MODELING OF A HYDROCRACKING REACTOR

被引:50
作者
MOHANTY, S [1 ]
SARAF, DN [1 ]
KUNZRU, D [1 ]
机构
[1] INDIAN INST TECHNOL,DEPT CHEM ENGN,KANPUR 208016,UTTAR PRADESH,INDIA
关键词
D O I
10.1016/0378-3820(91)90013-3
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
A three parameter model has been developed for a two-stage vacuum gas oil hydrocracker unit. The feed and the products were lumped into 23 pseudocomponents, each characterized by its boiling range and specific gravity. The model assumes that each pseudocomponent can only form lighter products by a pseudohomogeneous first order reaction. The model parameters were determined using information from literature and plant data. Given the feed characterization and the inlet conditions, the concentration and temperature profiles throughout the reactors, the amount of recycle and hydrogen consumption can be calculated. The model was validated against plant data and the agreement was generally good. The effect of variation in the model parameters and operating conditions has also been discussed.
引用
收藏
页码:1 / 17
页数:17
相关论文
共 30 条
[1]  
EDMISTER WC, 1988, APPLIED HYDROCARBON, V2
[2]  
ELKADY FY, 1979, INDIAN J TECHNOL, V17, P176
[3]  
GERDES KF, 1977, 70TH ANN M AICHE NEW
[4]  
GOLDFARB YY, 1981, KINET KATAL, V22, P668
[5]  
JAFFE BE, 1976, IND ENG CHEM PROC DD, V15, P410
[6]  
KESLER MG, 1976, HYDROCARB PROCESS, V55, P153
[7]   USE OF AN AXIAL-DISPERSION MODEL FOR KINETIC DESCRIPTION OF HYDROCRACKING [J].
KRISHNA, R ;
SAXENA, AK .
CHEMICAL ENGINEERING SCIENCE, 1989, 44 (03) :703-712
[8]  
LANGLOIS GE, 1970, ADV CHEM SER, V9, P38
[9]   GENERALIZED THERMODYNAMIC CORRELATION BASED ON 3-PARAMETER CORRESPONDING STATES [J].
LEE, BI ;
KESLER, MG .
AICHE JOURNAL, 1975, 21 (03) :510-527
[10]  
MOHANTY S, 1989, THESIS INDIAN I TECH