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kw.\*:("REACTEUR CATALYTIQUE LIT FIXE")

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Results 1 to 25 of 517

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PARTIAL WETTING IN TRICKLE BED REACTORS, THE REDUCTION OF CROTONALDEHYDE OVER A PALLADIUM CATALYSTSEDRIKS W; KENNEY CN.1973; CHEM. ENGNG SCI.; G.B.; DA. 1973; VOL. 28; NO 2; PP. 559-568; BIBL. 10 REF.Serial Issue

THE STABILITY OF FIXED BED CATALYTIC REACTORSMCGREAVY C; SOLIMAN MA.1973; CHEM. ENGNG SCI.; G.B.; DA. 1973; VOL. 28; NO 7; PP. 1401-1415; BIBL. 1 P.Serial Issue

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

STATE-SPACE FORMULATION OF FIXED-BED REACTOR DYNAMICSMICHESEN ML; VAKIL HB; FOSS AS et al.1973; INDUSTR. ENGNG CHEM., FUNDAM.; U.S.A.; DA. 1973; VOL. 12; NO 3; PP. 323-328; BIBL. 10 REF.Serial Issue

FIXED BED REACTOR ANALYSIS BY ORTHOGONAL COLLOCATIONFINLAYSON BA.1972; ADV. CHEM. SER.; U.S.A.; DA. 1972; VOL. 109; PP. 50-53; BIBL. 12 REF.Serial Issue

PREDICTION OF HOT-SPOT LOCATION IN CATALYTIC FIXED-BED REACTORSKUNII D; FURUSAMA T.1972; CHEM. ENGNG J.; G.B.; DA. 1972; VOL. 4; NO 3; PP. 268-281; BIBL. 21 REF.Serial Issue

EFFECT OF TRANSPORT PROCESS ON CONVERSION IN A TRICKLE-BED REACTORSYLVESTER ND; PUNYA PITAYAGULSARN.1973; A.I.CH.E.J., NEW YORK; U.S.A.; DA. 1973; VOL. 19; NO 3; PP. 640-644; BIBL. 16 REF.Serial Issue

FIXED-BED REACTOR CONTROL WITH STATE ESTIMATIONVAKIL HB; MICHELSEN ML; FOSS AS et al.1973; INDUSTR. ENGNG CHEM., FUNDAM.; U.S.A.; DA. 1973; VOL. 12; NO 3; PP. 328-335; BIBL. 10 REF.Serial Issue

MOVING REACTION ZONES IN FIXED BED REACTORS UNDER THE INFLUENCE OF VARIOUS PARAMETERSVORTMEYER D; JAHNEL W.1972; CHEM. ENGNG SCI.; G.B.; DA. 1972; VOL. 27; NO 8; PP. 1485-1496; ABS. FR. ALLEM.; BIBL. 10 REF.Serial Issue

RADIANT ANALYSIS IN PACKED BED REACTORSVORTMEYER D.1972; ADV. CHEM. SER.; U.S.A.; DA. 1972; VOL. 109; PP. 43-47; BIBL. 13 REF.Serial Issue

FOULING OF BIFUNCTIONAL CATALYSTS IN A PACKED BED REACTORSNYDER C; MATTHEWS JC.1973; CHEM. ENGNG SCI.; G.B.; DA. 1973; VOL. 28; NO 1; PP. 291-295; BIBL. 14 REF.Serial Issue

GENERALIZED CRITERIA FOR PARAMETRIC SENSITIVITY AND TEMPERATURE RUNAWAY IN CATALYTIC REACTORSMCGREAVY C; ADDERLEY CI.1973; CHEM. ENGNG SCI.; G.B.; DA. 1973; VOL. 28; NO 2; PP. 577-584; BIBL. 8 REF.Serial Issue

PARTIAL WETTING IN TRICKLE BED REACTORSSEDRIKS W; KENNEY CN.1972; ADV. CHEM. SER.; U.S.A.; DA. 1972; VOL. 109; PP. 251-255Serial Issue

THE OPTIMUM TEMPERATURE POLICY FOR A DEACTIVATING CATALYTIC PACKED-BED REACTOR. AN IMPROVED METHOD OF OPERATIONSAJIT SADANA.1982; CHEM. ENG. SCI.; ISSN 0009-2509; GBR; DA. 1982; VOL. 37; NO 3; PP. 492-494; BIBL. 11 REF.Article

