FIXED BED CATALYTIC REACTORS - CURRENT DESIGN STATUS

[1] BARKELEW CR, 1959, CHEM ENG PROG S SER, V55, P38

[2] BARON T, 1952, CHEM ENG PROG, V48, P118

[3] BEEK T, 1962, ADVANCES CHEMICAL EN, P3

[4] BEEK T, 1962, ADVANCES CHEMICAL EN, P203

[5] BERNARD RA, 1950, CHEM ENG PROG, V46, P233

[6] CHEMICAL REACTOR STABILITY AND SENSITIVITY .2. EFFECT OF PARAMETERS ON SENSITIVITY OF EMPTY TUBULAR REACTORS [J]. AICHE JOURNAL, 1956, 2 (01) : 117 - 126

[7] LONGITUDINAL MIXING IN FLUIDIZATION [J]. AICHE JOURNAL, 1960, 6 (03) : 400 - 409

[8] Calderbank P.H., 1957, TRANS INST CHEM ENG, V35, P195

[9] CAMPBELL TM, 1952, HYDROCARBON PROCESS, V31, P123

[10] AXIAL DISPERSION OF MASS IN FLOW THROUGH FIXED BEDS [J]. AICHE JOURNAL, 1958, 4 (03) : 367 - 375

[1] BARKELEW CR, 1959, CHEM ENG PROG S SER, V55, P38

[2] BARON T, 1952, CHEM ENG PROG, V48, P118

[3] BEEK T, 1962, ADVANCES CHEMICAL EN, P3

[4] BEEK T, 1962, ADVANCES CHEMICAL EN, P203

[5] BERNARD RA, 1950, CHEM ENG PROG, V46, P233

[6] CHEMICAL REACTOR STABILITY AND SENSITIVITY .2. EFFECT OF PARAMETERS ON SENSITIVITY OF EMPTY TUBULAR REACTORS [J]. AICHE JOURNAL, 1956, 2 (01) : 117 - 126

[7] LONGITUDINAL MIXING IN FLUIDIZATION [J]. AICHE JOURNAL, 1960, 6 (03) : 400 - 409

[8] Calderbank P.H., 1957, TRANS INST CHEM ENG, V35, P195

[9] CAMPBELL TM, 1952, HYDROCARBON PROCESS, V31, P123

[10] AXIAL DISPERSION OF MASS IN FLOW THROUGH FIXED BEDS [J]. AICHE JOURNAL, 1958, 4 (03) : 367 - 375