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ANALYSIS AND DESIGN OF FIXED BED CATALYTIC REACTORSFROMENT GF.1972; ADV. CHEM. SER.; U.S.A.; DA. 1972; VOL. 109; PP. 1-34; BIBL. 2 P.Serial Issue

THERMAL CRACKING FOR OLEFINS PRODUCTION. FUNDAMENTALS AND THEIR APPLICATION TO INDUSTRIAL PROBLEMSFROMENT GF.1981; CHEM. ENG. SCI.; ISSN 0009-2509; GBR; DA. 1981; VOL. 36; NO 8; PP. 1271-1282; BIBL. 48 REF.Article

MODEL DISCRIMINATION AND PARAMETER ESTIMATION IN HETEROGENEOUS CATALYSISFROMENT GF.1975; A. I. CH. E. J., NEW YORK; U.S.A.; DA. 1975; VOL. 21; NO 6; PP. 1041-1057; BIBL. 1 P. 1/2Article

RELATIONSHIPS BETWEEN THE KINETIC PARAMETERS OF DECOMPOSITION RATES OF RADICALS IN THE THERMAL CRACKING OF PARAFFINSMOENS JA; FROMENT GF.1982; J. ANAL. APPL. PYROLYSIS; ISSN 0165-2370; NLD; DA. 1982; VOL. 3; NO 3; PP. 187-197; BIBL. 14 REF.Article

THE PROBLEM OF INTRAPARTICLE MASS TRANSFER LIMITATIONS IN REACTOR DESIGN. A SIMPLIFIED APPROACH.DUMEZ FJ; FROMENT GF.1977; CHEM. ENGNG SCI.; G.B.; DA. 1977; VOL. 32; NO 8; PP. 974-977; BIBL. 5 REF.Article

VELOCITY, TEMPERATURE AND CONVERSION PROFILES IN FIXED BED CATALYTIC REACTORS.LEROU JJ; FROMENT GF.1977; CHEM. ENGNG SCI.; G.B.; DA. 1977; VOL. 32; NO 8; PP. 853-861; BIBL. 39 REF.Article

PARAMETER ESTIMATION IN MULTIRESPONSE MODELSHOSTEN LH; FROMENT GF.1975; PERIOD. POLYTECH., CHEM. ENGNG; HONGR.; DA. 1975; VOL. 19; NO 1-2; PP. 123-136; BIBL. 12 REF.Article

RESIDUAL HYDROGEN IN SUPPORTED PLATINUM CATALYSTS AND ITS INFLUENCE ON THEIR CATALYTIC PROPERTIESMENON PG; FROMENT GF.1981; APPL. CATAL.; NLD; DA. 1981; VOL. 1; NO 1-2; PP. 31-48; BIBL. 26 REF.Article

CATALYST DEACTIVATION BY SITE COVERAGE AND PORE BLOCKAGE: FINITE RATE OF GROWTH OF THE CARBONACEOUS DEPOSITBEECKMAN JW; FROMENT GF.1980; CHEM. ENG. SCI.; ISSN 0009-2509; GBR; DA. 1980; VOL. 35; NO 4; PP. 805-815; BIBL. 11 REF.Article

TWO DIMENSIONAL MODEL FOR THE SIMULATION OF TUBULAR REACTORS FOR THERMAL CRACKINGSUNDARAM KM; FROMENT GF.1980; CHEM. ENGNG SCI.; GBR; DA. 1980; VOL. 35; NO 1-2; PP. 364-371; BIBL. 15 REF.Conference Paper

DEACTIVATION OF CATALYSTS BY COKE FORMATION IN THE PRESENCE OF INTERNAL DIFFUSIONAL LIMITATIONBEECKMAN JW; FROMENT GF.1982; IND. ENG. CHEM., FUNDAM.; ISSN 0019-7874; USA; DA. 1982; VOL. 21; NO 3; PP. 243-250; BIBL. 15 REF.Article

HYDROISOMERIZATION AND HYDROCRACKING. III: KINETIC ANALYSIS OF RATE DATA FOR N-DECANE AND N-DODECANESTEIJNS M; FROMENT GF.1981; IND. ENG. CHEM., PROD. RES. DEV.; ISSN 0019-7890; USA; DA. 1981; VOL. 20; NO 4; PP. 660-668; BIBL. 30 REF.Article

KINETICS OF COKE DEPOSITION IN THE THERMAL CRACKING OF PROPANESUNDARAM KM; FROMENT GF.1979; CHEM. ENGNG SCI.; GBR; DA. 1979; VOL. 34; NO 5; PP. 635-644; BIBL. 23 REF.Article

