ON THE ESTIMATION OF AVERAGE SHEAR RATE IN BUBBLE-COLUMNS

[1] AKITA K, 1972, THESIS KYOTO U

[2] ON THE CALCULATION OF SHEAR RATE AND APPARENT VISCOSITY IN AIRLIFT AND BUBBLE COLUMN BIOREACTORS [J]. BIOTECHNOLOGY AND BIOENGINEERING, 1989, 34 (11) : 1391 - 1392

[3] KATO Y, 1962, KAGAKU KOGAKU, V26, P1068

[4] GAS-ABSORPTION IN A MULTISTAGE GAS-LIQUID SPOUTED VESSEL [J]. JOURNAL OF CHEMICAL ENGINEERING OF JAPAN, 1985, 18 (06) : 496 - 501

[5] HEAT-TRANSFER IN AERATED TOWER FILLED WITH NON-NEWTONIAN LIQUID [J]. INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1977, 16 (01): : 133 - 137

[6] Nishikawa M, 1976, J CHEM ENG JAPAN, V9, P214

[7] GAS HOLD-UP AND AXIAL MIXING IN FLUID PHASE OF BUBBLE COLUMNS [J]. CHEMICAL ENGINEERING SCIENCE, 1968, 23 (06) : 619 - &

[8] STEIN N, 1954, CHEM ING TECHN, V26, P614

[9] YOSHITOME H, 1963, KAGAKU KOGAKU, V27, P27

[1] AKITA K, 1972, THESIS KYOTO U

[2] ON THE CALCULATION OF SHEAR RATE AND APPARENT VISCOSITY IN AIRLIFT AND BUBBLE COLUMN BIOREACTORS [J]. BIOTECHNOLOGY AND BIOENGINEERING, 1989, 34 (11) : 1391 - 1392

[3] KATO Y, 1962, KAGAKU KOGAKU, V26, P1068

[4] GAS-ABSORPTION IN A MULTISTAGE GAS-LIQUID SPOUTED VESSEL [J]. JOURNAL OF CHEMICAL ENGINEERING OF JAPAN, 1985, 18 (06) : 496 - 501

[5] HEAT-TRANSFER IN AERATED TOWER FILLED WITH NON-NEWTONIAN LIQUID [J]. INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1977, 16 (01): : 133 - 137

[6] Nishikawa M, 1976, J CHEM ENG JAPAN, V9, P214

[7] GAS HOLD-UP AND AXIAL MIXING IN FLUID PHASE OF BUBBLE COLUMNS [J]. CHEMICAL ENGINEERING SCIENCE, 1968, 23 (06) : 619 - &

[8] STEIN N, 1954, CHEM ING TECHN, V26, P614

[9] YOSHITOME H, 1963, KAGAKU KOGAKU, V27, P27