RESIDENCE BEHAVIOUR OF GAS AND MATERIAL TRANSFER OF A BUBBLE IN A FLUIDIZED BED

[1] BAERNS M, 1963, CHEM-ING-TECH, V35, P609

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

[3] DARIES L, 1966, T I CHEM ENGR, V44, pT293

[4] Davidson J.F, 1961, TRANS INST CHEM ENG, V39, P230

[5] GAS AND SOLID MIXING IN FLUIDIZED BEDS [J]. INDUSTRIAL AND ENGINEERING CHEMISTRY, 1949, 41 (06): : 1191 - 1196

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

[7] GAS MIXING CHARACTERISTICS OF A FLUID BED REGENERATOR [J]. INDUSTRIAL AND ENGINEERING CHEMISTRY, 1957, 49 (01): : 25 - 30

[8] HANNES H, 1963, FORSCH ING WES, V29, P159

[9] MAY A, 1959, DECHEMA MONOGRAPHIEN, V32, P261

[10] ON MATHEMATICS OF FLUIDIZATION .2. STEADY MOTION OF FULLY DEVELOPED BUBBLES [J]. JOURNAL OF FLUID MECHANICS, 1965, 22 : 57 - &

[1] BAERNS M, 1963, CHEM-ING-TECH, V35, P609

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

[3] DARIES L, 1966, T I CHEM ENGR, V44, pT293

[4] Davidson J.F, 1961, TRANS INST CHEM ENG, V39, P230

[5] GAS AND SOLID MIXING IN FLUIDIZED BEDS [J]. INDUSTRIAL AND ENGINEERING CHEMISTRY, 1949, 41 (06): : 1191 - 1196

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

[7] GAS MIXING CHARACTERISTICS OF A FLUID BED REGENERATOR [J]. INDUSTRIAL AND ENGINEERING CHEMISTRY, 1957, 49 (01): : 25 - 30

[8] HANNES H, 1963, FORSCH ING WES, V29, P159

[9] MAY A, 1959, DECHEMA MONOGRAPHIEN, V32, P261

[10] ON MATHEMATICS OF FLUIDIZATION .2. STEADY MOTION OF FULLY DEVELOPED BUBBLES [J]. JOURNAL OF FLUID MECHANICS, 1965, 22 : 57 - &