470738 Highly Efficient Warm Gas Carbon Capture System for IGCC Power Plants

Monday, November 14, 2016: 12:51 PM
Van Ness (Hilton San Francisco Union Square)
Ambalavanan Jayaraman1, Gokhan Alptekin1, Steve Dietz1, Matt Cates1, Michael Bonnema1, Chakravarthy Sishtla2 and Ashok Rao3, (1)TDA Research Inc., Wheat Ridge, CO, (2)Gas Technology Institute, Des Plaines, IL, (3)Advanced Power & Energy Program, University of California, Irvine, CA

TDA is developing a novel sorbent that removes CO2 via physical adsorption from synthesis gas. The relatively strong affinity of the sorbent to CO2 enables effective operation at temperatures up to 300oC (well above the dew point of synthesis gas stream generated by commercial gasifiers). However, because the sorbent and the CO2 do not form a true covalent bond, the energy needed to regenerate TDA’s sorbent (5.4 kcal per mol of CO2) is much lower than that observed for either chemical absorbents (e.g., 29.9 kcal/mol CO2 for sodium carbonate) or amine-based solvents (e.g., 14.2 kcal/mol CO2 for monoethanolamine). TDA’s sorbent can be regenerated isothermally and CO2 can be recovered at pressure (as high as 150 psia). Thus, the energy needed to regenerate the sorbent and compress the CO2 for sequestration is significantly lower than that for any other technology reported to date. The high surface area and favorable porosity of the sorbent also provides a unique platform to introduce additional functionality, such as active groups to catalyze the water-gas-shift (WGS) reaction or to remove trace metals (e.g., Hg, As). Hence, TDA’s CO2 sorbent could be used to do a warm gas capture of CO2 above the dew point of the synthesis gas in an Integrated Gasification Combined Cycle (IGCC) power plant. TDA's pre-combustion CO2 capture system achieves a net plant efficiency of 34% on a coal high heating value basis when operated on bituminous coal, which is significantly higher than that can be achieved with the SelexolTM scrubber at 31.6% (state-of-the-art pre-combustion carbon capture technology). The levelized cost of electricity including the transport, storage and monitoring costs for CO2 is calculated as $92.9/MWh for TDA's system, in comparison to $105.2/MWh for SelexolTM. In a current DOE sponsored project, TDA is preparing to carryout field tests with the warm gas CO2 capture unit at 0.1 MWe scale. In this paper we present the results from the system analysis, bench-scale evaluations, and the fabrication and testing of the 0.1 MWe field test unit.

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