Shape selective methanol to olefins over highly thermostable DDR catalysts

被引:54
作者
Kumita, Yasukazu [1 ,2 ]
Gascon, Jorge [1 ]
Stavitski, Eli [1 ,3 ]
Moulijn, Jacob A. [1 ]
Kapteijn, Freek [1 ]
机构
[1] Delft Univ Technol, Catalysis Engn Chem Engn Dept, NL-2628 BL Delft, Netherlands
[2] Kao Corp, Global R&D Proc Dev, Wakayama 6408580, Japan
[3] Univ Utrecht, Inorgan Chem & Catalysis Grp, Debye Inst Nanomat Sci, NL-3584 CA Utrecht, Netherlands
基金
美国国家科学基金会;
关键词
DDR; ZSM-58; MTO; ZSM-5; NH3-TPD; CARBONACEOUS DEPOSITS; ADSORPTION; CONVERSION; ZEOLITES; DIFFUSION; DEACTIVATION; HYDROCARBONS; SORPTION; SAPO-34; ACIDITY;
D O I
10.1016/j.apcata.2010.07.023
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
ZSM-58, having a DDR topology, is shown to be a very attractive catalyst for the direct formation of propylene and ethylene via conversion of methanol. A performance similar to the state of the art SAPO-34 catalysts is achieved, while no olefins longer than C-4 are formed. In addition, ZSM-58 has a much higher thermostability than SAPO catalysts. Mainly propylene, ethylene and linear butenes (trans-but-2-ene and butadiene) are formed when materials with the DDR topology are used as catalysts during the MTO process. The ratio propylene/ethylene can be tuned by changing the reaction conditions or the degree of catalyst coking. An optimum in performance, in terms of stability and selectivity, is found for catalysts containing one acid site (one Al) per accessible cavity. Deactivation of the catalysts takes place due to formation of coke and homogeneous blocking of the catalysts porosity. Activity is fully recovered after regeneration in air. (C) 2010 Elsevier B.V. All rights reserved.
引用
收藏
页码:234 / 243
页数:10
相关论文
共 38 条
[1]   Role of acidity and microporous structure in alternative catalysts for the transformation of methanol into olefins [J].
Aguayo, AT ;
Gayubo, AG ;
Vivanco, R ;
Olazar, M ;
Bilbao, J .
APPLIED CATALYSIS A-GENERAL, 2005, 283 (1-2) :197-207
[2]   Catalytic cracking of n-octane on small-pore zeolites [J].
Altwasser, S ;
Welker, C ;
Traa, Y ;
Weitkamp, J .
MICROPOROUS AND MESOPOROUS MATERIALS, 2005, 83 (1-3) :345-356
[3]  
Caspary K.J., 2008, HDB HETEROGENEOUS CA, P3207
[4]   Influence of coke on the acid properties of a USHY zeolite [J].
Cerqueira, HS ;
Ayrault, P ;
Datka, J ;
Guisnet, M .
MICROPOROUS AND MESOPOROUS MATERIALS, 2000, 38 (2-3) :197-205
[5]   The effect of crystal size of SAPO-34 on the selectivity and deactivation of the MTO reaction [J].
Chen, D ;
Moljord, K ;
Fuglerud, T ;
Holmen, A .
MICROPOROUS AND MESOPOROUS MATERIALS, 1999, 29 (1-2) :191-203
[6]   Methanol conversion to light olefins over SAPO-34. Sorption, diffusion, and catalytic reactions [J].
Chen, D ;
Rebo, HP ;
Moljord, K ;
Holmen, A .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1999, 38 (11) :4241-4249
[7]   Insights into the mechanism of methanol-to-olefin conversion at zeolites with systematically selected framework structures [J].
Cui, Zhi-Min ;
Liu, Qiang ;
Song, Wei-Guo ;
Wan, Li-Jun .
ANGEWANDTE CHEMIE-INTERNATIONAL EDITION, 2006, 45 (39) :6512-6515
[8]   The effect of crystallite size on the activity and selectivity of the reaction of ethanol and 2-propanol over SAPO-34 [J].
Dahl, IM ;
Wendelbo, R ;
Andersen, A ;
Akporiaye, D ;
Mostad, H ;
Fuglerud, T .
MICROPOROUS AND MESOPOROUS MATERIALS, 1999, 29 (1-2) :159-171
[9]   Synthesis and characterization of the all-silica 8-ring Clathrasil DD3R comparison of adsorption properties with the hydrophilic zeolite A [J].
denExter, MJ ;
Jansen, JC ;
vanBekkum, H ;
Zikanova, A .
ZEOLITES, 1997, 19 (5-6) :353-358
[10]  
DENEXTER MJ, 1994, STUD SURF SCI CATAL, V84, P1159