OPTIMAL OPERATION OF A CATALYTIC TUBULAR REACTOR WITH FOULING CATALYST BY COKE DEPOSITION

被引：3

作者：

NODA, H ^{[1
]}

KANEHARA, S ^{[1
]}

TONE, S ^{[1
]}

OTAKE, T ^{[1
]}

机构：

[1] OSAKA UNIV, DEPT CHEM ENGN, TOYONAKA, OSAKA, JAPAN

来源：

关键词：

D O I：

10.1016/0009-2509(75)80053-4

中图分类号：

TQ [化学工业];

学科分类号：

0817 ;

摘要：

引用

页码：887 / 892

页数：6

共 21 条

[1]

BINNS DR, 1969, TRANS INST CHEM ENG, V47, pT53

[2]

CAMPBELL DR, 1970, CAN J CHEM ENGNG, V48, P576

[3]

CHOU A, 1967, TRANS INST CHEM ENG, V45, pT153

FROMENT, GF ;

BISCHOFF, KB .

[5] ESTIMATION OF CATALYST ACTIVITY PROFILES IN FIXED BED REACTORS [J].

GAVALAS, GR ;

SEINFELD, JH ;

HSU, GC .

[6]

GAVALAS GR, 1972, CHEM ENG J, V4, P77

[7]

HANO J, 1972, KAGAKU KOGAKU, V36, P1230

[8]

HEINEMANN H, 1969, CATALYST REV, V2

[9]

JACKSON R, 1967, TRANS INST CHEM ENG, V45, pT160

[10]

Kirk D.E., 2004, OPTIMAL CONTROL THEO