A THEORETICAL-MODEL FOR PARTICLE SEGREGATION IN A FLUIDIZED-BED DUE TO SIZE DIFFERENCE

[1] PARTICLE SEGREGATION IN A FLUIDIZED-BED [J]. CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1975, 53 (04) : 395 - 402

[2] MODEL FOR A SEGREGATING GAS FLUIDIZED-BED [J]. CHEMICAL ENGINEERING SCIENCE, 1974, 29 (06) : 1403 - 1412

[3] Kunii D, 1991, FLUIDIZATION ENG, V2nd, DOI 10.1016/C2009-0-24190-0

[4] MATHESON GL, 1949, IND ENG CHEM, V41, P1099

[5] ROWE PN, 1972, TRANS INST CHEM ENG, V50, P310

[6] ROWE PN, 1972, TRANS INST CHEM ENG, V50, P324

[7] SHANNON PT, 1959, THESIS IIT CHICAGO

[8] TRAWINSKI H, 1953, CHEM ENG TECH, V254, P201

[9] TRAWINSKI H, 1951, CHEM ING TECHN, V23, P416

[10] Wen C.Y., 1966, FLUID PART TECHNOL C, V62, P100, DOI DOI 10.1016/S0032-0633(98)00014-2

[1] PARTICLE SEGREGATION IN A FLUIDIZED-BED [J]. CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1975, 53 (04) : 395 - 402

[2] MODEL FOR A SEGREGATING GAS FLUIDIZED-BED [J]. CHEMICAL ENGINEERING SCIENCE, 1974, 29 (06) : 1403 - 1412

[3] Kunii D, 1991, FLUIDIZATION ENG, V2nd, DOI 10.1016/C2009-0-24190-0

[4] MATHESON GL, 1949, IND ENG CHEM, V41, P1099

[5] ROWE PN, 1972, TRANS INST CHEM ENG, V50, P310

[6] ROWE PN, 1972, TRANS INST CHEM ENG, V50, P324

[7] SHANNON PT, 1959, THESIS IIT CHICAGO

[8] TRAWINSKI H, 1953, CHEM ENG TECH, V254, P201

[9] TRAWINSKI H, 1951, CHEM ING TECHN, V23, P416

[10] Wen C.Y., 1966, FLUID PART TECHNOL C, V62, P100, DOI DOI 10.1016/S0032-0633(98)00014-2