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HEAT EFFECTS IN GAS ABSORPTION ACCOMPANIED BY A RAPID FIRST-ORDER REACTION IN TURBULENT LIQUID FILMSSANDALL OC.1975; CANAD. J. CHEM. ENGNG; CANADA; DA. 1975; VOL. 53; NO 6; PP. 702-705; BIBL. 6 REF.Article

GAS ABSORPTION ACCOMPANIED BY AN IRREVERSIBLE SECOND-ORDER REACTION IN TURBULENT LIQUIDSNOMAN HAIMOUR; SANDALL OC.1983; AICHE JOURNAL; ISSN 0001-1541; USA; DA. 1983; VOL. 29; NO 2; PP. 277-281; BIBL. 12 REF.Article

LOW REYNOLDS NUMBER HEAT TRANSFER TO NON-NEWTONIAN FLUIDS IN ANCHOR-AGITATED VESSELSHEINLEIN HW; SANDALL OC.1972; INDUSTR. ENGNG CHEM., PROCESS DESIGN DEVELOP.; U.S.A.; DA. 1972; VOL. 11; NO 4; PP. 490-495; BIBL. 10 REF.Serial Issue

LIQUID PHASE MASS TRANSFER RESISTANCE IN A SMALL SCALE PACKED DISTILLATION COLUMNARWIKAR KJ; SANDALL OC.1980; CHEM. ENG. SCI.; ISSN 0009-2509; GBR; DA. 1980; VOL. 35; NO 11; PP. 2337-2343; BIBL. 20 REF.Article

LARGE SCHMIDT NUMBER MASS TRANSFER IN TURBULENT PIPE FLOWSANDALL OC; HANNA OT.1979; A.I.CH.E.J. NEW YORK; USA; DA. 1979; VOL. 25; NO 1; PP. 190-192; BIBL. 6 REF.Article

GAS ABSORPTION ACCOMPANIED BY A SECOND-ORDER CHEMICAL REACTION MODELED ACCORDING TO THE DANCKWERTS SURFACE RENEWAL THEORY.MATHERON ER; SANDALL OC.1978; A.I.CH.E. J., NEW YORK; U.S.A.; DA. 1978; VOL. 24; NO 3; PP. 552-554; BIBL. 3 REF.Article

EFFECTIVE INTERFACIAL AREA DETERMINATION BY GAS ABSORPTION ACCOMPANIED BY SECOND-ORDER IRREVERSIBLE CHEMICAL REACTIONMATHERON ER; SANDALL OC.1979; A.I.CH.E.J., NEW YORK; USA; DA. 1979; VOL. 25; NO 2; PP. 332-338; BIBL. 16 REF.Article

GAS ABSORPTION INTO A TURBULENT LIQUIDLAMOURELLE AP; SANDALL OC.1972; CHEM. ENGNG SCI.; G.B.; DA. 1972; VOL. 27; NO 5; PP. 1035-1043; ABS. FR. ALLEM.; BIBL. 34 REF.Serial Issue

SIMULTANEOUS HEAT AND MASS TRANSFER FOR MULTICOMPONENT DISTILLATION IN A WETTED-WALL COLUMNDRIBIKA MM; SANDALL OC.1979; CHEM. ENGNG SCI.; GBR; DA. 1979; VOL. 34; NO 5; PP. 733-739; BIBL. 15 REF.Article

SIMULTANEOUS HEAT AND MASS TRANSFER IN A PACKED BINARY DISTILLATION COLUMN.HONORAT A; SANDALL OC.1978; CHEM. ENGNG SCI.; G.B.; DA. 1978; VOL. 33; NO 6; PP. 635-640; BIBL. 8 REF.Article

GAS ABSORPTION BY NON-NEWTONIAN FLUIDS IN AGITATED VESSELSPEREZ JF; SANDALL OC.1974; A.I.CH.E.J., NEW YORK; U.S.A.; DA. 1974; VOL. 20; NO 4; PP. 770-775; BIBL. 17 REF.Article

HEAT TRANSFER IN TURBULENT PIPE FLOW FOR LIQUIDS HAVING A TEMPERATURE-DEPENDENT VISCOSITYHANNA OT; SANDALL OC.1978; J. HEAT TRANSFER; USA; DA. 1978; VOL. 100; NO 2; PP. 224-229; BIBL. 12 REF.Article

ENTRANCE EFFECTS IN LIQUID FILM FLOWAULT JW; SANDALL OC.1972; CANAD. J. CHEM. ENGNG; CANADA; DA. 1972; VOL. 50; NO 3; PP. 318-322; ABS. FR.; BIBL. 8 REF.Serial Issue

