PRECISE EXPERIMENTATION IN HETEROGENEOUS CATALYSIS

[1] CHU JC, 1953, CHEM ENGNG PROG, V49, P141

[2] DOW WM, 1951, CHEM ENG PROG, V47, P637

[3] Gamson BW, 1943, T AM INST CHEM ENG, V39, P0001

[4] THE PARTIAL COEFFICIENT OF HEAT TRANSFER IN A DRYING FLUIDIZED BED [J]. CHEMICAL ENGINEERING SCIENCE, 1956, 5 (04) : 161 - 167

[5] HOUGEN OA, 1953, CHEM PROCESS PRINC 3, P973

[6] Jacob A., 1957, CAN J CHEM ENG, V35, P5

[7] HEAT TRANSFER TO GASES THROUGH PACKED TUBES - GENERAL CORRELATION FOR SMOOTH SPHERICAL PARTICLES [J]. INDUSTRIAL AND ENGINEERING CHEMISTRY, 1947, 39 (07): : 857 - 862

[8] HEAT TRANSFER CHARACTERISTICS OF FLUIDIZED BEDS [J]. INDUSTRIAL AND ENGINEERING CHEMISTRY, 1949, 41 (06): : 1135 - 1147

[9] AN IMPROVED EXPERIMENTAL REACTOR FOR APPLIED KINETIC STUDIES [J]. AICHE JOURNAL, 1958, 4 (03) : 351 - 355

[10] POZZI AL, 1961, THESIS U TEXAS

[1] CHU JC, 1953, CHEM ENGNG PROG, V49, P141

[2] DOW WM, 1951, CHEM ENG PROG, V47, P637

[3] Gamson BW, 1943, T AM INST CHEM ENG, V39, P0001

[4] THE PARTIAL COEFFICIENT OF HEAT TRANSFER IN A DRYING FLUIDIZED BED [J]. CHEMICAL ENGINEERING SCIENCE, 1956, 5 (04) : 161 - 167

[5] HOUGEN OA, 1953, CHEM PROCESS PRINC 3, P973

[6] Jacob A., 1957, CAN J CHEM ENG, V35, P5

[7] HEAT TRANSFER TO GASES THROUGH PACKED TUBES - GENERAL CORRELATION FOR SMOOTH SPHERICAL PARTICLES [J]. INDUSTRIAL AND ENGINEERING CHEMISTRY, 1947, 39 (07): : 857 - 862

[8] HEAT TRANSFER CHARACTERISTICS OF FLUIDIZED BEDS [J]. INDUSTRIAL AND ENGINEERING CHEMISTRY, 1949, 41 (06): : 1135 - 1147

[9] AN IMPROVED EXPERIMENTAL REACTOR FOR APPLIED KINETIC STUDIES [J]. AICHE JOURNAL, 1958, 4 (03) : 351 - 355

[10] POZZI AL, 1961, THESIS U TEXAS