

CO 2 sequestration. Pilot projects exist in North America and some European countries to<br />

study the feasibility <strong>of</strong> CO 2 sequestration in depleted oil and gas reservoirs.<br />

Among different well patterns currently used for primary recovery <strong>of</strong> coalbed methane,<br />

horizontal pinnate wells demonstrate high methane recovery in a short period <strong>of</strong> time along<br />

with cost reductions and smaller footprints.<br />

In this study, a pinnate well is first used for primary recovery <strong>of</strong> methane and then converted<br />

into an injector for CO 2 injection to enhance the methane recovery and eventually long term<br />

sequestration. The large contact area between the wellbore and the formation helps fast<br />

dewatering, hence producing the methane, which is desorbed from the coal matrix into the<br />

natural fractures. The pinnate pattern distributes the CO 2 in a large area <strong>of</strong> the formation<br />

before it reaches the producing wells. Therefore, a larger amount <strong>of</strong> CO 2 could be stored in<br />

the formation before CO 2 breakthrough occurs.<br />

In this paper, a feasibility study <strong>of</strong> CO 2 sequestration using pinnate patterns into a coal seam<br />

in the Allison Unit is presented. Several characteristics <strong>of</strong> the pinnate pattern and the CO 2<br />

injection strategy are studied and optimized using a numerical reservoir simulator in order to<br />

increase the methane recovery and total CO 2 that can be stored before breakthrough. Results<br />

will be compared with the results from the well pattern currently used for CO 2 flooding in<br />

the field.<br />

6-3<br />

Experimental Measurements <strong>of</strong> the Solubility <strong>of</strong> CO 2 in<br />

the Oriskany Sandstone Aquifer<br />

Robert M. Dilmore, Patrice Pique, Sheila Hedges, Yee Soong, R. J. Jones,<br />

DOE/NETL, USA<br />

5<br />

Douglas Allen, DOE/NETL, Salem State College, USA<br />

Experiments were conducted to determine the solubility <strong>of</strong> CO 2 in a natural brine<br />

solution <strong>of</strong> the Oriskany sandstone formation under elevated temperature and pressure<br />

conditions. These data were collected at pressures between 100 and 450 bars and at<br />

temperatures <strong>of</strong> 21 and 75ºC. In addition, data on CO 2 solubility in pure water were<br />

collected over the same pressure range as a means <strong>of</strong> verifying reliability <strong>of</strong><br />

experimental technique. Experimentally determined data were compared with CO 2<br />

solubility predictions using a model developed by Duan and Sun (2003). Model results<br />

compare well with Oriskany brine CO 2 solubility data collected experimentally,<br />

suggesting that the Duan and Sun model is a reliable tool for estimating solution CO 2<br />

capacity in high salinity aquifers in the temperature and pressure range evaluated.<br />

6-4<br />

Evaluation <strong>of</strong> CO 2 Flood on the Geomechanics <strong>of</strong> Whole Core Samples<br />

Steve Gerdemann, Hank Rush, Bill O'Connor, NETL, USA<br />

Geological sequestration <strong>of</strong> CO 2 , whether by enhanced oil recovery (EOR), coal-bed<br />

methane (CBM) recovery, or saline-aquifer injection, is a promising near-term sequestration<br />

methodology. While tremendous experience exists for EOR, and CBM recovery has been<br />

demonstrated in existing fields, saline-aquifer-injection studies have only recently been<br />

initiated. Studies evaluating the availability <strong>of</strong> saline aquifers suitable for CO 2 injection show<br />

great potential.<br />

This study evaluated the physical and chemical effects on Mt. Simon sandstone core from<br />

the Illinois Basin exposed to simulated deep-aquifer brine saturated with super-critical CO 2 .<br />

Conducting these tests on whole core samples rather than crushed core allowed an<br />

evaluation <strong>of</strong> the impact <strong>of</strong> the CO 2 flood on the rock-mechanics properties as well as the<br />

geochemistry <strong>of</strong> the core and brine solution. Preliminary results show an increase in porosity<br />

and a decrease in crushing strength <strong>of</strong> the core after exposure to CO 2 for 2000 hours.<br />

6-5<br />

Sequestration <strong>of</strong> CO 2 in Mixtures <strong>of</strong> Bauxite Residue and Saline Waste Water<br />

with Carbonate Mineral Formation and Caustic Byproduct Neutralization<br />

Robert Dilmore, Yee Soong, Sheila Hedges, Angelo Degalbo, DOE/NETL, USA<br />

Douglas Allen, DOE/NETL, Salem State College, USA<br />

Jaw K. Fu, Charles L. Dobbs, ALCOA, USA<br />

Chen Zhu, Indiana <strong>University</strong>, USA<br />

Under consideration is a process designed to enhance the CO 2 trapping capacity <strong>of</strong><br />

brine solutions through addition <strong>of</strong> bauxite residue with subsequent carbonation <strong>of</strong> the<br />

caustic mixture. A set <strong>of</strong> experiments was conducted to explore the concept <strong>of</strong> utilizing<br />

mixtures <strong>of</strong> bauxite residue and brine to sequester carbon dioxide from industrial gas<br />

streams such as flue gas from coal fired electric utility boilers. Factors affecting the<br />

solubility <strong>of</strong> acid gasses in such mixtures include temperature, pressure, and water<br />

chemistry properties including pH, ionic concentration, and salinity. Bauxite<br />

residue/brine mixture <strong>of</strong> 90/10 by volume exhibited a CO 2 sequestration capacity <strong>of</strong><br />

greater than 9.5 grams per liter when exposed pure CO 2 at 20ºC and 100 psig. Calcite<br />

formation was verified as a product <strong>of</strong> bauxite/brine mixture carbonation. Data<br />

presented herein provide a preliminary assessment <strong>of</strong> overall process feasibility and<br />

probe the influence <strong>of</strong> several variables on treatment efficiency. It is demonstrated that<br />

CO 2 sequestration is augmented by adding bauxite residue as a caustic agent to acidic<br />

brine solutions, and that trapping is accomplished through solubilization and ultimate<br />

mineralization.<br />

SESSION 7<br />

GASIFICATION TECHNOLOGIES:<br />

APPLICATIONS AND ECONOMICS – 2<br />

7-1<br />

The Shell Coal Gasification Process<br />

Hugo T. P. Bos, F.G. van Dongen, Shell Global Solutions International BV, THE<br />

NETHERLANDS<br />

The latest status <strong>of</strong> the Shell Coal gasification Process (SCGP) is discussed.<br />

Applications <strong>of</strong> gasification for chemicals production and power production are given.<br />

Projects throughout the world are presented including the status <strong>of</strong> completion/ startup.<br />

The latest developments <strong>of</strong> the Shell Coal gasification Process are presented such as<br />

combined oil + coal gasification, biomass/coal to liquids conversion and methods for<br />

CO 2 sequestration.<br />

7-2<br />

The GSP Gasification Process; State-<strong>of</strong>-the-Art and Further Development<br />

Manfred Schingnitz, Klaus-Dieter Klemmer, Future Energy GmbH, GERMANY<br />

The development <strong>of</strong> the GSP-Process, a pulverized fuel pressure gasification technology,<br />

was started in 1975 by Deutsches Brennst<strong>of</strong>finstitut Freiberg/Sa. (DBI, German Fuel<br />

Research Institute). Main objective for this development was the demand to save crude oil

Hooray! Your file is uploaded and ready to be published.

Saved successfully!

Ooh no, something went wrong!