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kw.\*:("TUBULAR REACTOR")

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SURFACE EFFECTS DURING PYROLYSIS OF ETHANE IN TUBULAR FLOW REACTORS.DUNHLEMAN JJ; ALBRIGHT LF.1976; A.C.S. SYMP. SER.; U.S.A.; DA. 1976; VOL. 32; PP. 241-260; BIBL. 19 REF.; (IND. LAB. PYROLYSES. SYMP. CHEM. CONGR. NORTH AM. CONT. 1. MEET. AM. CHEM. SOC. 169; MEXICO CITY, PHILADELPHIA; 1975)Conference Paper

BREVET INSTALLATION D'EPURATION D'EAUX RESIDUAIRES1978; ; FRA; DA. 1978-11-17; FR/A1/2.383.887; DEP.77-08299/1977-03-18Patent

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

BREVET 2.336.174 (A1) (76 39051). - 24 DECEMBRE 1976. PROCEDE ET APPAREIL POUR EXECUTER UNE REACTION CHIMIQUE FAISANT INTERVENIR UNE PHASE GAZEUSE.sdPatent

NEW CAT REFORMER DESIGN TESTEDFROMAGER MH; PATOUILLET JJ.1979; HYDROCARBON PROCESSG; USA; DA. 1979; VOL. 58; NO 4; PP. 171-172Article

PYROLYSIS OF GASOLINE RAFFINATE IN A NEW TYPE MULTIDIRECTIONAL TUBULAR REACTOR WORKING CONTINUOUSLYGORISLAVETS SP; DMITRIEV VM.1981; NEFTEPERERAB. NEFTEHIM. (MOSK.); ISSN 0028-1190; SUN; DA. 1981; NO 5; PP. 27-30Article

PYROLYSIS OF PROPANE IN TUBULAR FLOW REACTORS CONSTRUCTED OF DIFFERENT MATERIALS.DUNKLEMAN JJ; ALBRIGHT LF.1976; A.C.S. SYMP. SER.; U.S.A.; DA. 1976; VOL. 32; PP. 261-273; BIBL. 12 REF.; (IND. LAB. PYROLYSES. SYMP. CHEM. CONGR. NORTH AM. CONT. 1. MEET. AM. CHEM. SOC. 169; MEXICO CITY, PHILADELPHIA; 1975)Conference Paper

PYROLYSIS OF HYDROCARBON BASE PRODUCT IN A TUBULAR REACTOR WORKING BY CONTACTAVERKIEVA VI; KATS NG; OSTROVSKIJ GM et al.1981; NEFTEPERERAB. NEFTEHIM., (MOSK.); ISSN 0028-1190; SUN; DA. 1981; NO 6; PP. 34-35Article

WASSERSTOFF-PERMEATION DURCH ROHRREAKTORWAENDE BEI DER METHAN-DAMPFREFORMIERUNG = HYDROGEN PERMEATION THROUGH THE TUBE REACTOR WALL IN THE METHANE STEAM REFORMING = PERMEATION DE L'HYDROGENE A TRAVERS LA PAROI D'UN REACTEUR TUBULAIRE DANS LE REFORMAGE A LA VAPEUR DU METHANERIENSCHE E.1980; VDI-BER.; ISSN 0083-5560; DEU; DA. 1980; NO 391; PP. 322-335; BIBL. 10 REF.Article

FLOW STABILITY OF MULTITUBULAR CONTINUOUS POLYMERIZATION REACTORSJOOSTEN GEH; HOOGSTRATEN HW; OUWERKERK C et al.1981; IND. ENG. CHEM., PROCESS DES. DEV.; ISSN 0019-7882; USA; DA. 1981; VOL. 20; NO 2; PP. 177-182; BIBL. 11 REF.Article

PYROLYSIS IN A REACTION COIL WITH AN ANNULAR SPACESTEPANOV AV; ZELENTSOV VV; SUL'ZHIK NI et al.1981; HIM. TEHNOL. (KIEV, 1971); ISSN 0368-556X; SUN; DA. 1981; NO 1; PP. 17-18Article

CONTROL OF TEMPERATURE PEAKS IN ADIABATIC FIXED-BED TUBULAR REACTORSGIGER GK; MUTHARASAN R; COUGHANOWR DR et al.1980; IND. ENG. CHEM., FUNDAM.; ISSN 0196-4313; USA; DA. 1980; VOL. 19; NO 4; PP. 389-396; BIBL. 19 REF.Article

