EFFECT OF LIQUID MIXING ON THE PERFORMANCE OF BUBBLE TRAYS

[1] PREDICTION OF CATALYST ACTIVITY IN FLUIDIZED SYSTEMS - EMPLOYING CONSTANT CATALYST REPLACEMENT RATE [J]. INDUSTRIAL AND ENGINEERING CHEMISTRY, 1954, 46 (06): : 1296 - 1298

[2] ANDERSON JE, 1954, THESIS MASS I TECHNO

[3] BROWN JW, 1954, THESIS MASS I TECHNO

[4] THE DISTRIBUTION OF RESIDENCE-TIMES IN AN INDUSTRIAL FLUIDISED REACTOR [J]. CHEMICAL ENGINEERING SCIENCE, 1954, 3 (01) : 26 - 35

[5] CONTINUOUS FLOW SYSTEMS - DISTRIBUTION OF RESIDENCE TIMES [J]. CHEMICAL ENGINEERING SCIENCE, 1953, 2 (01) : 1 - 13

[6] DIXON BE, 1955, J APPL CHEM LONDON, V5, P390

[7] FOSS AS, 1956, CHEM ENG PROGR, V52, pJ28

[8] FOSS AS, 1957, THESIS U DELAWARE NE

[9] Gautreaux MF, 1955, CHEM ENG PROG, V51, P232

[10] GAS MIXING IN BEDS OF FLUIDIZED SOLIDS [J]. INDUSTRIAL AND ENGINEERING CHEMISTRY, 1952, 44 (01): : 218 - 224

[1] PREDICTION OF CATALYST ACTIVITY IN FLUIDIZED SYSTEMS - EMPLOYING CONSTANT CATALYST REPLACEMENT RATE [J]. INDUSTRIAL AND ENGINEERING CHEMISTRY, 1954, 46 (06): : 1296 - 1298

[2] ANDERSON JE, 1954, THESIS MASS I TECHNO

[3] BROWN JW, 1954, THESIS MASS I TECHNO

[4] THE DISTRIBUTION OF RESIDENCE-TIMES IN AN INDUSTRIAL FLUIDISED REACTOR [J]. CHEMICAL ENGINEERING SCIENCE, 1954, 3 (01) : 26 - 35

[5] CONTINUOUS FLOW SYSTEMS - DISTRIBUTION OF RESIDENCE TIMES [J]. CHEMICAL ENGINEERING SCIENCE, 1953, 2 (01) : 1 - 13

[6] DIXON BE, 1955, J APPL CHEM LONDON, V5, P390

[7] FOSS AS, 1956, CHEM ENG PROGR, V52, pJ28

[8] FOSS AS, 1957, THESIS U DELAWARE NE

[9] Gautreaux MF, 1955, CHEM ENG PROG, V51, P232

[10] GAS MIXING IN BEDS OF FLUIDIZED SOLIDS [J]. INDUSTRIAL AND ENGINEERING CHEMISTRY, 1952, 44 (01): : 218 - 224