THE INFLUENCE OF INITIAL COKE PROFILE AND HYDROGEN CONTENT OF COKE ON THE REGENERATION OF FIXED-BEDS OF CATALYST

被引:22
作者
BYRNE, A
HUGHES, R
SANTAMARIARAMIRO, J
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D O I
10.1016/0009-2509(85)80092-0
中图分类号
TQ [化学工业];
学科分类号
0817 ;
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页码:1507 / 1516
页数:10
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共 16 条
[1]   SIMPLE METHOD FOR APPROXIMATING ACTIVITY PROFILES IN A DEACTIVATING ADIABATIC REACTOR [J].
BRITOALAYON, A ;
HUGHES, R ;
KAM, EKT .
INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS, 1981, 20 (04) :399-403
[2]  
DART JC, 1949, CHEM ENG PROG, V45, P102
[3]   NON-STEADY STATE BEHAVIOUR OF FIXED BED CATALYTIC REACTORS DUE TO CATALYST FOULING [J].
FROMENT, GF ;
BISCHOFF, KB .
CHEMICAL ENGINEERING SCIENCE, 1961, 16 (3-4) :189-201
[4]   A MULTIPLE-REACTION MODEL FOR BURNING REGENERATION OF COKED CATALYSTS [J].
HASHIMOTO, K ;
TAKATANI, K ;
IWASA, H ;
MASUDA, T .
CHEMICAL ENGINEERING JOURNAL AND THE BIOCHEMICAL ENGINEERING JOURNAL, 1983, 27 (03) :177-186
[5]  
HUGHES R, 1970, J APPL CHEM BIOTECHN, V21, P35
[6]   TEMPERATURE PROFILES IN PACKED BEDS OF CATALYST DURING REGENERATION [J].
JOHNSON, BM ;
FROMENT, GF ;
WATSON, CC .
CHEMICAL ENGINEERING SCIENCE, 1962, 17 (11) :835-&
[7]   OXIDATION OF COKED SILICA-ALUMINA CATALYST [J].
MASSOTH, FE .
INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1967, 6 (02) :200-&
[8]  
NASCIMENTO C, 1982, THESIS SALFORD U
[9]   REGENERATION OF ADIABACTIC FIXED BEDS [J].
OLSON, KE ;
LUSS, D ;
AMUNDSON, NR .
INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1968, 7 (01) :96-&
[10]   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-&