OPTIMAL THERMAL DESIGN OF AN AUTOTHERMAL AMMONIA SYNTHESIS REACTOR

被引：35
作者：
MURASE, A
ROBERTS, HL
CONVERSE, AO
机构：
来源：
INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT | 1970年 / 9卷 / 04期
关键词：
D O I：
10.1021/i260036a003
中图分类号：
TQ [化学工业];
学科分类号：
0817 ;
摘要：
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页码：503 / &
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共 17 条
[1]   APPLICATION OF THE TEMKIN KINETIC EQUATION TO AMMONIA SYNTHESIS IN LARGE-SCALE REACTORS [J].
ANNABLE, D .
CHEMICAL ENGINEERING SCIENCE, 1952, 1 (04) :145-164
[2]  
ARIES RS, 1955, CHEMICAL ENGINEERING, P16
[3]   STEADY-STATE SIMULATION OF AN AMMONIA SYNTHESIS CONVERTER [J].
BADDOUR, RF ;
BRAIN, PLT ;
LOGEAIS, BA ;
EYMERY, JP .
CHEMICAL ENGINEERING SCIENCE, 1965, 20 (04) :281-&
[4]  
CHILTON CH, 1960, COST ENGINEERING PRO, P113
[5]  
CONVERSE AO, 1970, OPTIMIZATION, P174
[6]   Velocity and yield in continuous reaction systems. [J].
Denbigh, KG .
TRANSACTIONS OF THE FARADAY SOCIETY, 1944, 40 :0352-0373
[7]  
DYSON DC, 1965, THESIS LONDON U
[8]  
EYMERY JP, 1964, THESIS MIT
[9]   PROCESS OPTIMIZATION AT DESIGN STAGE WITH AM OBJESTIVE FUNCTION LINEAR IN PROFIT AND INVESTMENT [J].
MCEWAN, MW ;
BEVERIDG.GS .
CHEMICAL ENGINEERING SCIENCE, 1965, 20 (12) :987-&
[10]  
MURASE A, 1968, THESIS DARTMOUTH COL
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