Synthesis of methanol and dimethyl ether from the CO2 hydrogenation over Cu•ZnO supported on Al2O3 and Nb2O5

被引:79
作者
da Silva, Renata J. [1 ]
Pimentel, Allan F. [2 ]
Monteiro, Robson S. [2 ,3 ]
Mota, Claudio J. A. [1 ,2 ,4 ]
机构
[1] Univ Fed Rio de Janeiro, Escola Quim, Av Athos da Silveira Ramos 149,CT Bloco E, BR-21941909 Rio De Janeiro, Brazil
[2] Univ Fed Rio de Janeiro, Inst Quim, Av Athos da Silveira Ramos 149,CT Bloco A, BR-21941909 Rio De Janeiro, Brazil
[3] Catalysis Consultoria Ltda, Av Amer 7837, BR-22793081 Rio De Janeiro, Brazil
[4] Univ Fed Rio de Janeiro, INCT Energia & Ambiente, BR-21941909 Rio de Janeiro, RJ, Brazil
关键词
Methanol Dimethyl ether; CO2; hydrogenation; Al2O3; Nb2O5; VALUE-ADDED PRODUCTS; CARBON-DIOXIDE; SYNTHESIS CATALYSTS; TO-HYDROCARBONS; CONVERSION; DME; DEHYDRATION; GAS; OPPORTUNITIES; CHALLENGES;
D O I
10.1016/j.jcou.2016.01.006
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
We report the synthesis, characterization and catalytic evaluation of Cu center dot ZnO catalysts supported on Al2O3 and Nb2O5, as acidic materials, to study the CO2 hydrogenation to methanol and dimethyl ether. The catalysts were prepared by precipitation or impregnation of the metals over the supports. They were characterized by different techniques, such as XRF, BET area, TPD of n-butylamine, XRD and TPR. Catalytic tests were performed in an automated catalytic unit coupled to a gas chromatograph with FID and TCD detectors. Different conditions of temperature and pressure were studied. It could be observed that the choice of the synthesis method affects the activity and selectivity of the CO2 hydrogenation, at the conditions used in this work. The catalyst prepared by impregnation of the metals over the Al2O3 support was the most active and selective to dimethyl ether. This result can be explained by the better and lower temperature reducibility of CuO particles along with higher density of acid sites and strength of the alumina support. (C) 2016 Elsevier Ltd. All rights reserved.
引用
收藏
页码:83 / 88
页数:6
相关论文
共 48 条
[11]   The influence of different methanol synthesis catalysts on direct synthesis of DME from syngas [J].
Flores, J. H. ;
Peixoto, D. P. B. ;
Appel, L. G. ;
de Avillez, R. R. ;
Pais da Silva, M. I. .
CATALYSIS TODAY, 2011, 172 (01) :218-225
[12]   The chemical modification seen in the Cu/ZnO methanol synthesis catalysts [J].
Fujitani, T ;
Nakamura, J .
APPLIED CATALYSIS A-GENERAL, 2000, 191 (1-2) :111-129
[13]   Conversion of carbon dioxide into methanol - a potential liquid fuel: Fundamental challenges and opportunities (a review) [J].
Ganesh, Ibram .
RENEWABLE & SUSTAINABLE ENERGY REVIEWS, 2014, 31 :221-257
[14]   Recycling of carbon dioxide to methanol and derived products - closing the loop [J].
Goeppert, Alain ;
Czaun, Miklos ;
Jones, John-Paul ;
Prakash, G. K. Surya ;
Olah, George A. .
CHEMICAL SOCIETY REVIEWS, 2014, 43 (23) :7995-8048
[15]   Acetylation of glycerol catalyzed by different solid acids [J].
Goncalves, Valter L. C. ;
Pinto, Bianca P. ;
Silva, Joao C. ;
Mota, Claudio J. A. .
CATALYSIS TODAY, 2008, 133 (1-4) :673-677
[16]   ACIDIC AND CATALYTIC PROPERTIES OF NIOBIUM PENTAOXIDE [J].
IIZUKA, T ;
OGASAWARA, K ;
TANABE, K .
BULLETIN OF THE CHEMICAL SOCIETY OF JAPAN, 1983, 56 (10) :2927-2931
[17]   Carbon Capture and Recycle by Integration of CCS and Green Hydrogen [J].
Kameyama, Hiromichi ;
Yoshizaki, Koji ;
Yasuda, Isamu .
10TH INTERNATIONAL CONFERENCE ON GREENHOUSE GAS CONTROL TECHNOLOGIES, 2011, 4 :2669-2676
[18]   Methanol-to-hydrocarbons: process technology [J].
Keil, FJ .
MICROPOROUS AND MESOPOROUS MATERIALS, 1999, 29 (1-2) :49-66
[19]   Catalytic conversion of chloromethane to methanol and dimethyl ether over mesoporous γ-alumina [J].
Khaleel, Abbas ;
Shehadi, Ihsan ;
Al-Marzouqi, Ali .
FUEL PROCESSING TECHNOLOGY, 2011, 92 (09) :1783-1789
[20]  
Marceau E., 2009, SYNTHESIS SOLID CATA, P59, DOI DOI 10.1002/9783527626854.CH4