Zeolite Membranes in Catalysis-From Separate Units to Particle Coatings

被引:33
作者
Dragomirova, Radostina [1 ]
Wohlrab, Sebastian [1 ]
机构
[1] Univ Rostock, Leibniz Inst Catalysis, LIKAT Rostock, D-18059 Rostock, Germany
来源
CATALYSTS | 2015年 / 5卷 / 04期
关键词
membrane reactor; permselectivity; permselective zeolite membrane; zeolite membrane reactor; packed bed membrane reactor; catalytic membrane reactor; zeolite membrane coating; zeolite capsuled catalyst; equilibrium shift; FISCHER-TROPSCH SYNTHESIS; ORIENTED MFI MEMBRANES; MAXWELL-STEFAN DESCRIPTION; GAS PERMEATION PROPERTIES; IN-SITU CRYSTALLIZATION; M-XYLENE ISOMERIZATION; PHASE TRANSPORT METHOD; FREE SECONDARY GROWTH; MIDDLE ISO-PARAFFINS; N-BUTANE OXIDATION;
D O I
10.3390/catal5042161
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
Literature on zeolite membranes in catalytic reactions is reviewed and categorized according to membrane location. From this perspective, the classification is as follows: (i) membranes spatially decoupled from the reaction zone; (ii) packed bed membrane reactors; (iii) catalytic membrane reactors and (iv) zeolite capsuled catalyst particles. Each of the resulting four chapters is subdivided by the kind of reactions performed. Over the whole sum of references, the advantage of zeolite membranes in catalytic reactions in terms of conversion, selectivity or yield is evident. Furthermore, zeolite membrane preparation, separation principles as well as basic considerations on membrane reactors are discussed.
引用
收藏
页码:2161 / 2222
页数:62
相关论文
共 296 条
  • [91] On the preferred orientation and microstructural manipulation of molecular sieve films prepared by secondary growth
    Gouzinis, A
    Tsapatsis, M
    [J]. CHEMISTRY OF MATERIALS, 1998, 10 (09) : 2497 - 2504
  • [92] On-stream modification of MFI zeolite membranes for enhancing hydrogen separation at high temperature
    Gu, Xuehong
    Tang, Zhong
    Dong, Junhang
    [J]. MICROPOROUS AND MESOPOROUS MATERIALS, 2008, 111 (1-3) : 441 - 448
  • [93] Separation of p-xylene from multicomponent vapor mixtures using tubular MFI zeolite mmbranes
    Gu, Xuehong
    Dong, Junhang
    Nenoff, Tina M.
    Ozokwelu, Dickson E.
    [J]. JOURNAL OF MEMBRANE SCIENCE, 2006, 280 (1-2) : 624 - 633
  • [94] Synthesis of FAU-type zeolite membrane: An original in situ process focusing on the rheological control of gel-like precursor species
    Guillou, Florent
    Rouleau, Loic
    Pirngruber, Gerhard
    Valtchev, Valentin
    [J]. MICROPOROUS AND MESOPOROUS MATERIALS, 2009, 119 (1-3) : 1 - 8
  • [95] Aromatic permeation through crystalline molecular sieve membranes
    Gump, CJ
    Tuan, VA
    Noble, RD
    Falconer, JL
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2001, 40 (02) : 565 - 577
  • [96] On the use of a catalytic H-ZSM-5 membrane for xylene isomerization
    Haag, Stephane
    Hanebuth, Marc
    Mabande, Godwin T. P.
    Avhale, Abhijeet
    Schwieger, Wilhelm
    Dittmeyer, Roland
    [J]. MICROPOROUS AND MESOPOROUS MATERIALS, 2006, 96 (1-3) : 168 - 176
  • [97] Application of a CHA-type zeolite membrane to the esterification of adipic acid with isopropyl alcohol using sulfuric acid catalyst
    Hasegawa, Y.
    Abe, C.
    Mizukami, F.
    Kowata, Y.
    Hanaoka, T.
    [J]. JOURNAL OF MEMBRANE SCIENCE, 2012, 415 : 368 - 374
  • [98] Influence of acid on the permeation properties of NaA-type zeolite membranes
    Hasegawa, Y.
    Nagase, T.
    Kiyozumi, Y.
    Hanaoka, T.
    Mizukami, F.
    [J]. JOURNAL OF MEMBRANE SCIENCE, 2010, 349 (1-2) : 189 - 194
  • [99] Multiple-functional capsule catalysts: A tailor-made confined reaction environment for the direct synthesis of middle isoparaffins from syngas
    He, Jingjiang
    Liu, Zhenlin
    Yoneyama, Yoshiharu
    Nishiyama, Norikazu
    Tsubaki, Noritatsu
    [J]. CHEMISTRY-A EUROPEAN JOURNAL, 2006, 12 (32) : 8296 - 8304
  • [100] Designing a capsule catalyst and its application for direct synthesis of middle isoparaffins
    He, JJ
    Yoneyama, Y
    Xu, BL
    Nishiyama, N
    Tsubaki, N
    [J]. LANGMUIR, 2005, 21 (05) : 1699 - 1702