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Results 1 to 25 of 132

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DESIGN AND OPTIMIZATION OF A TUBE-WALL REACTORSMITH TG; CARBERRY JJ.1975; CHEM. ENGNG SCI.; G.B.; DA. 1975; VOL. 30; NO 2; PP. 221-227; BIBL. 13 REF.Article

SURFACE-CATALYZED REACTIONS IN TURBULENT PIPE FLOWSRANDHAVA SS; WASAN DT.1972; ADV. CHEM. SER.; U.S.A.; DA. 1972; VOL. 109; PP. 564-568; BIBL. 6 REF.Serial Issue

DYNAMICS OF A TUBE-WALL REACTOR.SMITH TG; CARBERRY JJ.1976; CHEM. ENGNG SCI.; G.B.; DA. 1976; VOL. 31; NO 11; PP. 1071-1076; BIBL. 6 REF.Article

SURFACE REACTION WITH COMBINED FORCED AND FREE CONVECTIONCHING YUAN CHANG; GUIN JA; ROBERTS LD et al.1976; A.I.CH.E. J., NEW YORK; U.S.A.; DA. 1976; VOL. 22; NO 2; PP. 252-259; BIBL. 18 REF.Article

AN ANALYSIS OF WALL-SUPPORTED CATALYST STRUCTURESSENKAN SM; EVANS LB; HOWARD JB et al.1979; INDUSTR. ENGNG CHEM., PROCESS DESIGN DEVELOP.; USA; DA. 1979; VOL. 18; NO 1; PP. 125-130; BIBL. 10 REF.Article

LE PROBLEME DE LA SIMULATION COMPLETE DES FLUX THERMIQUES STATIONNAIRES DANS L'ECOULEMENT SUB- ET HYPERSONIQUE SUR DES SURFACES CATALYTIQUESAGAFONOV VP; KUZNETSOV MM.1980; CHISLENN. METODY MEKH. SPLOSHN. SREDY; SUN; DA. 1980; VOL. 11; NO 7; PP. 5-11; BIBL. 4 REF.Article

EFFECT OF SURFACE CATALYTIC ACTIVITY ON STAGNATION HEAT-TRANSFER RATESANDERSON LA.1973; A.I.A.A. J., NEW YORK; U.S.A.; DA. 1973; VOL. 11; NO 5; PP. 649-656; BIBL. 46 REF.Serial Issue

TRANSIENT BEHAVIOUR OF A WALL-CATALYSED TUBULAR FLOW REACTORRAGHURAMAN J.1973; INDIAN CHEM. ENGR; INDIA; DA. 1973; VOL. 15; NO 4; PP. 12-17; BIBL. 12 REF.Article

YIELD OPTIMIZATION IN A TUBE-WALL REACTORTA JEN HUANG D; VARMA A.1980; A.C.S. SYMP. SER.; ISSN 0097-6156; USA; DA. 1980; NO 124; PP. 469-480; BIBL. 9 REF.Article

AN ANALYSIS OF THE TUBE-WALL REACTOR UNDER DIFFUSION LIMITING CONDITIONSSENKAN SM; EVANS LB; HOWARD JB et al.1976; INDUSTR. ENGNG CHEM., PROCESS DESIGN DEVELOP.; U.S.A.; DA. 1976; VOL. 15; NO 1; PP. 184-187; BIBL. 21 REF.Article

DISPERSION APPROXIMATIONS TO THE MULTICOMPONENT CONVECTIVE DIFFUSION EQUATION FOR CHEMICALLY ACTIVE SYSTEMSJOHNS LE; DEGANGE AE.1975; CHEM. ENGNG SCI.; G.B.; DA. 1975; VOL. 30; NO 9; PP. 1065-1067; BIBL. 8 REF.Article

HOMOGENEOUS MODELS FOR POROUS CATALYSTS AND TUBULAR REACTORS WITH HETEROGENEOUS REACTIONSGILL WN; RUCKENSTEIN E; HSIEH HP et al.1975; CHEM. ENGNG SCI.; G.B.; DA. 1975; VOL. 30; NO 7; PP. 685-694; BIBL. 21 REF.Article

TUBE-WALL CATALYTIC REACTOR COOLED BY AN ANNULAR HEAT PIPEPARENT YO; CARAM HS; COUGHLIN RW et al.1983; AICHE JOURNAL; ISSN 0001-1541; USA; DA. 1983; VOL. 29; NO 3; PP. 443-451; BIBL. 17 REF.Article

