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Results 1 to 25 of 20378

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DYNAMICS OF LIQUID -SOLID SEMIFLUIDIZATION. III. RELATION BETWEEN ONSET OF SEMIFLUIDIZATION AND MINIMUM FLUIDIZATION VELOCITYROY GK; SARMA KJR.1972; CHEM. ENGNG J.; G.B.; DA. 1972; VOL. 4; NO 3; PP. 294-296; BIBL. 3 REF.Serial Issue

TRANSITION BETWEEN PARTICULATE AND AGGREGATIVE FLUIDIZATION AT DIFFERENT STATE-OF-FLOW OF THE SOLIDSDOICHEV K; TODOROV S; DIMITROV V et al.1975; CHEM. ENG SCI.; G.B.; DA. 1975; VOL. 30; NO 4; PP. 419-424; BIBL. 17 REF.Article

ENERGIE DES SYSTEMES FLUIDISES HOMOGENES ET HETEROGENESDOJCHEV K.1972; GOD. VISSH. KHIM.-TEKHNOL. INST., SOFIJA; BALG.; DA. 1972; VOL. 19; NO 3; PP. 91-99; ABS. RUSSE ANGL.; BIBL. 13 REF.Article

DESCRIPTION GLOBALE DE LA FLUIDISATIONGOOSSENS WRA; HELLINCKY L.1973; CHIM. INDUSTR., GENIE CHIM.; FR.; DA. 1973; VOL. 106; NO 4; PP. 309-311; ABS. ANGL.; BIBL. 18 REF.Serial Issue

PREDICTION DE LA STRUCTURE DES LITS FLUIDISES POUR DIFFERENTS ETATS D'ECOULEMENT DES PARTICULES SOLIDESDOJCHEV K; DIMITROV V; TODOROV S et al.1975; FOD. VISSH. KHIM.-TEKHNOL. INST., SOFIJA; GBR; DA. 1975 PUBL. 1977; VOL. 22; NO 2; PP. 195-204; ABS. RUS/ENG; BIBL. 14 REF.Article

PREDICTION OF SEMI-FLUIDIZATION VELOCITY OF IRREGULAR PARTICLES IN LIQUID-SOLID SYSTEMROY GK; SARMA KJR.1975; CHEM. ENGNG WORLD.; INDIA; DA. 1975; VOL. 10; NO 5; PP. 85-86; BIBL. 3 REF.Article

CRITERION FOR INITIAL CONTRACTION OR EXPANSION OF THREE-PHASE FLUIDIZED BEDS.EPSTEIN N.1976; CANAD. J. CHEM. ENGNG; CANADA; DA. 1976; VOL. 54; NO 4; PP. 259-263; BIBL. 14 REF.Article

CHARACTERISTICS OF LARGE TWO-DIMENSIONAL AIR BUBBLES IN LIQUIDS AND IN THREE-PHASE FLUIDISED BEDSHENRIKSEN HK; OSTERGAARD K.1974; CHEM. ENGNG J.; G.B.; DA. 1974; VOL. 7; NO 2; PP. 141-146; BIBL. 19 REF.Article

TRANSITION ENTRE FLUIDISATION HOMOGENE ET FLUIDISATION HETEROGENE AU COURS DE L'EXPANSION DU LIT FLUIDISEDOJCHEV K; DIMITROV V; TODOROV S et al.1975; FOD. VISSH. KHIM.-TEKHNOL. INST., SOFIJA; BGR; DA. 1975 PUBL. 1977; VOL. 22; NO 2; PP. 205-212; ABS. RUS/ENG; BIBL. 15 REF.Article

HOLD-UP AND AXIAL MIXING CHARACTERISTICS OF TWO AND THREE PHASE FLUIDIZED BEDSKIM SD; BACKER CGJ; BERGOUGNOU MA et al.1972; CANAD. J. CHEM. ENGNG; CANADA; DA. 1972; VOL. 50; NO 6; PP. 695-701; ABS. FR.; BIBL. 22 REF.Serial Issue

DEBUT DE FLUIDISATION DANS LES APPAREILS CONIQUESBUEVICH YU A; EHLLENGORN SM.1978; INZHENER.-FIZ. ZH., BELORUS. S.S.R.; S.S.S.R.; DA. 1978; VOL. 34; NO 2; PP. 221-229; ABS. ANGL.; BIBL. 14 REF.Article

ONSET OF FLUIDIZATION AND SLUGGING IN BEDS OF UNIFORM PARTICLESBROADHURST TE; BECKER HA.1975; A.I.CH.E.J., NEW YORK; U.S.A.; DA. 1975; VOL. 21; NO 2; PP. 238-247; BIBL. 14 REF.Article

