DEACTIVATION OF A PLATINUM REFORMING CATALYST IN A TUBULAR REACTOR

被引：63

作者：

DEPAUW, RP ^{[1
]}

FROMENT, GF ^{[1
]}

机构：

[1] RIJKS UNIV GHENT,LAB PETRACHEM TECH,GHENT,BELGIUM

来源：

关键词：

D O I：

10.1016/0009-2509(75)80043-1

中图分类号：

TQ [化学工业];

学科分类号：

0817 ;

摘要：

引用

页码：789 / 801

页数：13

共 10 条

[1] BAYESIAN ESTIMATION OF COMMON PARAMETERS FROM SEVERAL RESPONSES
BOX, GEP
DRAPER, NR
[J]. BIOMETRIKA, 1965, 52 : 355 - &
[2] BUTT JB, 1972, ADV CHEM SER, P259
[3] NON-STEADY STATE BEHAVIOUR OF FIXED BED CATALYTIC REACTORS DUE TO CATALYST FOULING
FROMENT, GF
BISCHOFF, KB
[J]. CHEMICAL ENGINEERING SCIENCE, 1961, 16 (3-4) : 189 - 201
[4] HOSTEN LH, 1971, IND ENG CHEM P DES D, V10, P2
[5] JOHN TM, 1974, ADV CHEM SERIES, P133
[6] LAMBRECHT GC, 1972, 5TH P EUR S CHEM REA
[7] KINETICS OF NORMAL-PENTANE ISOMERIZATION OVER PT-AL2O3 CATALYST
SINFELT, JH
HURWITZ, H
ROHRER, JC
[J]. JOURNAL OF PHYSICAL CHEMISTRY, 1960, 64 (07) : 892 - 894
[8] VANDENBOSSCHE B, 1974, AICHE J, V20, P251
[9] CARBON FORMATION IN CATALYTIC CRACKING
VOORHIES, A
[J]. INDUSTRIAL AND ENGINEERING CHEMISTRY, 1945, 37 (04): : 318 - 322
[10] A MODEL OF CATALYTIC CRACKING CONVERSION IN FIXED MOVING AND FLUID-BED REACTORS
WEEKMAN, VW
[J]. INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1968, 7 (01): : 90 - &