OPTIMAL THERMAL DESIGN OF AN AUTOTHERMAL AMMONIA SYNTHESIS REACTOR

[1] APPLICATION OF THE TEMKIN KINETIC EQUATION TO AMMONIA SYNTHESIS IN LARGE-SCALE REACTORS [J]. 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]. 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]. 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]. CHEMICAL ENGINEERING SCIENCE, 1965, 20 (12) : 987 - &

[10] MURASE A, 1968, THESIS DARTMOUTH COL

[1] APPLICATION OF THE TEMKIN KINETIC EQUATION TO AMMONIA SYNTHESIS IN LARGE-SCALE REACTORS [J]. 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]. 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]. 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]. CHEMICAL ENGINEERING SCIENCE, 1965, 20 (12) : 987 - &

[10] MURASE A, 1968, THESIS DARTMOUTH COL