METHANATION OF LOW-CONCENTRATION CARBON MONOXIDE FEEDS OVER RUTHENIUM

被引:19
作者
RANDHAVA, SS
REHMAT, A
CAMARA, EH
机构
[1] Institute of Gas Technology, Chicago
来源
INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT | 1969年 / 8卷 / 04期
关键词
D O I
10.1021/i260032a008
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The methanation of carbon monoxide at parts per million levels was studied over 0.5% ruthenium metal catalyst, dispersed on alumina catalyst in a fixed-bed reactor. Gas mixtures of 3450, 1090, and 505 p.p.m. carbon monoxide in hydrogen were used. The rate of reaction of carbon monoxide follows simple pseudo-first-order kinetics. The rate constant follows the Arrhenius temperature dependence at low temperatures. Evidence of diffusion control of the reaction rate was found in the higher temperature regions investigated. © 1969, American Chemical Society. All rights reserved.
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页码:482 / &
相关论文
共 9 条
[1]  
AKERS WW, 1948, CHEM ENG PROGR, V44, P554
[2]   CATALYTIC COMBUSTION OF CYCLOHEXANE CYCLOHEXENE AND BENZENE . CHEMICAL AND TRANSPORT KINETICS [J].
CARETTO, LS ;
NOBE, K .
INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1966, 5 (03) :217-&
[3]   CATALYTIC COMBUSION OF CARBON MONOXIDE ON COPPER OXIDE . EFFECT OF WATER VAPOR [J].
COHEN, AE ;
NOBE, K .
INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1966, 5 (03) :214-&
[4]  
DIRKSEN HA, 1963, 31 I GAS TECHN RES B
[5]   SYNTHESIS OF METHANE - BY HYDROGENATION OF CARBON MONOXIDE IN A TUBULAR REACTOR [J].
GILKESON, MM ;
WHITE, RR ;
SLIEPCEVICH, CM .
INDUSTRIAL AND ENGINEERING CHEMISTRY, 1953, 45 (02) :460-467
[6]   HYDROGENATION OF CARBON MONOXIDE AND CARBON DIOXIDE ON SUPPORTED RUTHENIUM CATALYSTS AT MODERATE PRESSURES [J].
KARN, FS ;
SHULTZ, JF ;
ANDERSON, RB .
INDUSTRIAL & ENGINEERING CHEMISTRY PRODUCT RESEARCH AND DEVELOPMENT, 1965, 4 (04) :265-&
[7]  
Levenspid O, 1962, CHEMICAL REACTION EN
[8]  
MCKEE DWJ, 1967, CATALYSIS, V8, P240
[9]  
Nicolai J., 1946, Bull. Soc. Chim. Belg, V55, P160