THE PARTICULATE-AGGREGATIVE TRANSITION CRITERION IN FLUIDISED BEDSCREASY DE.1973; POWDER TECHNOL.; SWITZ.; DA. 1973; VOL. 7; NO 6; PP. 353-354; BIBL. 8 REF.Serial Issue

THE USE OF THREE PHASE FLUIDIZATION IN THE RECTIFICATION PROCESSKOMOROWICZ T; LASZUK A; MROWIEC M et al.1977; NAFTA; POLSKA; DA. 1977; VOL. 33; NO 12; PP. 423-427; ABS. RUSSE ANGL.; BIBL. 16 REF.Article

MIXING PROCESSES IN LIQUID FLUIDIZED BEDSRITZMANN H; HOFFMANN G; SCHUGERL K et al.1972; POWDER TECHNOL.; SWITZ.; DA. 1972; VOL. 6; NO 4; PP. 225-230; BIBL. 20 REF.Serial Issue

TYPES OF GAS FLUIDIZATIONGELDART D.1973; POWDER TECHNOL.; SWITZ.; DA. 1973; VOL. 7; NO 5; PP. 285-292; BIBL. 38 REF.Serial Issue

FLUIDDYNAMISCHE UNTERSUCHUNGEN EINER MEHRSTUFIGEN DREIPHASENWIRBELSCHICHT = RECHERCHES SUR LA DYNAMIQUE DES FLUIDES DANS UN LIT FLUIDISE A 3 PHASES ET PLUSIEURS ETAGESSCHMIDT M.1973; CHEM.-INGR-TECH.; DTSCH.; DA. 1973; VOL. 45; NO 6; PP. 377-378; BIBL. 4 REF.Serial Issue

PREDICTION OF THE PACKED BED HEIGHT IN GAS-SOLID SEMIFLUIDIZATIONROY GK; SEN GUPTA P.1974; INDUSTR. ENGNG CHEM., PROCESS DESIGN DEVELOP.; U.S.A.; DA. 1974; VOL. 13; NO 3; PP. 219-221; BIBL. 12 REF.Article

TRANSFERT DE MASSE A LA PAROI DES LITS FLUIDISES LIQUIDESITO R; KOMAGAWA Y; OMODAKA K et al.1973; KAGAKU KOGAKU; JAP.; DA. 1973; VOL. 35; NO 5; PP. 497-503; ABS. ANGL.; BIBL. 20 REF.Serial Issue

BED EXPANSION CHARACTERISTICS OF ANNULAR LIQUID-FLUIDIZED BEDSRAMAMURTHY K; SUBBARAJU K.1973; INDUSTR. ENGNG CHEM., PROCESS DESIGN DEVELOP.; U.S.A.; DA. 1973; VOL. 12; NO 2; PP. 184-189; BIBL. 10 REF.Serial Issue

INSTABILITY WAVES AND THE ORIGIN OF BUBBLES IN FLUIDIZED BEDSEL KAISSY MM; HOMSY GM.1976; INTERNATION. J. MULTIPHASE FLOW; G.B.; DA. 1976; VOL. 2; NO 4; PP. 379-395; BIBL. 18 REF.Article

A FEW COMMENTS ON PARTICLE TO LIQUID MASS TRANSFER IN FLUIDIZED BEDLAGUERIE C; ANGELINO H.1975; CHEM. ENGNG SCI.; G.B.; DA. 1975; VOL. 30; NO 12; PP. 1525-1526; BIBL. 5 REF.Article

RELATIONSHIP BETWEEN THE ONSET OF SEMI-FLUIDIZATION VELOCITY & THE MINIMUM FLUIDIZATION VELOCITYROY GK; SENGUPTA P.1972; INDIAN J. TECHNOL.; INDIA; DA. 1972; VOL. 10; NO 11; PP. 397-399; BIBL. 9 REF.Serial Issue

THE SIZE DISTRIBUTION OF GAS BUBBLES LEAVING A THREE-PHASE FLUIDIZED BEDPAGE RE; HARRISON D.1972; POWDER TECHNOL.; SWITZ.; DA. 1972; VOL. 6; NO 4; PP. 245-249; BIBL. 10 REF.Serial Issue

STABILITY OF BUBBLES IN FLUIDIZED BEDSBHATIA VK; CLIFT R; GRACE JR et al.1976; INDUSTR. ENGNG CHEM., FUNDAM.; U.S.A.; DA. 1976; VOL. 15; NO 1; PP. 86-87; BIBL. 4 REF.Article

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