Cu/ZnO/AlOOH catalyst for methanol synthesis through CO2 hydrogenation

被引:59
作者
Choi, EunGyoung [1 ,2 ]
Song, KyoungHo [1 ,2 ]
An, SoRa [1 ,2 ]
Lee, KwanYoung [2 ]
Youn, MinHyeh [1 ]
Park, KiTae [1 ]
Jeong, SoonKwan [1 ]
Kim, HakJoo [1 ]
机构
[1] Korea Inst Energy Res, Greenhouse Gas Res Lab, Daejeon 34129, South Korea
[2] Korea Univ, Dept Chem & Biol Engn, Seoul 02841, South Korea
关键词
Methanol Synthesis; CO2; Hydrogenation; FT-IR; Copper-based Methanol Synthesis Catalyst; Catalyst Support; Adsorption; Temperature-programmed Desorption (TPD); CONTACT QUANTIFICATION MODEL; CU-ZNO SYNERGY; ACTIVE-SITE; SURFACE-PROPERTIES; CARBON-MONOXIDE; AL; MORPHOLOGY; MECHANISM; MIXTURES; ORIGIN;
D O I
10.1007/s11814-017-0230-y
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
Catalytic conversion of CO2 to methanol is gaining attention as a promising route to using carbon dioxide as a new carbon feedstock. AlOOH supported copper-based methanol synthesis catalyst was investigated for direct hydrogenation of CO2 to methanol. The bare AlOOH catalyst support was found to have increased adsorption capacity of CO2 compared to conventional Al2O3 support by CO2 temperature-programmed desorption (TPD) and FT-IR analysis. The catalytic activity measurement was carried out in a fixed bed reactor at 523 K, 30 atm and GHSV 6,000 hr(-1) with the feed gas of CO2/H-2 ratio of 1/3. The surface basicity of the AlOOH supported Cu-based catalysts increased linearly according to the amount of AlOOH. The optimum catalyst composition was found to be Cu : Zn : Al=40 : 30 : 30 at%. A decrease of methanol productivity was observed by further increasing the amount of AlOOH due to the limitation of hydrogenation rate on Cu sites. The AlOOH supported catalyst with optimum catalyst compositions was slightly more active than the conventional Al2O3 supported Cu-based catalyst.
引用
收藏
页码:73 / 81
页数:9
相关论文
共 37 条
[1]  
Audibert E., 1926, FUEL, V5, P170
[2]  
Behrens M, 2012, SCIENCE, V336, P893, DOI [10.1126/science.1219831, 10.1126/science.12198331]
[3]   The changing nature of the active site of Cu-Zn-Zr catalysts for the CO2 hydrogenation reaction to methanol [J].
Bonura, G. ;
Cordaro, M. ;
Cannilla, C. ;
Arena, F. ;
Frusteri, F. .
APPLIED CATALYSIS B-ENVIRONMENTAL, 2014, 152 :152-161
[4]  
Bratt D., 2016, Catalytic CO2 Hydrogenation - Literature Review : Technology Development since
[5]   THE ROLE OF COPPER AND ZINC-OXIDE IN METHANOL SYNTHESIS CATALYSTS [J].
BURCH, R ;
GOLUNSKI, SE ;
SPENCER, MS .
JOURNAL OF THE CHEMICAL SOCIETY-FARADAY TRANSACTIONS, 1990, 86 (15) :2683-2691
[6]   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
[7]  
Cornthwaite D., 1974, Patent, Patent No. [US3923694A, 3923694]
[8]  
DAVIES P, 1967, Patent No. 3326956
[9]   Structure and surface and catalytic properties of Mg-Al basic oxides [J].
Di Cosimo, JI ;
Diez, VK ;
Xu, M ;
Iglesia, E ;
Apesteguia, CR .
JOURNAL OF CATALYSIS, 1998, 178 (02) :499-510
[10]   STRUCTURE REFINEMENT OF BOEHMITE (GAMMA-A100H) AND STUDY OF ITS STRUCTURAL VARIABILITY BASED ON GUINIER-HAGG POWDER DATA [J].
FARKAS, L ;
GADO, P ;
WERNER, PE .
MATERIALS RESEARCH BULLETIN, 1977, 12 (12) :1213-1219