High-purity hydrogen production through sorption enhanced water gas shift reaction using K2CO3-promoted hydrotalcite

Sorption enhanced water gas shift (SEWGS) reaction is a process concept, which simultaneously carries out the gas phase water gas shift (WGS) reaction (CO+H2O↔CO2+H2) and selective chemisorption of the byproduct CO2 from the gas phase reaction zone for direct production of essentially pure H2 in a single unit operation. A packed bed sorber-reactor containing an admixture of a WGS catalyst and a CO2 chermisorbent is used in the process. The concept circumvents the thermodynamic limitation of the WGS reaction and enhances the rate of reaction for H2 production. In this study, the SEWGS reaction concept was successfully demonstrated by both experiment and numerical simulation using K2CO3-promoted hydrotalcite as the CO2 sorbent. Numerical model simulations were also carried out to investigate the effects of various operating conditions of SEWGS reaction on the process performance. In general, higher H2O/CO feed ratio, higher fraction of sorbent (chemisorbent ratio in the sorber-reactor), and lower operating temperature favor both H2 productivity and CO conversion. Higher reaction pressure increases H2 productivity but decreases CO conversion.

[1]  R. Siriwardane,et al.  Sorption-enhanced water gas shift reaction by sodium-promoted calcium oxides , 2010 .

[2]  Ki Bong Lee,et al.  Reversible Chemisorbents for Carbon Dioxide and Their Potential Applications , 2008 .

[3]  Yulong Ding,et al.  Adsorption-enhanced steam–methane reforming , 2000 .

[4]  Jong-Nam Kim,et al.  Hydrotalcites for adsorption of CO2 at high temperature , 2006 .

[5]  O. Levenspiel Chemical Reaction Engineering , 1972 .

[6]  Jeffrey Raymond Hufton,et al.  Sorption‐enhanced reaction process for hydrogen production , 1999 .

[7]  Rodney John Allam,et al.  Chapter 13 – Development of the Sorption Enhanced Water Gas Shift Process , 2005 .

[8]  Jae-goo Lee,et al.  Preparation of CuO-CeO2-Al2O3 catalyst with mesopore structure for water gas shift reaction , 2009 .

[9]  De Chen,et al.  Sorption enhanced hydrogen production by steam methane reforming using Li2ZrO3 as sorbent: Sorption kinetics and reactor simulation , 2005 .

[10]  Nicholas H. Florin,et al.  Enhanced hydrogen production from biomass with in situ carbon dioxide capture using calcium oxide sorbents , 2008 .

[11]  David A. Bell,et al.  Coal Gasification and Its Applications , 2010 .

[12]  Douglas P. Harrison,et al.  Simultaneous shift reaction and carbon dioxide separation for the direct production of hydrogen , 1994 .

[13]  A. I. Lysikov,et al.  Sorption properties of lithium carbonate doped CaO and its performance in sorption enhanced methane reforming , 2011 .

[14]  Alírio E. Rodrigues,et al.  Hydrogen production from steam methane reforming coupled with in situ CO2 capture : Conceptual parametric study , 2005 .

[15]  S. Sircar,et al.  Chemisorption of carbon dioxide on potassium-carbonate-promoted hydrotalcite. , 2007, Journal of colloid and interface science.

[16]  Julian R.H. Ross,et al.  Catalysis for conversion of biomass to fuels via pyrolysis and gasification: A review , 2011 .

[17]  A. L. Ortíz,et al.  Hydrogen from methane in a single-step process , 1999 .

[18]  Jeffrey Raymond Hufton,et al.  Sorption-enhanced reaction process , 1996 .

[19]  Ki Bong Lee,et al.  Reversible chemisorption of carbon dioxide: simultaneous production of fuel-cell grade H2 and compressed CO2 from synthesis gas , 2007 .

[20]  K. Sotowa,et al.  Hydrogen production in zirconia membrane reactors for use in PEM fuel cells , 2005 .

[21]  J. Natowitz,et al.  Our Energy Future , 2009 .

[22]  Harvey G. Stenger,et al.  Water gas shift reaction kinetics and reactor modeling for fuel cell grade hydrogen , 2003 .

[23]  Ki Bong Lee,et al.  Enhancement of CO2 sorption uptake on hydrotalcite by impregnation with K2CO3. , 2010, Langmuir : the ACS journal of surfaces and colloids.

[24]  Ki Bong Lee,et al.  Effect of reaction temperature on the performance of thermal swing sorption enhanced reaction process for simultaneous production of fuel cell grade H2 and compressed CO2 from synthesis gas , 2008 .

[25]  Fabrizio Cavani,et al.  Hydrotalcite-type anionic clays: Preparation, properties and applications. , 1991 .

[26]  M. E. Bretado,et al.  Hydrogen production by absorption enhanced water gas shift (AEWGS) , 2010 .