UNSTEADY CONVECTIVE DIFFUSION IN AN ANNULAR CATALYTIC REACTOR.SHANKAR SUBRAMANIAN R; SHIMALLIS BERHE.1976; CHEM. ENGNG SCI.; G.B.; DA. 1976; VOL. 31; NO 11; PP. 1005-1017; BIBL. 25 REF.Article

DC GLOW DISCHARGE IN A TUBE WITH THE WALLS OF A DIFFERENT CATALYTIC ACTIVITYMASEK K; LASKA L.1980; CZECH. J. PHYS.; ISSN 0011-4626; CSK; DA. 1980; VOL. 30; NO 7; PP. 805-815; BIBL. 25 REF.Article

THE OXYDATION OF ETHENE IN AN EMPTY AND PACKED TUBULAR WALL REACTOR OPERATING IN THE REACTION- AND DIFFUSION-CONTROLLED REGIMESBOERSMA MAM; SPIERTS JAM; VAN LITH WJG et al.1980; CHEM. ENG. J.; ISSN 0300-9467; CHE; DA. 1980; VOL. 20; NO 3; PP. 177-183; BIBL. 26 REF.Article

THEORIE ASYMPTOTIQUE D'UNE COUCHE HORS D'EQUILIBRE CHIMIQUE AU VOISINAGE D'UNE PAROI CATALYTIQUE PARFAITEBENILOV MS; TIRSKIJ GA.1980; PRIKL. MAT. MEKH.; SUN; DA. 1980; VOL. 44; NO 2; PP. 281-289; BIBL. 12 REF.Article

EQUATIONS DE TRANSPORT PRES DES SURFACES CATALYTIQUESMARKEEV BM.1979; ZH. TEKH. FIZ.; SUN; DA. 1979; VOL. 49; NO 6; PP. 1145-1152; BIBL. 14 REF.Article

AN EXPLICIT METHOD OF DESIGN OF NON-ISOTHERMAL TUBE-WALL REACTOR WITH VOLUME CHANGEGOYAL SK; ESMAIL MN; BAKHSHI NN et al.1982; CAN. J. CHEM. ENG.; ISSN 0008-4034; CAN; DA. 1982; VOL. 60; NO 5; PP. 627-634; ABS. FRE; BIBL. 2 P.Article

CONDITIONS AUX LIMITES THERMIQUES POUR LES ELECTRONS DANS UN GAZ FAIBLEMENT IONISE AUTOUR D'UNE PAROI CATALYTIQUECHEKMAREV IB.1981; Z. TEH. FIZ.; ISSN 0044-4642; SUN; DA. 1981; VOL. 51; NO 8; PP. 1601-1606; BIBL. 9 REF.Article

KINETICS OF THE CATALYTIC AIR-OXIDATION OF O-XYLENE MEASURED IN A TUBE-WALL-CATALYTIC REACTORCHANDRASEKHARAN K; CALDERBANK PH.1980; CHEM. ENGNG SCI.; GBR; DA. 1980; VOL. 35; NO 7; PP. 1523-1535; BIBL. 35 REF.Article

ANALYSIS AND DESIGN OF CATALYST-COATED FINS/SPINESSENKAM SM.1980; IND. ENG. CHEM., PROCESS DES. DEV.; ISSN 0019-7882; USA; DA. 1980; VOL. 19; NO 4; PP. 680-688; BIBL. 18 REF.Article

EFFICACITE DES REACTEURS ET ECHANGEURS LIMITES PAR LE TRANSFERT DIFFUSIONNEL VERS LA PAROI.VILLERMAUX J; HOUZELOT JL.1977; ACTUAL. CHIM.; FR.; DA. 1977; PP. 18-21Article

INFLUENCE DE PROCESSUS DE TRANSPORT DANS UNE SOUS-COUCHE LAMINAIRE SUR LE FROTTEMENT ET L'ECHANGE DE CHALEUR DANS UNE COUCHE LIMITE TURBULENTE HORS D'EQUILIBRE AVEC DISSOCIATIONKOJCHEV YU N; CHUMAKOV YU S.1974; IZVEST. AKAD. NAUK S.S.S.R., MEKH. ZHIDKOSTI GAZA; S.S.S.R.; DA. 1974; NO 3; PP. 114-119; BIBL. 7 REF.Article

Reformulation and numerical solution of the equations for a catalytic porous wall gas-liquid reactorAKYURTLU, A; AKYURTLU, J. F; HAMRIN, C. E. JR et al.Computers & chemical engineering. 1986, Vol 10, Num 4, pp 361-365, issn 0098-1354Article

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