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MODELE MATHEMATIQUE DE LA PYROLYSE DANS UN REACTEUR A LIT FIXELEBEDEV BN; KOROTOV S YA.1974; IZVEST. VYSSH. UCHEBN. ZAVED., LESN. ZH.; S.S.S.R.; DA. 1974; VOL. 17; NO 5; PP. 103-106; BIBL. 4 REF.Article

REOPTER. A COMPUTER PROGRAM FOR SIMULATION, DESIGN AND ANALYSIS OF FIXED BED CATALYTIC REACTORS = REOPTER. UN PROGRAMME D'ORDINATEUR POUR LA SIMULATION, LA CONCEPTION ET L'ANALYSE DE REACTEURS CATALYTIQUES A LIT FIXEHAZBUN EA; WHITE JW.sdIN: 76TH NATL. MEET. AM INST. CHEM. ENG.; TULSA, OKLA.; 1974; NEW YORK; A.I.CH.E.; DA. S.D.; VOL. 41A; PP. (17 P.); BIBL. 13 REF.Conference Paper

CONTRIBUTION A L'ETUDE DE LA DECOMPOSITION CATALYTIQUE DU PEROXYDE D'HYDROGENE LIQUIDE PAR L'ARGENTVANTELON JP.1975; AO-CNRS-10937; FR.; DA. 1975; PP. 1-140; H.T. 42; BIBL. 5 P. 1/2; (THESE DOCT. SCI. PHYS.; POITIERS)Thesis

COKED CATALYST REGENERATION PROBLEMSHETTIGAR UR; SEBASTIAN MT.1974; CHEM. ENGNG J.; G.B.; DA. 1974; VOL. 7; NO 2; PP. 167-172; BIBL. 10 REF.Article

RECENT DEVELOPMENTS IN COAL GASIFICATIONSCHAD MK; HAFKE CF.1983; CEP, CHEMICAL ENGINEERING PROGRESS; ISSN 0360-7275; USA; DA. 1983; VOL. 79; NO 5; PP. 45-51; BIBL. 4 REF.Article

GASIFIER BRINGS ENERGY SECURITY1982; POWER; ISSN 0032-5929; USA; DA. 1982; VOL. 126; NO 9; PP. 115Article

OPTIMAL CATALYST PROFILES FOR A TWO-STEP REACTION SEQUENCE IN A PACKED BEDHO NAM CHANG; REILLY PJ.1976; CHEM. ENGNG SCI.; G.B.; DA. 1976; VOL. 31; NO 6; PP. 413-418; BIBL. 11 REF.Article

EXPERIMENTAL VERIFICATION OF AN ENGINEERING MODEL OF COAL AGGLOMERATION DURING GASIFICATIONAPTE AJ; FEIN HL; GARDNER MP et al.1982; INTERNATIONAL GAS RESEARCH CONFERENCE/1981/LOS ANGELES CA; USA; ROCKVILLE MD: GOVERNMENT INSTITUTES; DA. 1982; PP. 418-431; BIBL. 12 REF.Conference Paper

SENSITIVITY ANALYSIS IN THE DESIGN OF A PACKED BED REACTORPRIESTLEY AJ; AGNEW JB.1975; INDUSTR. ENGNG CHEM., PROCESS DESIGN DEVELOP.; U.S.A.; DA. 1975; VOL. 14; NO 2; PP. 171-174; BIBL. 10 REF.Article

OPTIMIZATION BY DISTRIBUTED CONTROL OF REACTORS WITH DECAYING CATALYST. I. NON-LINEAR CATALYST DEACTIVATIONTHERIEN N; CROWE CM.1974; CANAD. J. CHEM. ENGNG; CANADA; DA. 1974; VOL. 52; NO NO 6; PP. 810-821; BIBL. 13 REF.Article

OPTIMIZATION BY DISTRIBUTED CONTROL OF REACTORS WITH DECAYING CATALYST. II. FIRST-ORDER CATALYST DEACTIVATION = OPTIMALISATION PAR COMMANDE DISTRIBUEE DES REACTEURS AVEC DEGRADATION DU CATALYSEUR. II. DESACTIVATION DU CATALYSEUR DE PREMIER ORDRECROWE CM; THERIEN N.1974; CANAD. J. CHEM. ENGNG; CANADA; DA. 1974; VOL. 52; NO NO 6; PP. 822-829; ABS. FR.; BIBL. 16 REF.Article

MODELLI FISICO-MATEMATICI DI REATTORI CATALITICI A LETTO FISSO. II. MODELLO MONODIMENSIONALE CORETTO = MODELES PHYSICO-MATHEMATIQUES DE REACTEURS CATALYTIQUES A LIT FIXE. II. MODELE UNIDIMENSIONNEL CORRIGEFONTANA P; DE MARCHI G; CANEPA B et al.1974; QUAD. INGEGNERE CHIM. ITAL.; ITAL.,; DA. 1974; VOL. 10; NO 6 SUPPL; PP. 99-106; ABS. ANGL.; BIBL. 13 REF.Article