RESTRICTIONS AND EQUIVALENCE OF OPTIMAL TEMPERATURE POLICIES FOR REACTORS WITH DECAYING CATALYSTSPOMMERSHEIM JM; TAVLARIDES LL; MUKKAVILLI S et al.1980; A.I. CH. E.J., NEW YORK; USA; DA. 1980; VOL. 26; NO 2; PP. 327-330; BIBL. 3 REF.Article

OPTIMUM AXIAL TEMPERATURE DISTRIBUTION FOR MAXIMUM REACTOR YIELD WITH THE STAGNANT POCKET MODELKUBO K; ARATANI T; MISHIMA A et al.1979; J. CHEM. ENGNG JAP.; JPN; DA. 1979; VOL. 12; NO 1; PP. 74-76; BIBL. 7 REF.Article

REDUCED DYNAMIC MODEL OF A FIXED BED REACTOR.MCGREAVY C; NAIM HM.1977; CANAD. J. CHEM. ENGNG; CANADA; DA. 1977; VOL. 55; NO 3; PP. 326-332; ABS. FR.; BIBL. 10 REF.Article

DISTRIBUTION OPTIMALE DU CATALYSEUR SUR LA LONGUEUR D'UNE COUCHE DE CONTACTDARINSKIJ YU V; IKHSANOV ZH A; LUK'YANOV AT et al.1977; TEOR. OSHOVY KHIM. TEKHNOL.; S.S.S.R.; DA. 1977; VOL. 11; NO 3; PP. 371-376; BIBL. 7 REF.Article

ZUR MODELLIERUNG KATALYTISCHER DREIPHASENPROZESSE. II. EXPERIMENTELLE UNTERSUCHUNGEN IM RIESELREAKTOR ZUR HYDRIERUNG VON ALPHA -METHYLSTYROL = MODELISATION DES PROCESSUS CATALYTIQUES A TROIS PHASES. II. ETUDES EXPERIMENTALES DANS UN REACTEUR A RUISSELLEMENT DE L'HYDROGENATION DE L'ALPHA -METHYLSTYRENETUREK F; LANGE R; BUSCH A et al.1976; CHEM. TECH.; DTSCH.; DA. 1976; VOL. 28; NO 3; PP. 149-152; BIBL. 11 REF.Article

A MODEL FOR THE RESIDENCE TIME DISTRIBUTION OF LIQUID PHASE IN TRICKLE BEDSRAO VG; VARMA YBG.1976; A.I.CH.E. J., NEW YORK; U.S.A.; DA. 1976; VOL. 22; NO 3; PP. 612-615; BIBL. 14 REF.Article

PARAMETER-ERMITTLUNG FUER FESTBETTREAKTOREN MIT INSTATIONAEREN MESSTECHNIKEN = DETERMINATION DES PARAMETRES POUR REACTEURS A LIT FIXE A L'AIDE DE TECHNIQUES DE MESURES VARIABLESSCHUGERL K; ORTH P.1972; V.D.I. BER.; DTSCH.; DA. 1972; NO 187; PP. 135-140; BIBL. 6 REF.Serial Issue

BREVET 2.330.451 (A1) (75 31495). - 15 OCTOBRE 1975. REACTEUR A CLAIES A PLUSIEURS ETAGES.sdPatent

OPTIMIZING CYCLE LENGTHS OF CATALYTIC REACTORSSHAH GC; MATLEY J ED.1983; CHEMICAL ENGINEERING (NEW YORK); ISSN 0009-2460; USA; DA. 1983; VOL. 90; NO 12; PP. 123-126; 3 P.; BIBL. 3 REF.Article

FILM DIFFUSIONAL INFLUENCES ON THE KINETIC PARAMETERS IN PACKED-BED IMMOBILIZED ENZYME REACTORS = INFLUENCE DE LA DIFFUSION A TRAVERS LE FILM SUR LES PARAMETRES CINETIQUES DE REACTEURS A ENZYMES IMMOBILISEES EN LIT FIXEPATWARDHAN VS; KARANTH NG.1982; BIOTECHNOL. BIOENG.; ISSN 0006-3592; USA; DA. 1982; VOL. 24; NO 4; PP. 763-780; BIBL. 37 REF.Article

A NON-FICKIAN MODEL OF PACKED-BED REACTORSHSUEH CHIA CHANG.1982; AICHE J.; ISSN 0001-1541; USA; DA. 1982; VOL. 28; NO 2; PP. 208-214; BIBL. 19 REF.Article

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