REACTOR SCALE-UP FOR POLYMERIZATION IN SUSPENSION

[1] EFFECTIVE INTERFACIAL AREA IN AGITATED LIQUID-LIQUID CONTACTORS [J]. CHEMICAL ENGINEERING SCIENCE, 1967, 22 (10) : 1267 - &

[2] HEDDEN H, 1970, CHEM ING TECHN, V42, P475

[3] HOPFF H, 1964, CHEM-ING-TECH, V36, P1085

[4] PARTICLE-SIZE OF SUSPENSION POLYMERS .2. PHASE POLYMERIZATION SYSTEMS [J]. CHEMIE INGENIEUR TECHNIK, 1979, 51 (07) : 746 - 747

[5] DESIGN AND SCALE-UP OF AGITATORS [J]. CHEMIE INGENIEUR TECHNIK, 1975, 47 (23) : 953 - 964

[6] PARTICLE-SIZE OF SUSPENSION POLYMERS .1. NON-POLYMERIZING 2-PHASE SYSTEMS [J]. CHEMIE INGENIEUR TECHNIK, 1978, 50 (09) : 710 - 711

[7] MINIMUM IMPELLER SPEEDS FOR LIQUID-LIQUID DISPERSION IN BAFFLED VESSELS [J]. INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1978, 17 (01): : 56 - 61

[1] EFFECTIVE INTERFACIAL AREA IN AGITATED LIQUID-LIQUID CONTACTORS [J]. CHEMICAL ENGINEERING SCIENCE, 1967, 22 (10) : 1267 - &

[2] HEDDEN H, 1970, CHEM ING TECHN, V42, P475

[3] HOPFF H, 1964, CHEM-ING-TECH, V36, P1085

[4] PARTICLE-SIZE OF SUSPENSION POLYMERS .2. PHASE POLYMERIZATION SYSTEMS [J]. CHEMIE INGENIEUR TECHNIK, 1979, 51 (07) : 746 - 747

[5] DESIGN AND SCALE-UP OF AGITATORS [J]. CHEMIE INGENIEUR TECHNIK, 1975, 47 (23) : 953 - 964

[6] PARTICLE-SIZE OF SUSPENSION POLYMERS .1. NON-POLYMERIZING 2-PHASE SYSTEMS [J]. CHEMIE INGENIEUR TECHNIK, 1978, 50 (09) : 710 - 711

[7] MINIMUM IMPELLER SPEEDS FOR LIQUID-LIQUID DISPERSION IN BAFFLED VESSELS [J]. INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1978, 17 (01): : 56 - 61