Thermodynamic Analyses of a Moderate-Temperature Process of Carbon Dioxide Hydrogenation to Methanol via Reverse Water-Gas Shift with In Situ Water Removal

被引:42
作者
Cui, Xiaoti [1 ]
Kaer, Soren K. [1 ]
机构
[1] Aalborg Univ, Dept Energy Technol, DK-9220 Aalborg, Denmark
关键词
CO2; HYDROGENATION; DIMETHYL ETHER; MEMBRANE REACTOR; SORPTION; CATALYSTS; DEACTIVATION; OPTIMIZATION; SIMULATION;
D O I
10.1021/acs.iecr.9b01312
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
CO2 hydrogenation to methanol via the reverse water-gas shift (the CAMERE process) is an alternative method for methanol synthesis. High operating temperatures (600-800 degrees C) are required for the reverse water-gas shift (RWGS) process because of the thermodynamic limit. In this study, moderate temperatures (200-300 degrees C) were used for the RWGS part of the CAMERE process by the application of in situ water removal (ISWR). Thermodynamic analyses were conducted on this process using the Gibbs-free-energy-minimization method. The analyses show that by using ISWR with high water-removal fractions (e.g., 0.80-0.99), the CO2 conversion of the RWGS part can be significantly improved at moderate operating temperatures. One-step CO2 hydrogenation to methanol (CTM) with ISWR was also investigated, and it resulted in similar methanol yields. Both processes showed high potential and the ability to promote CO2 hydrogenation to methanol through the use of ISWR.
引用
收藏
页码:10559 / 10569
页数:11
相关论文
共 42 条
[1]   Deactivation and regeneration of hybrid catalysts in the single-step synthesis of dimethyl ether from syngas and CO2 [J].
Aguayo, AT ;
Ereña, J ;
Sierra, I ;
Olazar, M ;
Bilbao, J .
CATALYSIS TODAY, 2005, 106 (1-4) :265-270
[2]   Comparison between two methods of methanol production from carbon dioxide [J].
Anicic, B. ;
Trop, P. ;
Goricanec, D. .
ENERGY, 2014, 77 :279-289
[3]  
[Anonymous], 2001, THESIS
[4]   Synthesis, characterization and activity pattern of Cu-ZnO/ZrO2 catalysts in the hydrogenation of carbon dioxide to methanol [J].
Arena, Francesco ;
Barbera, Katia ;
Italiano, Giuseppe ;
Bonura, Giuseppe ;
Spadaro, Lorenzo ;
Frusteri, Francesco .
JOURNAL OF CATALYSIS, 2007, 249 (02) :185-194
[5]   Optimal Methanol Production via Sorption-Enhanced Reaction Process [J].
Arora, Akhil ;
Iyer, Shachit S. ;
Bajaj, Ishan ;
Hasan, M. M. Faruque .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2018, 57 (42) :14143-14161
[6]   Thermocatalytic CO2 hydrogenation for methanol and ethanol production: Process improvements [J].
Atsonios, Konstantinos ;
Panopoulos, Kyriakos D. ;
Kakaras, Emmanuel .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2016, 41 (02) :792-806
[7]   Simulation of CO2 hydrogenation with CH3OH removal in a zeolite membrane reactor [J].
Barbieri, G ;
Marigliano, G ;
Golemme, G ;
Drioli, E .
CHEMICAL ENGINEERING JOURNAL, 2002, 85 (01) :53-59
[8]  
Bertau M., 2014, METHANOL BASIC CHEM, Vfirst
[9]   Sorption enhanced CO2 methanation [J].
Borgschulte, Andreas ;
Gallandat, Noris ;
Probst, Benjamin ;
Suter, Riccardo ;
Callini, Elsa ;
Ferri, Davide ;
Arroyo, Yadira ;
Erni, Rolf ;
Geerlings, Hans ;
Zuettel, Andreas .
PHYSICAL CHEMISTRY CHEMICAL PHYSICS, 2013, 15 (24) :9620-9625
[10]   Efficient methanol synthesis: Perspectives, technologies and optimization strategies [J].
Bozzano, Giulia ;
Manenti, Flavio .
PROGRESS IN ENERGY AND COMBUSTION SCIENCE, 2016, 56 :71-105