Methanol Synthesis from Industrial CO2 Sources: A Contribution to Chemical Energy Conversion

被引:104
作者
Bukhtiyarova, Marina [1 ]
Lunkenbein, Thomas [2 ]
Kaehler, Kevin [1 ]
Schloegl, Robert [1 ,2 ]
机构
[1] Max Planck Inst Chem Energy Convers, Stiftstr 34-36, D-45470 Mulheim, Germany
[2] Max Planck Gesell, Fritz Haber Inst, Faradayweg 4-6, D-14195 Berlin, Germany
关键词
Methanol synthesis; Carbon dioxide; Activation energy < elementary kinetics; Stability; Benzene impurities; CU/ZNO-BASED CATALYSTS; GAS SHIFT KINETICS; OXIDE CATALYST; HYDROGENATION; DEACTIVATION; ZNO; STABILITY; MECHANISM; AL;
D O I
10.1007/s10562-016-1960-x
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
CO2 hydrogenation as a route for the chemical energy storage over a commercial Cu/ZnO/Al2O3 catalyst has been studied. To check the optimal conditions for an efficient methanol production the influence of temperature and space velocity on the catalytic performance has been demonstrated. Time-on-stream measurements in the absence and the presence of benzene in the gas feed mixture were performed to investigate the possibility to use alternative carbon sources, which contain traces of aromatics. The catalyst can operate in a stable way without the presence of carbon monoxide in the feed, which means that increased water contents in the product gas cannot destroy the catalyst's performance completely. The presence of benzene in the feed does not lead to a deactivation of the catalyst. With these findings methanol production starting from exhaust gases from steel mills seems to become an interesting alternative for sustainable methanol production. [GRAPHICS] .
引用
收藏
页码:416 / 427
页数:12
相关论文
共 39 条
[1]  
[Anonymous], 2008, HDB HETEROGENEOUS CA
[2]  
[Anonymous], 2011, METHANOL CLEAR ALTER
[3]   Impact of K and Ba promoters on CO2 hydrogenation over Cu/Al2O3 catalysts at high pressure [J].
Bansode, Atul ;
Tidona, Bruno ;
von Rohr, Philipp Rudolf ;
Urakawa, Atsushi .
CATALYSIS SCIENCE & TECHNOLOGY, 2013, 3 (03) :767-778
[4]  
Bart J.C.J., 1987, CATAL TODAY, V2, P1, DOI [10.1016/0920-5861(87)80001-9, DOI 10.1016/0920-5861(87)80001-9]
[5]   New process for producing methanol from coke oven gas by means of CO2 reforming. Comparison with conventional process [J].
Bermudez, J. M. ;
Ferrera-Lorenzo, N. ;
Luque, S. ;
Arenillas, A. ;
Menendez, J. A. .
FUEL PROCESSING TECHNOLOGY, 2013, 115 :215-221
[6]   Synthesis Gas Processes for Methanol Production via CH4 Reforming with CO2, H2O, and O2 [J].
Canete, Benjamin ;
Gigola, Carlos E. ;
Brignole, Nelida B. .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2014, 53 (17) :7103-7112
[7]   MECHANISM OF METHANOL SYNTHESIS FROM CO2/CO/H2 MIXTURES OVER COPPER/ZINC OXIDE/ALUMINA CATALYSTS - USE OF C-14-LABELED REACTANTS [J].
CHINCHEN, GC ;
DENNY, PJ ;
PARKER, DG ;
SPENCER, MS ;
WHAN, DA .
APPLIED CATALYSIS, 1987, 30 (02) :333-338
[8]  
Chunshan S., 2006, CATAL TODAY, V115, P2
[9]   Wetting/non-wetting phenomena during catalysis: evidence from in situ on-line EXAFS studies of Cu-based catalysts [J].
Clausen, Bjerne S. ;
Schiotz, Jakob ;
Grabaek, Lars ;
Ovesen, Charlotte V. ;
Jacobsen, Karsten W. ;
Norskov, Jens K. ;
Topsoe, Henrik .
TOPICS IN CATALYSIS, 1994, 1 (3-4) :367-376
[10]   Promoting effect of a Cu-Zn binary precursor on a ternary Cu-Zn-Al catalyst for methanol synthesis from synthesis gas [J].
Ding, Wen ;
Liu, Yingwei ;
Wang, Fang ;
Zhou, Shuailing ;
Chen, Aiping ;
Yang, Yiquan ;
Fang, Weiping .
RSC ADVANCES, 2014, 4 (58) :30677-30682