Reaction phenomena of high-temperature water gas shift reaction in a membrane reactor

作者: Wei-Hsin Chen , Ching-Wei Tsai , Yu-Li Lin , Rei-Yu Chein , Ching-Tsung Yu

DOI: 10.1016/J.FUEL.2017.03.002

关键词:

摘要: Abstract The membrane reactor is a promising device to produce pure hydrogen and enrich CO 2 from syngas. To figure out the detailed reaction phenomena of high-temperature water gas shift (WGSR) in Pd-based reactor, computational fluid dynamics (CFD) model developed simulate chemical where feed temperature steam-to-CO molar ratio (S/C ratio) are ranges 400–700 °C 1–3, respectively. predictions suggest that WGSR proceeds kinetically controlled thermodynamically governed one when increases. conversion at high temperatures can be improved up 83% compared without membrane. This mainly attributed intensification membrane’s permeance with increasing temperature, even though disadvantage conversion. analysis also reveals breakthrough thermodynamic limit achieved higher than 500 °C. equilibrium 61%.

参考文章(48)
M.L. Ang, U. Oemar, Y. Kathiraser, E.T. Saw, C.H.K. Lew, Y. Du, A. Borgna, S. Kawi, High-temperature water–gas shift reaction over Ni/xK/CeO2 catalysts: Suppression of methanation via formation of bridging carbonyls Journal of Catalysis. ,vol. 329, pp. 130- 143 ,(2015) , 10.1016/J.JCAT.2015.04.031
Farshad Farshchi Tabrizi, Seyed Amir Hossein Seyed Mousavi, Hossein Atashi, Thermodynamic analysis of steam reforming of methane with statistical approaches Energy Conversion and Management. ,vol. 103, pp. 1065- 1077 ,(2015) , 10.1016/J.ENCONMAN.2015.07.005
Fereshteh Meshkani, Mehran Rezaei, Hydrogen production by high temperature water gas shift reaction over highly active and stable chromium free Fe–Al–Ni catalysts International Journal of Hydrogen Energy. ,vol. 40, pp. 10867- 10875 ,(2015) , 10.1016/J.IJHYDENE.2015.06.170
Xueliang Dong, Haibing Wang, Zebao Rui, Y.S. Lin, Tubular dual-layer MFI zeolite membrane reactor for hydrogen production via the WGS reaction: Experimental and modeling studies Chemical Engineering Journal. ,vol. 268, pp. 219- 229 ,(2015) , 10.1016/J.CEJ.2015.01.046
H.A.J. van Dijk, D. Cohen, A.A. Hakeem, M. Makkee, K. Damen, Validation of a water–gas shift reactor model based on a commercial FeCr catalyst for pre-combustion CO2 capture in an IGCC power plant International Journal of Greenhouse Gas Control. ,vol. 29, pp. 82- 91 ,(2014) , 10.1016/J.IJGGC.2014.07.005
Trevor L. LeValley, Anthony R. Richard, Maohong Fan, The progress in water gas shift and steam reforming hydrogen production technologies – A review International Journal of Hydrogen Energy. ,vol. 39, pp. 16983- 17000 ,(2014) , 10.1016/J.IJHYDENE.2014.08.041
Wei-Hsin Chen, Yu-Jhih Syu, Hydrogen production from water gas shift reaction in a high gravity (Higee) environment using a rotating packed bed International Journal of Hydrogen Energy. ,vol. 35, pp. 10179- 10189 ,(2010) , 10.1016/J.IJHYDENE.2010.07.126
M DEFALCO, L DIPAOLA, L MARRELLI, Heat transfer and hydrogen permeability in modelling industrial membrane reactors for methane steam reforming International Journal of Hydrogen Energy. ,vol. 32, pp. 2902- 2913 ,(2007) , 10.1016/J.IJHYDENE.2007.04.014
M. Esperanza Adrover, Eduardo López, Daniel O. Borio, Marisa N. Pedernera, Simulation of a membrane reactor for the WGS reaction: Pressure and thermal effects Chemical Engineering Journal. ,vol. 154, pp. 196- 202 ,(2009) , 10.1016/J.CEJ.2009.04.057