1997
DOI: 10.1016/s0196-8904(96)00263-4
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Water gas shift membrane reactor for CO2 control in IGCC systems: techno-economic feasibility study

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Cited by 111 publications
(66 citation statements)
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“…A case study on a coke gasification IGCC plant indicates that a novel cryogenic technology for CO 2 separation promises 16% reduction in CO 2 avoidance costs versus a base case with Selexol [77]. Various studies on the techno-economic impact of hightemperature membranes to separate CO 2 from H 2 , eventually integrated with water gas shift reactor, indicate that the IGCC conversion efficiency can be increased and investment costs reduced in comparison to physical absorption [7,29,78].…”
Section: Key Performance Datamentioning
confidence: 99%
“…A case study on a coke gasification IGCC plant indicates that a novel cryogenic technology for CO 2 separation promises 16% reduction in CO 2 avoidance costs versus a base case with Selexol [77]. Various studies on the techno-economic impact of hightemperature membranes to separate CO 2 from H 2 , eventually integrated with water gas shift reactor, indicate that the IGCC conversion efficiency can be increased and investment costs reduced in comparison to physical absorption [7,29,78].…”
Section: Key Performance Datamentioning
confidence: 99%
“…Another more detail techno-economic feasibility study (Bracht et al, 1997) 11 used a set of rather detail simulation and optimization tools for industrial scale membrane reactors (Koukou et al, 1998) 12 including computational fluid dynamics (CFD) along with mass and energy balances. Membrane reactors were shown to be efficient for the water gas shift reaction (WGS) in an IGCC plant with CO 2 emission control.…”
Section: Preliminary Techno-economic Analysismentioning
confidence: 99%
“…The combination of reaction and separation in WGSR in IGCC systems is an attractive future option for CO 2 removal, as compared to conventional options [115]. The membrane reactor provides simultaneous removal of H 2 or CO 2 in the WGS reaction to shift the reaction equilibrium towards the complete conversion of CO.…”
Section: Hydrotalcite Membranesmentioning
confidence: 99%
“…Several researchers [115][116][117][118] have utilized the WGS membrane reactor with H 2 removal using palladium or other metallic membranes. Criscuoli et al [116] have reported a H 2 /CO 2 separation factor of 1.46 at 325 °C from the mesoporous alumina membranes, which is significantly lower than the Knudsen value (4.7), because of the presence of viscous flow at elevated temperatures.…”
Section: Hydrotalcite Membranesmentioning
confidence: 99%