OPTIMUM QUENCH LOCATION FOR A HYDRODESULFURIZATION REACTOR WITH TIME-VARYING CATALYST ACTIVITY

被引：23

作者：

SHAH, YT

MHASKAR, RD

PARASKOS, JA

机构：

[1] UNIV PITTSBURGH,DEPT CHEM ENGN,PITTSBURGH,PA 15261

[2] GULF RES & DEV CO,PITTSBURGH,PA 15230

来源：

INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT | 1976年 / 15卷 / 03期

关键词：

D O I：

10.1021/i260059a009

中图分类号：

TQ [化学工业];

学科分类号：

0817 ;

摘要：

引用

页码：400 / 406

页数：7

共 10 条

[1] BEUTHER H, 1963, 6TH WORLD PETR C
[2] BRIDGE AG, 1975, HYDROCARB PROCESS, V54, P74
[3] Carnahan B., 1969, APPL NUMERICAL METHO
[4] MICKLEY HS, 1957, APPLIED MATHEMATICS
[5] CATALYST DEACTIVATION DUE TO PORE-PLUGGING BY REACTION-PRODUCTS
NEWSON, E
[J]. INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1975, 14 (01): : 27 - 33
[6] EFFECT OF HOLDUP INCOMPLETE CATALYST WETTING AND BACKMIXING DURING HYDROPROCESSING IN TRICKLE BED REACTORS
PARASKOS, JA
FRAYER, JA
SHAH, YT
[J]. INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1975, 14 (03): : 315 - 322
[7] PARASKOS JA, 1974, 67TH ANN M AICHE WAS
[8] PARASKOS JA, 1973, Patent No. 3746636
[9] CRITERIA FOR AXIAL DISPERSION EFFECTS IN ADIABATIC TRICKLE BED HYDROPROCESSING REACTORS
SHAH, YT
PARASKOS, JA
[J]. CHEMICAL ENGINEERING SCIENCE, 1975, 30 (09) : 1169 - 1176
[10] [No title captured]