KINETICS ASSISTED DESIGN OF CATALYSTS

被引：9

作者：

Boudart, M. ^{[1
]}

机构：

[1] Stanford Univ, Dept Chem Engn, Stanford, CA 94305 USA

来源：

CATALYSIS LETTERS | 1988年 / 1卷 / 1-3期

基金：

美国国家科学基金会;

关键词：

D O I：

10.1007/BF00765349

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：

Whether thermokinetic data obtained on model large single crystals at low surface coverage can be used successfully to calculate yields on real catalysts at high surface coverage is a question that is considered in the conjecture presented in this note.

引用

页码：21 / 25

页数：5

共 15 条

[1]

Aris R., 1987, CATALYST DESIGN PROG

[2] CLASSICAL CATALYTIC KINETICS - A PLACEBO OR THE REAL THING [J].

BOUDART, M .

INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS, 1986, 25 (04) :656-658

[3]

BOUDART M, 1986, CHEMTECH, P688

[4]

Boudart M., 1984, KINETICS HETEROGENEO

[5]

Boudart M., 1954, IND CHIMIQUE BELGE, V19, P489

[6]

Boudart M., REACTION KI IN PRESS

[7] EXTRAPOLATION OF THE KINETICS OF MODEL AMMONIA-SYNTHESIS CATALYSTS TO INDUSTRIALLY RELEVANT TEMPERATURES AND PRESSURES [J].

BOWKER, M ;

PARKER, IB ;

WAUGH, KC .

APPLIED CATALYSIS, 1985, 14 (1-3) :101-118

[8] A KINETIC MODELING APPROACH TO THE DESIGN OF CATALYSTS - FORMULATION OF A CATALYST DESIGN ADVISORY PROGRAM [J].

DUMESIC, JA ;

MILLIGAN, BA ;

GREPPI, LA ;

BALSE, VR ;

SARNOWSKI, KT ;

BEALL, CE ;

KATAOKA, T ;

RUDD, DF ;

TREVINO, AA .

INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1987, 26 (07) :1399-1407

[9]

ERTL G, 1983, CATALYSIS SCI TECHNO, V4, P209

[10] COMPARATIVE KINETIC-STUDIES OF CO-O2 AND CO-NO REACTIONS OVER SINGLE-CRYSTAL AND SUPPORTED RHODIUM CATALYSTS [J].

OH, SH ;

FISHER, GB ;

CARPENTER, JE ;

GOODMAN, DW .

JOURNAL OF CATALYSIS, 1986, 100 (02) :360-376

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