STABILITY OF HYPERBOLIC REACTORSRETI P.1980; REACT. KINET. CATAL. LETT.; ISSN 0304-4122; NLD; DA. 1980; VOL. 15; NO 2; PP. 215-220; ABS. RUS; BIBL. 6 REF.Article

EFFICACITE ET QUALITE DE FONCTIONNEMENT D'UN REACTEUR CONTINU IDEALBELOGLAZOV IN.1980; Z. PRIKL. HIM.; ISSN 0044-4618; SUN; DA. 1980; VOL. 53; NO 9; PP. 2011-2015; BIBL. 4 REF.Article

FLASH HYDROPYROLYSIS FOR HIGH-VALUE PRODUCTSOBERG CL; FALK AY; SILVERMAN J et al.1979; COAL PROCESSING TECHNOLOGY; USA; NEW YORK: AMER. INST. CHEM. ENG.; DA. 1979; VOL. 5; PP. 182-183Book Chapter

LOW-CONSISTENCY OXYGEN DELIGNIFICATION IN A PIPELINE REACTOR. A PILOT STUDY.KIRK BS; KIRSCHNER MJ; TSENG JK et al.1978; T.A.P.P.I.; U.S.A.; DA. 1978; VOL. 61; NO 5; PP. 77-80; BIBL. 6 REF.Article

REGIME AUTOVIBRATOIRE DU DEVELOPPEMENT DES REACTIONS EXOTHERMIQUES DANS UN REACTEUR TUBULAIREBUTAKOV AA; SHKADINSKIJ KG.1978; DOKL. AKAD. NAUK S.S.S.R.; S.S.S.R.; DA. 1978; VOL. 238; NO 1; PP. 166-169; BIBL. 7 REF.Article

MODELLING OF COMMERCIAL OXIDATION REACTORS ACCOUNTING FOR MASS TRANSFER EFFECTS.PALMER DA.1977; CANAD. J. CHEM. ENGNG; CANADA; DA. 1977; VOL. 55; NO 5; PP. 626-628; BIBL. 21 REF.Article

STUDIES IN THE CONTROL OF TUBULAR REACTORS. II. STABILIZATION BY MODAL CONTROL.GEORGAKIS C; ARIS R; AMUNDSON NR et al.1977; CHEM. ENGNG SCI.; G.B.; DA. 1977; VOL. 32; NO 11; PP. 1371-1379; BIBL. 11 REF.Article

BOUNDS ON THE STEADY STATE CONCENTRATION AND TEMPERATURE IN A TUBULAR REACTOR.VARMA A.1977; CANAD. J. CHEM. ENGNG; CANADA; DA. 1977; VOL. 55; NO 5; PP. 629-632; BIBL. 7 REF.Article

VARIABLE MEASUREMENT STRUCTURES FOR THE CONTROL OF A TUBULAR REACTORALVAREZ J; ROMAGNOLI JA; STEPHANOPOULOS G et al.1981; CHEM. ENG. SCI.; ISSN 0009-2509; GBR; DA. 1981; VOL. 36; NO 10; PP. 1695-1712; BIBL. 41 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

MODELAREA REACTORULUI DE REFORMARE PRIMARA A METANULUI. II: DETERMINAREA COEFICIENTULUI DE TRANSFER DE CALDURA = REACTOR MODELING FOR THE PRIMARY METHANE REFORMING. II. DETERMINATION OF THE HEAT TRANSFER COEFFICIENT KT = MODELISATION DU REACTEUR DE REFORMAGE PRIMAIRE DU METHANE. II. DETERMINATION DU COEFFICIENT DE TRANSFERT DE CHALEUR KTSIMINICEANU I; CALISTRU C.1980; BUL. INST. POLITECH. IASI, 4; ISSN 0373-3262; ROM; DA. 1980; VOL. 26; NO 1-2; PP. 59-65; ABS. ENG; BIBL. 11 REF.Article

APPLICATION OF GALERKIN TECHNIQUE TO DIFFUSION PROBLEMS IN TUBULAR REACTORNIGAM KM; NIGAM KDP.1980; CHEM. ENG. SCI.; ISSN 0009-2509; GBR; DA. 1980; VOL. 35; NO 11; PP. 2358-2360; BIBL. 15 REF.Article

STABILITY OF CHEMICAL REACTORSOROSKAR A; STERN SA.1979; A.I.CH.E.J., NEW YORK; USA; DA. 1979; VOL. 25; NO 5; PP. 903-905; BIBL. 3 REF.Article

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