Pascal and Francis Bibliographic Databases

Help

Search results

Your search

kw.\*:("TUBULAR REACTOR")

Document Type [dt]

A-Z Z-A Frequency ↓ Frequency ↑
Export in CSV

Publication Year[py]

A-Z Z-A Frequency ↓ Frequency ↑
Export in CSV

Discipline (document) [di]

A-Z Z-A Frequency ↓ Frequency ↑
Export in CSV

Language

A-Z Z-A Frequency ↓ Frequency ↑
Export in CSV

Author Country

A-Z Z-A Frequency ↓ Frequency ↑
Export in CSV

Results 1 to 25 of 1024

  • Page / 41
Export

Selection :

  • and

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

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

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

OPTIMAL SENSOR LOCATIONS FOR TUBULAR-FLOW REACTOR SYSTEMS.COLANTUONI G; PADMANABHAN L.1977; CHEM. ENGNG SCI.; G.B.; DA. 1977; VOL. 32; NO 9; PP. 1035-1049; BIBL. 14 REF.Article

SOLUTION OF THE DIFFERENTIAL EQUATION OF THE DISPERSION TYPE TUBE REACTOR.ARGYELAN J.1977; HUNGR. J. INDUSTR. CHEM.; HUNGARY; DA. 1977; VOL. 5; NO 2; PP. 203-208; ABS. RUSSE; BIBL. 1 REF.Article

EIN ROHRREAKTOR ZUR ABWASSEREINIGUNG. = UN REACTEUR TUBULAIRE POUR L'EPURATION DES EAUX USEESMOSER F.1977; VERFAHR.-TECH.; DTSCH.; DA. 1977; VOL. 11; NO 11; PP. 670-673; BIBL. 23 REF.Article

TUBULAR REACTOR WITH RECYCLE FROM AN INTERMEDIATE POINT: YIELD OF VAN DE VUSSE'S REACTIONS.LEE HH.1977; CHEM. ENGNG SCI.; G.B.; DA. 1977; VOL. 32; NO 5; PP. 562-563; BIBL. 2 REF.Article

AN EXPERIMENTAL STUDY OF INSTABILITY IN A NON-ADIABATIC MULTI-REACTION TUBULAR REACTOR.SCHLEPPY R JR; SHAH YT.1977; CHEM. ENGNG SCI.; G.B.; DA. 1977; VOL. 32; NO 8; PP. 881-887; BIBL. 14 REF.Article

BEHAVIOUR OF TUBULAR REACTORS OF ARBITRARY CROSS-SECTIONTROTTA A; DEL GIUDICE S.1981; TRANS. INST. CHEM. ENG.; ISSN 0046-9858; GBR; DA. 1981; VOL. 59; NO 3; PP. 207-210; BIBL. 9 REF.Article

FLOCKENBILDUNG IN ROHRSTRECKEN = FORMATION DE FLOCS DANS DES SECTIONS TUBULAIRESMEINS W.1980; GAS UND WASSERFACH, WASSER ABWASSER; ISSN 0341-0625; DEU; DA. 1980; VOL. 121; NO 2; PP. 74-78; ABS. ENG; BIBL. 5 REF.Article

BASES TECHNOLOGIQUES DES REACTEURS TUBULAIRES A COURANTS MULTIPLES POUR LA PYROLYSE SELECTIVEGORISLAVETS SP; DMITRIEV VM.1980; HIM. TEHNOL. (KIEV, 1971); ISSN 0368-556X; SUN; DA. 1980; VOL. 114; NO 6; PP. 33-36; BIBL. 9 REF.Article

REAKTIONSTECHNIK PHOTOCHEMISCHER PROZESSE. V. EIN- UND ZWEIDIMENSIONALE MODELLIERUNG VON PHOTOROHRREAKTOREN - MODELLGRUNDLAGEN = TECHNIQUE REACTIONNELLE DES PROCESSUS PHOTOCHIMIQUES. V. MODELISATION A UNE ET DEUX DIMENSIONS DES PHOTOREACTEURS TUBULAIRES. BASES DU MODELETHIELE R; VOSS H; MUELLER WD et al.1980; CHEM. TECH.; DDR; DA. 1980; VOL. 32; NO 2; PP. 67-70; BIBL. 17 REF.Article

EXPERIMENTAL OBSERVATION OF MULTIPLE STEADY STATES AND TEMPERATURE FIELDS IN A LABORATORY TUBULAR REACTORMIKUS O; PUSZYNSKI J; HLAVACEK V et al.1979; CHEM. ENGNG. SCI.; GBR; DA. 1979; VOL. 34; NO 3; PP. 434-436; BIBL. 5 REF.Article

ABGASREINIGUNG DURCH TERMISCHE VERBRENNUNG. II. THERMISCHE ABLUFTVERBRENNUNG MIT INDIREKTER BEHEIZUNG. = EPURATION DES EFFLUENTS GAZEUX PAR INCINERATION THERMIQUE. II. INCINERATION THERMIQUE DES EFFLUENTS GAZEUX PAR CHAUFFAGE INDIRECTMEIER ZU KOCKER H.1978; STAUB, REINFALTG LUFT; DTSCH.; DA. 1978; VOL. 38; NO 5; PP. 167-172; ABS. ANGL. FR.; BIBL. 5 REF.Article

INFLUENCE DE L'APTITUDE A L'ACCUMULATION DE CHALEUR DES PAROIS SUR LA DYNAMIQUE D'UN REACTEUR TUBULAIREVOL'TER BV; SVIRIDOV VN; SOFIEV A EH et al.1978; TEOR. OSNOVY KHIM. TEKHNOL.; SUN; DA. 1978; VOL. 12; NO 4; PP. 529-539; BIBL. 13 REF.Article

DIFFUSION AND REACTION IN TUBULAR REACTOR WITH NON-NEWTONIAN LAMINAR FLOW.NIGAM KDP; VASUDEVA K.1977; CHEM. ENGNG SCI.; G.B.; DA. 1977; VOL. 32; NO 6; PP. 673-677; BIBL. 26 REF.Article

EIN BEITRAG ZUR DIMENSIONIERUNG VON LOCHPLATTENEINBAUTEN IN ROHRREAKTOREN ZUR ERZIELUNG EINES MOEGLICHST PFROPFENSTROEMUNGSAEHNLICHEN VERWEILZEITVERHALTENS. = CONTRIBUTION AU DIMENSIONNEMENT DES DISQUES PERFORES DANS LES REACTIONS TUBULAIRES POUR LA REALISATION DE COMPORTEMENT DE TEMPS DE SEJOUR AUSSI PROCHE QUE POSSIBLE D'UN ECOULEMENT AVEC TEMPS DE SEJOUR UNIFORMENAUE G; FRIEDEMANN I.1977; CHEM. TECH.; DTSCH.; DA. 1977; VOL. 29; NO 9; PP. 485-488; BIBL. 3 REF.Article

  • Page / 41