EFFECT OF TRANSPORT PROCESSES ON CONVERSION IN A FIXED BED REACTOR

[1] THE MICRO-MACRO EFFECTIVENESS FACTOR FOR THE REVERSIBLE CATALYTIC REACTION [J]. AICHE JOURNAL, 1962, 8 (04) : 557 - 558

[2] YIELD IN CHEMICAL REACTOR ENGINEERING [J]. INDUSTRIAL AND ENGINEERING CHEMISTRY, 1966, 58 (10): : 40 - &

[3] FIXED BED CATALYTIC REACTORS - CURRENT DESIGN STATUS [J]. INDUSTRIAL AND ENGINEERING CHEMISTRY, 1967, 59 (02): : 18 - &

[4] KUNNI D, 1967, INT J HEAT MASS TRAN, V10, P845

[5] AXIAL MIXING OF BINARY GAS MIXTURES FLOWING IN A RANDOM BED OF SPHERES [J]. AICHE JOURNAL, 1957, 3 (01) : 83 - 91

[6] EFFECTIVENESS OF LARGE CATALYST PELLETS-AN EXPERIMENTAL STUDY [J]. JOURNAL OF CATALYSIS, 1966, 5 (02) : 332 - &

[7] RANZ WE, 1952, CHEM ENG PROG, V48, P247

[8] A SIMPLE METHOD OF CALCULATING MASS TRANSFER FACTORS FOR HETEROGENEOUS CATALYTIC GAS REACTIONS [J]. CHEMICAL ENGINEERING SCIENCE, 1968, 23 (07) : 759 - &

[9] SUZUKI M, TO BE PUBLISHED

[10] Relation between catalytic activity and size of particle [J]. INDUSTRIAL AND ENGINEERING CHEMISTRY, 1939, 31 : 916 - 920

[1] THE MICRO-MACRO EFFECTIVENESS FACTOR FOR THE REVERSIBLE CATALYTIC REACTION [J]. AICHE JOURNAL, 1962, 8 (04) : 557 - 558

[2] YIELD IN CHEMICAL REACTOR ENGINEERING [J]. INDUSTRIAL AND ENGINEERING CHEMISTRY, 1966, 58 (10): : 40 - &

[3] FIXED BED CATALYTIC REACTORS - CURRENT DESIGN STATUS [J]. INDUSTRIAL AND ENGINEERING CHEMISTRY, 1967, 59 (02): : 18 - &

[4] KUNNI D, 1967, INT J HEAT MASS TRAN, V10, P845

[5] AXIAL MIXING OF BINARY GAS MIXTURES FLOWING IN A RANDOM BED OF SPHERES [J]. AICHE JOURNAL, 1957, 3 (01) : 83 - 91

[6] EFFECTIVENESS OF LARGE CATALYST PELLETS-AN EXPERIMENTAL STUDY [J]. JOURNAL OF CATALYSIS, 1966, 5 (02) : 332 - &

[7] RANZ WE, 1952, CHEM ENG PROG, V48, P247

[8] A SIMPLE METHOD OF CALCULATING MASS TRANSFER FACTORS FOR HETEROGENEOUS CATALYTIC GAS REACTIONS [J]. CHEMICAL ENGINEERING SCIENCE, 1968, 23 (07) : 759 - &

[9] SUZUKI M, TO BE PUBLISHED

[10] Relation between catalytic activity and size of particle [J]. INDUSTRIAL AND ENGINEERING CHEMISTRY, 1939, 31 : 916 - 920