NON-ISOTHERMAL EFFECTIVENESS FACTORS

[1] A COMPUTER MODEL OF THE FIXED BED CATALYTIC REACTOR - THE ADIABATIC AND QUASI-ADIABATIC CASES [J]. AICHE JOURNAL, 1963, 9 (01) : 129 - 133

[2] AN EXPERIMENTAL STUDY OF EFFECT OF INTRAPARTICLE TEMPERATURE GRADIENTS ON CATALYTIC ACTIVITY [J]. CHEMICAL ENGINEERING SCIENCE, 1967, 22 (12) : 1859 - &

[3] LIU SL, UNPUBLISHED WORKS

[4] MCGREAVY C, 1968, SEP TRIP CHEM ENG C

[5] PETERSEN EE, 1962, CHEM ENGNG SCI, V17, P986

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

[7] THE BEHAVIOUR OF POROUS CATALYST PARTICLES IN VIEW OF INTERNAL MASS AND HEAT DIFFUSION EFFECTS [J]. CHEMICAL ENGINEERING SCIENCE, 1962, 17 (04) : 265 - 275

[8] [No title captured]

[1] A COMPUTER MODEL OF THE FIXED BED CATALYTIC REACTOR - THE ADIABATIC AND QUASI-ADIABATIC CASES [J]. AICHE JOURNAL, 1963, 9 (01) : 129 - 133

[2] AN EXPERIMENTAL STUDY OF EFFECT OF INTRAPARTICLE TEMPERATURE GRADIENTS ON CATALYTIC ACTIVITY [J]. CHEMICAL ENGINEERING SCIENCE, 1967, 22 (12) : 1859 - &

[3] LIU SL, UNPUBLISHED WORKS

[4] MCGREAVY C, 1968, SEP TRIP CHEM ENG C

[5] PETERSEN EE, 1962, CHEM ENGNG SCI, V17, P986

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

[7] THE BEHAVIOUR OF POROUS CATALYST PARTICLES IN VIEW OF INTERNAL MASS AND HEAT DIFFUSION EFFECTS [J]. CHEMICAL ENGINEERING SCIENCE, 1962, 17 (04) : 265 - 275

[8] [No title captured]