KINETIC-STUDY OF PYROLYSIS GASOLINE HYDROGENATION OVER SUPPORTED PALLADIUM CATALYST

被引：44

作者：

CHENG, YM

CHANG, JR

WU, JC

机构：

来源：

APPLIED CATALYSIS | 1986年 / 24卷 / 1-2期

关键词：

D O I：

10.1016/S0166-9834(00)81275-0

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：

引用

页码：273 / 285

页数：13

共 13 条

[1]

BOITIAUX JP, 1982, 3RD INT S

[2] THE SORPTION OF HYDROGEN ON PALLADIUM IN A FLOW SYSTEM [J].

CHEN, G ;

CHOU, WT ;

YEH, CT .

APPLIED CATALYSIS, 1983, 8 (03) :389-397

[3] DETERMINATION OF RATE CONSTANTS FOR COMPLEX KINETICS MODELS [J].

HIMMELBLAU, DM ;

JONES, CR ;

BISCHOFF, KB .

INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS, 1967, 6 (04) :539-+

[4]

KRONIG W, 1970, MAR HYDR P, P121

[5] DIAGNOSTIC CRITERIA FOR HEAT TRANSPORT LIMITATIONS IN FIXED BED REACTORS [J].

MEARS, DE .

JOURNAL OF CATALYSIS, 1971, 20 (02) :127-&

[6] TESTS FOR TRANSPORT LIMITATIONS IN EXPERIMENTAL CATALYTIC REACTORS [J].

MEARS, DE .

INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1971, 10 (04) :541-&

[7] A MATHEMATICAL-MODEL FOR A TUBULAR REACTOR PERFORMING ETHYLENE OXIDATION TO ETHYLENE-OXIDE BY A CATALYST DEPOSITED ON METALLIC STRIPS [J].

RAGAINI, V ;

DELUCA, G ;

FERRARIO, B ;

DELLAPORTA, P .

CHEMICAL ENGINEERING SCIENCE, 1980, 35 (11) :2311-2319

[8] UPFLOW REACTOR FOR THE SELECTIVE HYDROGENATION OF PYROLYSIS GASOLINE A COMPARATIVE-STUDY WITH RESPECT TO DOWNFLOW [J].

RAGAINI, V ;

TINE, C .

APPLIED CATALYSIS, 1984, 10 (01) :43-51

[9]

SZE MC, 1969, CHEM ENG PROG FEB, P59

[10] UNIFORMITY OF SUPPORTED CUO FROM RATE OF REDUCTION WITH HYDROGEN [J].

VOGE, HH ;

ATKINS, LT .

JOURNAL OF CATALYSIS, 1962, 1 (02) :171-179

← 1 2 →