TURBULENT HEAT TRANSFER IN A CIRCULAR TUBE WITH VISCOUS DISSIPATIONHANNA OT; SANDALL OC.1982; CHEM. ENG. COMMUN.; ISSN 0098-6445; USA; DA. 1982; VOL. 18; NO 1-4; PP. 163-172; BIBL. 14 REF.Article

DIFFUSION COEFFICIENTS FOR HELIUM, HYDROGEN, AND CARBON DIOXIDE IN WATER AT 25OCMAZAREI AF; SANDALL OC.1980; A.I. CH. E.J., NEW YORK; USA; DA. 1980; VOL. 26; NO 1; PP. 154-157; BIBL. 24 REF.Article

DIFFUSION COEFFICIENTS FOR OXYGEN AND CARBON DIOXIDE IN WATER AT 25OC BY UNSTEADY STATE DESORPTION FROM A QUIESCENT LIQUIDTSE FC; SANDALL OC.1979; CHEM. ENGNG COMMUNIC.; GBR; DA. 1979; VOL. 3; NO 3; PP. 147-153; BIBL. 14 REF.Article

GAS ABSORPTION ACCOMPANIED BY INSTANTANEOUS BIMOLECULAR REACTION IN TURBULENT LIQUIDSMENDEZ F; SANDALL OC.1975; A.I. CH. E.J., NEW YORK; U.S.A.; DA. 1975; VOL. 21; NO 3; PP. 534-540; BIBL. 15 REF.Article

SIMULTANEOUS HEAT AND MASS TRANSFER IN BINARY DISTILLATION. I. THEORYKAYIHAN F; SANDALL OC; MELLICHAMP DA et al.1975; CHEM. ENGNG SCI.; G.B.; DA. 1975; VOL. 30; NO 11; PP. 1333-1339; BIBL. 19 REF.Article

COMPARISON OF EFFECTIVE INTERFACIAL AREAS WITH THE ACTUAL CONTACT AREA FOR GAS ABSORPTION IN AN AGITATED VESSELNGEE SIEW KON; SANDALL OC.1978; CANAD. J. CHEM. ENGNG; CAN; DA. 1978; VOL. 56; NO 6; PP. 685-689; ABS. FRE; BIBL. 12 REF.Article

SIMULTANEOUS HEAT AND MASS TRANSFER IN BINARY DISTILLATION. II. EXPERIMENTAL.FERHAN KAYIHAN; SANDALL OC; MELLICHAMP DA et al.1977; CHEM. ENGNG SCI.; G.B.; DA. 1977; VOL. 32; NO 7; PP. 747-754; BIBL. 11 REF.Article

A NEW THEORETICAL FORMULA FOR TURBULENT HEAT AND MASS TRANSFER WITH GASES OR LIQUIDS IN TUBE FLOWSANDALL OC; HANNA OT; MAZET PR et al.1980; CAN. J. CHEM. ENG.; ISSN 0008-4034; CAN; DA. 1980; VOL. 58; NO 4; PP. 443-447; ABS. FRE; BIBL. 16 REF.Article

HEAT EFFECTS FOR PHYSICAL AND CHEMICAL ABSORPTION IN TURBULENT LIQUID FILMSSANDALL OC; HANNA OT; VALERI FJ et al.1982; CHEM. ENG. COMMUN.; ISSN 0098-6445; USA; DA. 1982; VOL. 16; NO 1-6; PP. 135-147; BIBL. 12 REF.Article

TURBULENT NON-NEWTONIAN TRANSPORT IN A CIRCULAR TUBE.SANDALL OC; HANNA OT; GELIBTER M et al.1976; A.I.CH.E.J., NEW YORK; U.S.A.; DA. 1976; VOL. 22; NO 6; PP. 1142-1145; BIBL. 10 REF.Article

A NEW THEORETICAL FORMULA FOR TURBULENT HEAT AND MASS TRANSFER WITH GASES OR LIQUIDS IN TUBE FLOWSANDALL OC; HANNA OT; MAZET PR et al.1980; CANADIAN CHEMICAL ENGINEERING CONFERENCE. 30. NATIONAL HEAT TRANSFER SYMPOSIUM/1980/EDMONTON AB; CAN; DA. 1980; PP. 681-689; BIBL. 16 REF.Conference Paper

THERMAL ENTRANCE LENGTHS FOR LAMINAR FLOW IN VARIOUS DUCTS FOR CONSTANT SURFACE HEAT FLUX. = LONGUEURS D'ENTREE THERMIQUE POUR UN ECOULEMENT LAMINAIRE DANS DIVERSES CANALISATIONS POUR UN FLUX THERMIQUE DE SURFACE CONSTANTHANNA OT; SANDALL OC; PARUIT BA et al.1976; LETTERS HEAT MASS TRANSFER; G.B.; DA. 1976; VOL. 3; NO 2; PP. 89-97; BIBL. 7 REF.Article

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