REACTOR INTERNAL CONTINUOUS HEAT TRANSFER PROCESS FOR SO2 CONVERSION SYSTEM (Ⅱ) SYNTHESIS OPTIMAL ANALYSIS
|更新时间:2025-12-10
|
REACTOR INTERNAL CONTINUOUS HEAT TRANSFER PROCESS FOR SO2 CONVERSION SYSTEM (Ⅱ) SYNTHESIS OPTIMAL ANALYSIS
CIESC JournalIssue 6, (2002)
作者机构:
华南理工大学教育部强化传热与过程节能重点实验室
作者简介:
基金信息:
DOI:
CLC:
Online First:25 June 2002,
Published:25 June 2002
稿件说明:
移动端阅览
ZHANG Yajun, DENG Xianhe, XING Huawei. REACTOR INTERNAL CONTINUOUS HEAT TRANSFER PROCESS FOR SO2 CONVERSION SYSTEM (Ⅱ) SYNTHESIS OPTIMAL ANALYSIS[J]. CIESC Journal, 2002, (6).
DOI:
ZHANG Yajun, DENG Xianhe, XING Huawei. REACTOR INTERNAL CONTINUOUS HEAT TRANSFER PROCESS FOR SO2 CONVERSION SYSTEM (Ⅱ) SYNTHESIS OPTIMAL ANALYSIS[J]. CIESC Journal, 2002, (6).DOI:
REACTOR INTERNAL CONTINUOUS HEAT TRANSFER PROCESS FOR SO2 CONVERSION SYSTEM (Ⅱ) SYNTHESIS OPTIMAL ANALYSIS
摘要
Abstract
In order to overcome the many shortcomings of the traditional conversion system
this paper proposes a new kind of continued heat transfer conversion system.The new system is in accordance with the advances of contemporary chemical engineering because it makes the equipment smaller. In addition
an optimal research on this new system is made and the optimal results under the three kinds of different objective function are obtained. Three kinds of different objective functions are minimum catalyst amount( R 1)
minimum total equipment investment ( R 2)
minimum total equipment investment and operation expense per year ( R 3).