KINETIC-MODEL FOR ISOMERIZATION OF N-BUTENE TO ISOBUTENE

[1] DISCRIMINATION AMONG MECHANISTIC MODELS [J]. TECHNOMETRICS, 1967, 9 (01) : 57 - +

[2] BOX GEP, 1965, 51 U WISC DEP STAT T

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

[4] ISOMERIZATION OF BUTENE TO ISOBUTENE .1. SELECTION OF CATALYST BY GROUP SCREENING [J]. JOURNAL OF CATALYSIS, 1971, 23 (01) : 54 - +

[5] DEVELOPMENT OF CONTINUOUS-STIRRED GAS-SOLID REACTORS FOR STUDIES IN KINETICS AND CATALYST EVALUATION [J]. INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1972, 11 (03): : 420 - +

[6] CHOUDHARY VR, 1971, THESIS U POONA

[7] MASS TRANSFER EFFECTS IN SURFACE CATALYSIS [J]. AICHE JOURNAL, 1963, 9 (03) : 371 - 374

[8] FORD FE, 1963, THESIS U ILLINOIS

[9] HOUGEN OA, 1947, CHEMICAL PROCESS P 3

[10] JENKINS AD, 1968, ENCYCLOPEDIA POLYMER, V8, P89

[1] DISCRIMINATION AMONG MECHANISTIC MODELS [J]. TECHNOMETRICS, 1967, 9 (01) : 57 - +

[2] BOX GEP, 1965, 51 U WISC DEP STAT T

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

[4] ISOMERIZATION OF BUTENE TO ISOBUTENE .1. SELECTION OF CATALYST BY GROUP SCREENING [J]. JOURNAL OF CATALYSIS, 1971, 23 (01) : 54 - +

[5] DEVELOPMENT OF CONTINUOUS-STIRRED GAS-SOLID REACTORS FOR STUDIES IN KINETICS AND CATALYST EVALUATION [J]. INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1972, 11 (03): : 420 - +

[6] CHOUDHARY VR, 1971, THESIS U POONA

[7] MASS TRANSFER EFFECTS IN SURFACE CATALYSIS [J]. AICHE JOURNAL, 1963, 9 (03) : 371 - 374

[8] FORD FE, 1963, THESIS U ILLINOIS

[9] HOUGEN OA, 1947, CHEMICAL PROCESS P 3

[10] JENKINS AD, 1968, ENCYCLOPEDIA POLYMER, V8, P89