Role of acidity and microporous structure in alternative catalysts for the transformation of methanol into olefins

被引:161
作者
Aguayo, AT [1 ]
Gayubo, AG [1 ]
Vivanco, R [1 ]
Olazar, M [1 ]
Bilbao, J [1 ]
机构
[1] Univ Basque Country, Dept Ingn Quim, E-48080 Bilbao, Spain
关键词
MTO process; microporous catalysts; surface acidity; catalyst deactivation;
D O I
10.1016/j.apcata.2005.01.006
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
The transformation of methanol into light olefins (C-2-C-4) has been studied oil several acid catalysts prepared by agglomerating different microporous acid phases (SAPO-11, SAPO-18, SAPO-34 and beta-zeolites) with bentonite and inert alumina. SAPO-11s and beta-zeolites have been prepared under different conditions and, consequently, they have different porous structure, total acidity and site acid strength. An analysis is made of the influence of their properties (micropore diameter, total acidity, acid strength and site density on their surface) on the kinetic behaviour of the catalysts (initial conversion and selectivity to olefins and deactivation rate). The catalyst SAPO-18 has a lower deactivation rate than the SAPO-34 due to a slightly lower acid strength and to a lower density of strong acid sites on the surface. This behaviour and the lower preparation cost make SAPO-18 an interesting alternative to SAPO-34, which is the one used in industry in the MTO process. (c) 2005 Elsevier B.V. All rights reserved.
引用
收藏
页码:197 / 207
页数:11
相关论文
共 50 条
[1]  
AGUAYO AT, 1994, AFINIDAD, V51, P122
[2]   Study of operating variables in the transformation of aqueous ethanol into hydrocarbons on an HZSM-5 zeolite [J].
Aguayo, AT ;
Gayubo, AG ;
Tarrío, AM ;
Atutxa, A ;
Bilbao, J .
JOURNAL OF CHEMICAL TECHNOLOGY AND BIOTECHNOLOGY, 2002, 77 (02) :211-216
[3]   Catalyst deactivation by coke in the transformation of aqueous ethanol into hydrocarbons. Kinetic modeling and acidity deterioration of the catalyst [J].
Aguayo, AT ;
Gayubo, AG ;
Atutxa, A ;
Olazar, M ;
Bilbao, J .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2002, 41 (17) :4216-4224
[4]  
Aguayo AT, 1999, J CHEM TECHNOL BIOT, V74, P1082
[5]  
Aguayo AT, 1999, J CHEM TECHNOL BIOT, V74, P315
[6]   Catalyst deactivation by coking in the MTG process in fixed and fluidized bed reactors [J].
Aguayo, AT ;
Gayubo, AG ;
Ortega, JM ;
Olazar, M ;
Bilbao, J .
CATALYSIS TODAY, 1997, 37 (03) :239-248
[7]  
ANTHONY RG, 1981, HYDROCARB PROCESS, V60, P85
[8]  
Benito PL, 1996, J CHEM TECHNOL BIOT, V66, P183
[9]   Concentration-dependent kinetic model for catalyst deactivation in the MTG process [J].
Benito, PL ;
Gayubo, AG ;
Aguayo, AT ;
Castilla, M ;
Bilbao, J .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1996, 35 (01) :81-89
[10]  
BOND AE, 1974, Patent No. 3793385