Experimental Investigation of the Application of Ionic Liquids to Methanol Synthesis in Membrane Reactors

被引:19
作者
Zebarjad, Fatemeh Sadat [1 ]
Hu, Sheng [1 ]
Li, Zhongtang [1 ,2 ]
Tsotsis, Theodore T. [1 ]
机构
[1] Univ Southern Calif, Mork Family Dept Chem Engn & Mat Sci, Univ Pk, Los Angeles, CA 90089 USA
[2] Palcan Energy Corp, 111 Xiangke Rd, Shanghai 201203, Peoples R China
基金
美国国家科学基金会;
关键词
FISCHER-TROPSCH SYNTHESIS; DIFFERENTIAL EVOLUTION; HYDROGEN-PRODUCTION; CYCLOHEXANE DEHYDROGENATION; ULTRAPURE HYDROGEN; CO2; HYDROGENATION; OPTIMIZATION; DECOMPOSITION; PERFORMANCE; STRATEGY;
D O I
10.1021/acs.iecr.9b01178
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
In this study, a high-pressure membrane reactor (MR) was employed to carry out the methanol synthesis (MeS) reaction. Syngas was fed into the MR shell side where a commercial MeS catalyst was used, while the tube side was swept with a high boiling point liquid with good solubility toward methanol. A mesoporous alumina ceramic membrane was utilized after its surface had been modified to be rendered more hydrophobic. The efficiency of the MR was investigated under a variety of experimental conditions (different pressures, temperatures, sweep liquid flow rates, and types of sweep liquids). The results reveal improved per single-pass carbon conversions when compared to the conventional packed-bed reactor. An ionic liquid (IL), 1-ethyl-3-methylimidazolium tetrafluoroborate, was utilized in the MR as the sweep liquid. The experimental results are compared to those previously reported by our group (Li, Z.; Tsotsis, T. T. J. Membrane Sci. 2019, 570, 103) while using a conventional petroleum-derived solvent as sweep liquid, tetraethylene glycol dimethyl ether (TGDE). Enhanced carbon conversion (over the petroleum-derived solvent) was obtained using the IL.
引用
收藏
页码:11811 / 11820
页数:10
相关论文
共 53 条
[1]  
Aasberg-Petersen K., 2008, Large Scale Methanol Production from Natural Gas
[2]   Hydrogen production by methane decomposition: A review [J].
Abbas, Hazzim F. ;
Daud, W. M. A. Wan .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2010, 35 (03) :1160-1190
[3]  
[Anonymous], 2001, ANGEW CHEM
[4]   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
[5]   Simultaneous hydrogen and methanol enhancement through a recuperative two-zone thermally coupled membrane reactor [J].
Bayat, M. ;
Rahimpour, M.R. .
Energy Systems, 2012, 3 (04) :401-420
[6]   Simultaneous hydrogen injection and in-situ H2O removal in a novel thermally coupled two-membrane reactor concept for Fischer-Tropsch synthesis in GTL technology [J].
Bayat, M. ;
Rahimpour, M. R. .
JOURNAL OF NATURAL GAS SCIENCE AND ENGINEERING, 2012, 9 :73-85
[7]   A comparative study of two different configurations for exothermic-endothermic heat exchanger reactor [J].
Bayat, M. ;
Rahimpour, M. R. ;
Taheri, M. ;
Pashaei, M. ;
Sharifzadeh, S. .
CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 2012, 52 :63-73
[8]   Simultaneous utilization of two different membranes for intensification of ultrapure hydrogen production from recuperative coupling autothermal multitubular reactor [J].
Bayat, M. ;
Rahimpour, M. R. .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2011, 36 (12) :7310-7325
[9]  
Behr A., 2014, ANGEW CHEM INT EDIT, V53, P12674, DOI [10.1002/anie.201409583, DOI 10.1002/ANIE.201409583]
[10]   Monolith loop catalytic membrane reactor for Fischer-Tropsch synthesis [J].
Bradford, MCJ ;
Te, M ;
Pollack, A .
APPLIED CATALYSIS A-GENERAL, 2005, 283 (1-2) :39-46