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kw.\*:("FIXED BED CATALYTIC REACTOR")

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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

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

IMPACT OF POROSITY AND VELOCITY DISTRIBUTION ON THE THEORETICAL PREDICTION OF FIXED-BED CHEMICAL REACTOR PERFORMANCEVORTMEYER D; WINTER RP.1981; ACS SYMP. SER.; ISSN 0097-6156; USA; DA. 1981; NO 196; PP. 49-61; BIBL. 21 REF.Conference Paper

CATALYST DEACTIVATION AND OPTIMAL OPERATION POLICY: IMMOBILIZED BETA -GALACTOSIDASE = LA DESACTIVATION DU CATALYSEUR, OPTIMALISATION DE L'OPERATION: LA BETA -GALACTOSIDASE IMMOBILISEEPRENOSIL JE; PETER J; BOURNE JR et al.1980; ENZYME ENGINEERING. INTERNATIONAL ENZYME ENGINEERING CONFERENCE. 5/1979-07-29/HENNIKER NH; USA/GBR; NEW YORK; LONDON: PLENUM PRESS; DA. 1980; PP. 317-320; BIBL. 3 REF.Conference Paper

ON OPTIMUM TEMPERATURE OPERATIONS IN DEACTIVATING FIXED-BED REACTORSAJIT SADANA.1980; CHEM. ENGNG COMMUNIC.; GBR; DA. 1980; VOL. 4; NO 1; PP. 51-55; BIBL. 7 REF.Article

MODELISATION DES REACTEURS AVEC CATALYSEUR A LIT FIXESLIN'KO MG; DIL'MAN VV; MARKEEV BM et al.1980; KHIM. PROMYSHL.; SUN; DA. 1980; NO 11; PP. 662-671; BIBL. 105 REF.Article

ESTIMATION DES CARACTERISTIQUES PRINCIPALES DU FRONT DE LA REACTION EXOTHERMIQUE, DANS UNE COUCHE IMMOBILE DE CATALYSEURBORESKOV GK; KISELEV OV; MATROS YU SH et al.1979; DOKL. AKAD. NAUK SSSR; ISSN 0002-3264; SUN; DA. 1979; VOL. 248; NO 2; PP. 406-408; BIBL. 5 REF.Article

MEASURED AND CALCULATED MIGRATING SPEEDS OF REACTION ZONES IN A FIXED BED REACTOR; A QUANTITATIVE COMPARISON.SIMON B; VORTMEYER D.1978; CHEM. ENGNG SCI.; G.B.; DA. 1978; VOL. 33; NO 1; PP. 109-114; BIBL. 23 REF.Article

DISCUSSION OF THE PRACTICAL APPLICABILITY OF SOME SUGGESTED CRITERIA FOR THE RUNAWAY OF FIXED BED REACTORSMAHMOUD EL SAWI; PROCOPIO A.1980; QUAD. ING. CHIM. ITAL.; ISSN 0370-288X; ITA; DA. 1980; NO 7-8; PP. 59-61; ABS. ITA; BIBL. 8 REF.Article

DYNAMISCHES VERHALTEN VON FESTBETTREAKTOREN. = COMPORTEMENT DYNAMIQUE DES REACTEURS A LIT FIXEGILLES ED.1977; CHEM. INGR-TECH.; DTSCH.; DA. 1977; VOL. 49; NO 2; PP. 142-149; ABS. ANGL.; BIBL. 19 REF.Article

DIE MODELLIERUNG DES STATISCHEN BETRIEBSVERHALTENS EINES SCHICHTREAKTORS ZUR AMMONIAKSYNTHESE. = MODELISATION DU COMPORTEMENT STATIQUE EN SERVICE D'UN REACTEUR MULTICOUCHES DE SYNTHESE DE L'AMMONIACLUTSCHUTENKOW SM; REINIG G; BRACK G et al.1976; WISSENSCH. Z. TECH. HOCHSCH. "CARL SCHORLEMMER" LEUNA-MERSEBURG; DTSCH.; DA. 1976; VOL. 18; NO 4; PP. 619-635; BIBL. 15 REF.Article

SENSITIVIDADE PARAMETRICA NO PROJETO DE REATORES QUIMICOS. = SENSIBILITE PARAMETRIQUE DANS LE CALCUL DES REACTEURS CHIMIQUESDA FONSECA NM; CHALBAUD BISCAIA E JR.1976; REV. BRAS. TECNOL.; BRAS.; DA. 1976; VOL. 7; NO 3; PP. 327-338; ABS. ANGL.; BIBL. 8 REF.Article

REACTEURS CATALYTIQUES DE TYPE RADIAL A LIT FIXESERGEEV SP; DIL'MAN VV.1982; HIM. PROM.; ISSN 506834; SUN; DA. 1982; NO 8; PP. 469-470; BIBL. 25 REF.Article

DIFFUSION KINETICS OF SELECTIVE HYDROGENATION OF FATTY OILS IN A STATIONARY CATALYST BED REACTORYERMAKOVA A; UMBETOV AS.1980; REACT. KINET. CATALYS. LETTERS; HUN; DA. 1980; VOL. 14; NO 2; PP. 187-192; ABS. RUS; BIBL. 7 REF.Article

AERODYNAMIQUE DES REACTEURS INDUSTRIELS AVEC CATALYSEUR A LIT FIXEBESKOV VS; ABAEV GN.1980; KHIM. PROMYSHL.; SUN; DA. 1980; NO 11; PP. 673-675; BIBL. 25 REF.Article

THE OPTIMUM TEMPERATURE POLICY FOR A DEACTIVATING CATALYTIC PACKED BED REACTORCROWE CM.1979; CHEM. ENGNG SCI.; GBR; DA. 1979; VOL. 34; NO 9; PP. 1176; BIBL. 2 REF.Article

ETUDE DES REGIONS PERMANENTS D'UN REACTEUR CHIMIQUE A COUCHE STATIONNAIRE DE CATALYSEUR NON POREUXMAKSIMOV EH I.1979; DOKL. AKAD. NAUK SSSR; ISSN 0002-3264; SUN; DA. 1979; VOL. 248; NO 6; PP. 1395-1399; BIBL. 4 REF.Article

THE OPTIMUM TEMPERATURE POLICY FOR A DEACTIVATING CATALYTIC PACKED BED REACTORLEVENSPIEL O; AJIT SADANA.1978; CHEM. ENGNG SCI.; GBR; DA. 1978; VOL. 33; NO 10; PP. 1393-1394; BIBL. 9 REF.Article

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