Model for the performance of a fluid catalytic cracking (FCC) riser reactor: effect of feed atomization

被引：64

作者：

Gupta, A ^{[1
]}

Rao, DS ^{[1
]}

机构：

[1] Indian Inst Technol, Dept Chem Engn, Delhi, India

来源：

CHEMICAL ENGINEERING SCIENCE | 2001年 / 56卷 / 15期

关键词：

reaction engineering; fluid catalytic cracking; feed atomization; vaporization; selectivity; simulation;

D O I：

10.1016/S0009-2509(01)00122-1

中图分类号：

TQ [化学工业];

学科分类号：

0817 ;

摘要：

A model for predicting conversions and yield patterns in FCC riser reactor is developed considering heat transfer, gas oil vaporization, catalyst entrainment hydrodynamics, mass transfer, catalytic cracking kinetics and deactivation. The effect of the initial average droplet size generated by feed atomization nozzle on conversion and yield pattern is discussed. (C) 2001 Elsevier Science Ltd. All rights reserved.

引用

页码：4489 / 4503

页数：15

共 26 条

[1] Modelling and control of a riser type fluid catalytic cracking (FCC) unit [J].