MODELING OF THERMAL CRACKING KINETICS. III: RADICAL MECHANISMS FOR THE PYROLYSIS OF SIMPLE PARAFFINS, OLEFINS, AND THEIR MIXTURESSUNDARAM KM; FROMENT GF.1978; INDUSTR. ENGNG CHEM., FUNDAM.; USA; DA. 1978; VOL. 17; NO 3; PP. 174-182; BIBL. 57 REF.Article

MODELING OF THERMAL CRACKING KINETICS. II. CRACKING OF ISO-BUTANE, OF N-BUTANE AND OF MIXTURES ETHANE-PROPANE-N-BUTANE.SUNDARAM KM; FROMENT GF.1977; CHEM. ENGNG SCI.; G.B.; DA. 1977; VOL. 32; NO 6; PP. 609-617; BIBL. 14 REF.Article

CATALYST DEACTIVATION BY ACTIVE SITE COVERAGE AND PORE BLOCKAGEBEECKMAN JW; FROMENT GF.1979; INDUSTR. ENGNG CHEM., FUNDAM.; USA; DA. 1979; VOL. 18; NO 3; PP. 245-256; BIBL. 20 REF.Article

MODIFICATION OF THE PROPERTIES OF PT-AL2O3 CATALYSTS BY HYDROGEN AT HIGH TEMPERATURESMENON PG; FROMENT GF.1979; J. CATALYS.; USA; DA. 1979; VOL. 59; NO 1; PP. 138-147; BIBL. 25 REF.Article

A COMPARISON OF SIMULATION MODELS FOR EMPTY TUBULAR REACTORSSUNDARAM KM; FROMENT GF.1979; CHEM. ENGNG SCI.; GBR; DA. 1979; VOL. 34; NO 1; PP. 117-124; BIBL. 11 REF.Article

THE ACCURACY OF THE PSEUDO-STEADY-STATE APPROXIMATION FOR RADICALS IN THERMAL CRACKINGSUNDARAM KM; FROMENT GF.1978; INTERNATION. J. CHEM. KINET.; USA; DA. 1978; VOL. 10; NO 11; PP. 1189-1193; BIBL. 7 REF.Article

MODELING OF THERMAL CRACKING KINETICS. I. THERMAL CRACKING OF ETHANE, PROPANE AND THEIR MIXTURES.SUNDARAM KM; FROMENT GF.1977; CHEM. ENGNG SCI.; G.B.; DA. 1977; VOL. 32; NO 6; PP. 601-608; BIBL. 13 REF.Article

DEHYDROGENATION OF 1-BUTENE INTO BUTADIENE. KINETICS, CATALYST COKING, AND REACTOR DESIGNDUMEZ FJ; FROMENT GF.1976; INDUSTR. ENGNG CHEM., PROCESS DESIGN DEVELOP.; U.S.A.; DA. 1976; VOL. 15; NO 2; PP. 291-301; BIBL. 31 REF.Article

DEACTIVATION OF A PLATINUM REFORMING CATALYST IN A TUBULAR REACTOR. = DESACTIVATION D'UN CATALYSEUR DE REFORMAGE AU PLATINE DANS UN REACTEUR TUBULAIREDE PAUW RP; FROMENT GF.1975; CHEM. ENGNG SCI.; G.B.; DA. 1975; VOL. 30; NO 8; PP. 789-801; BIBL. 10 REF.Article

AN IMPROVED ZONE METHOD USING MONTE CARLO TECHNIQUES FOR THE SIMULATION OF RADIATION IN INDUSTRIAL FURNACESVERCAMMEN HAJ; FROMENT GF.1980; INT. J. HEAT MASS TRANSFER; GBR; DA. 1980-03; VOL. 23; NO 3; PP. 329-337; BIBL. 17 REF.Article

ESTIMATION OF HEAT TRANSFER PARAMETERS IN PACKED BEDS FROM RADIAL TEMPERATURE PROFILESLEROU JJ; FROMENT GF.1978; CHEM. ENGNG J.; GBR; DA. 1978; VOL. 15; NO 3; PP. 233-237; BIBL. 13 REF.Article

THERMAL CRACKING COMPUTER CONTROL IN PILOT PLANTSVAN DAMME PS; FROMENT GF.1982; CEP CHEM. ENG. PROG.; ISSN 0360-7275; USA; DA. 1982; VOL. 78; NO 9; PP. 77-82; BIBL. 8 REF.Article

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