HETEROGENEOUS CATALYSIS IN A CONTINUOUS STIRRED TANK REACTOR

[1] DESIGNING LABORATORY CATALYTIC REACTORS [J]. INDUSTRIAL AND ENGINEERING CHEMISTRY, 1964, 56 (11): : 39 - &

[2] THE CATALYTIC EFFECTIVENESS FACTOR UNDER NONISOTHERMAL CONDITIONS [J]. AICHE JOURNAL, 1961, 7 (02) : 350 - 351

[3] A BOUNDARY-LAYER MODEL OF FLUID-PARTICLE MASS TRANSFER IN FIXED BEDS [J]. AICHE JOURNAL, 1960, 6 (03) : 460 - 463

[4] DIXON JK, 1960, CATALYSIS, V7, P281

[5] ELEY DD, 1961, 2 INT C CAT, V2, P1615

[6] FORD FE, 1964, CHEM ENG SCI, V19, P371, DOI 10.1016/0009-2509(64)80009-9

[7] MODELL M, 1964, THESIS MASSACHUSETTS

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

[9] SURFACE REACTIONS ON EVAPORATED PALLADIUM FILMS [J]. JOURNAL OF PHYSICAL CHEMISTRY, 1959, 63 (02) : 188 - 194

[10] TAJBL DG, 1966, THESIS U NOTRE DAME

[1] DESIGNING LABORATORY CATALYTIC REACTORS [J]. INDUSTRIAL AND ENGINEERING CHEMISTRY, 1964, 56 (11): : 39 - &

[2] THE CATALYTIC EFFECTIVENESS FACTOR UNDER NONISOTHERMAL CONDITIONS [J]. AICHE JOURNAL, 1961, 7 (02) : 350 - 351

[3] A BOUNDARY-LAYER MODEL OF FLUID-PARTICLE MASS TRANSFER IN FIXED BEDS [J]. AICHE JOURNAL, 1960, 6 (03) : 460 - 463

[4] DIXON JK, 1960, CATALYSIS, V7, P281

[5] ELEY DD, 1961, 2 INT C CAT, V2, P1615

[6] FORD FE, 1964, CHEM ENG SCI, V19, P371, DOI 10.1016/0009-2509(64)80009-9

[7] MODELL M, 1964, THESIS MASSACHUSETTS

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

[9] SURFACE REACTIONS ON EVAPORATED PALLADIUM FILMS [J]. JOURNAL OF PHYSICAL CHEMISTRY, 1959, 63 (02) : 188 - 194

[10] TAJBL DG, 1966, THESIS U NOTRE DAME