REGENERATION OF COKED CATALYST BEDS WITH KNOWN AXIAL COKE PROFILES

被引：8

作者：

BYRNE, A ^{[1
]}

DAKESSIAN, V ^{[1
]}

HUGHES, R ^{[1
]}

SANTAMARIARAMIRO, J ^{[1
]}

机构：

[1] UNIV SALFORD,DEPT CHEM ENGN,SALFORD M5 4WT,LANCS,ENGLAND

来源：

CHEMICAL ENGINEERING COMMUNICATIONS | 1986年 / 44卷 / 1-6期

关键词：

D O I：

10.1080/00986448608911352

中图分类号：

TQ [化学工业];

学科分类号：

0817 ;

摘要：

引用

页码：153 / 162

页数：10

共 10 条

[1] THE INFLUENCE OF INITIAL COKE PROFILE AND HYDROGEN CONTENT OF COKE ON THE REGENERATION OF FIXED-BEDS OF CATALYST [J].

BYRNE, A ;

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SANTAMARIARAMIRO, J .

CHEMICAL ENGINEERING SCIENCE, 1985, 40 (08) :1507-1516

[2] DETERMINATION OF COKE PROFILES IN FIXED-BED CATALYTIC REACTORS BY A NEUTRON ATTENUATION TECHNIQUE [J].

BYRNE, A ;

DAKESSIAN, V ;

HUGHES, R ;

SANTAMARIARAMIRO, J ;

WRIGHT, CJ .

JOURNAL OF CATALYSIS, 1985, 96 (01) :146-153

[3]

BYRNE A, 1984, ANN RES M I CHEM ENG

[4] TEMPERATURE PROFILES IN PACKED BEDS OF CATALYST DURING REGENERATION [J].

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FROMENT, GF ;

WATSON, CC .

CHEMICAL ENGINEERING SCIENCE, 1962, 17 (11) :835-&

[5] TEMPERATURE PROFILES IN A RAPIDLY FOULING CATALYST BED [J].

MENON, PG ;

SREERAMA.R .

JOURNAL OF CATALYSIS, 1967, 8 (01) :95-&

[6] REGENERATION OF ADIABACTIC FIXED BEDS [J].

OLSON, KE ;

LUSS, D ;

AMUNDSON, NR .

INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1968, 7 (01) :96-&

[7] REGENERATION OF COKED CATALYST IN ADIABATIC FIXED BEDS AT LOWER TEMPERATURES [J].

OZAWA, Y .

INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1969, 8 (03) :378-&

[8]

Schulman B., 1963, IND ENG CHEM, V55, P44

[9]

TAKAHASHI T, 1978, J JPN PET I, V21, P85

[10] HEAT AND MASS TRANSPORT IN A FIXED CATALYST BED DURING REGENERATION [J].

VANDEEMTER, JJ .

INDUSTRIAL AND ENGINEERING CHEMISTRY, 1953, 45 (06) :1227-1233

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