WALL HEAT TRANSFER TO CHEMICAL REACTORSCHAO RE; CABAN RA; IRIZARRY MM et al.1973; CANAD. J. CHEM. ENGNG; CANADA; DA. 1973; VOL. 51; NO 1; PP. 67-70; ABS. FR.; BIBL. 31 REF.Serial Issue

ZUR FRAGE DES DURCHGEHENS VON SCHUETTSCHICHTREAKTOREN. = SUR L'EMBALLEMENT DES REACTEURS A LIT A GARNISSAGEMAHMOUD EL SAWI; EMIG G; HOFFMANN U et al.1977; CHEM.-INGR-TECH.; DTSCH.; DA. 1977; VOL. 49; NO 1; PP. 40-42; BIBL. 7 REF.Article

DESIGN OF FIXED BED CATALYTIC MICROREACTORSSILVERSTEIN J; SHINNAR R.1975; INDUSTR. ENGNG CHEM., PROCESS DESIGN DEVELOP.; U.S.A.; DA. 1975; VOL. 14; NO 2; PP. 127-137; BIBL. 15 REF.Article

LIQUID DISTRIBUTION IN WETTED SLIT REACTORSKUZELA M; ROUSAR I; CEZNER V et al.1975; COLLECT. CZECHOSL. CHEM. COMMUNIC.; CZECHOSL.; DA. 1975; VOL. 40; NO 7; PP. 2140-2155; BIBL. 16 REF.Article

A SIMPLE METHOD FOR THE CALCULATION OF EFFECTIVENESS FACTORS FOR COMPLEX REACTIONSRAMACHANDRAN PA; KAM EKT; HUGUES R et al.1976; CHEM. ENGNG SCI.; G.B.; DA. 1976; VOL. 31; NO 3; PP. 244-247; BIBL. 6 REF.Article

EVALUATION OF TEMPERATURE PROFILE IN A GAS-SOLIDS REACTING FIXED BED AT CONSTANT WALL TEMPERATUREOLBRICH WO; BHAT GN.1975; HUNGAR. J. INDUSTR. CHEM.; HUNGARY; DA. 1975; VOL. 3; NO 3; PP. 519-526; ABS. RUSSE; BIBL. 3 REF.Article

WALL FLOW IN TRICKLE BED REACTORPRCHLIK J; SOUKUP J; ZAPLETAL V et al.1975; COLLECT. CZECHOSL. CHEM. COMMUNIV.; CZECHOSL.; DA. 1975; VOL. 40; NO 10; PP. 3145-3152; BIBL. 16 REF.Article

BREVET 2.214.516 (B) (7402254). A 23 JANVIER 1974. ENCEINTE DE REFROIDISSEMENT APPROPRIEE POUR ETRE UTILISEE DANS UN REACTEUR A ECOULEMENTsdPatent

BREVET 2.246.303(A1) (7433966). A 9 OCTOBRE 1974. APPAREIL ET PROCEDE POUR ELIMINER LES IMPURETES DES REACTEURS A GARNISSAGEsdPatent

MODEL FOR COAL OXIDATION KINETICS. I: REACTION UNDER CHEMICAL CONTROLKARSNER GG; PERLMUTTER DD.1982; FUEL (GUILDF.); ISSN 0016-2361; GBR; DA. 1982; VOL. 61; NO 1; PP. 29-34; BIBL. 23 REF.Article

EXPERIENCES WITH DYNAMIC ESTIMATORS FOR FIXED-BED REACTORSWALLMAN PH; FOSS AS.1981; IND. ENG. CHEM., FUNDAM.; ISSN 0019-7874; USA; DA. 1981; VOL. 20; NO 3; PP. 234-239; BIBL. 10 REF.Article

RECOVERY OF ELEMENTAL SULPHUR FROM SALADIPURA PYRITES BY THERMAL DECOMPOSITION.SINGH DK; VEERAMANI H; RAO VV et al.1976; INDIAN J. TECHNOL.; INDIA; DA. 1976; VOL. 14; NO 2; PP. 98-101; BIBL. 10 REF.Article

PARTICLE-LIQUID MASS TRANSFER IN A THREE-PHASE FIXED HED REACTOR WITH COCURRENT FLOW IN THE PULSING REGIMELEMAY Y; PINEAULT G; RUETHER JA et al.1975; INDUSTR. ENGNG CHEM., PROCESS DESIGN DEVELOP.; U.S.A.; DA. 1975; VOL. 14; NO 3; PP. 280-285; BIBL. 26 REF.Article

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