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AGITATED VESSEL PARTICLE-LIQUID MASS TRANSFER: A COMPARISON BETWEEN THEORIES AND DATANIENOW AW.1975; CHEM. ENGNG J.; G.B.; DA. 1975; VOL. 9; NO 2; PP. 153-160; BIBL. 27 REF.Article

THE EFFECT OF AGITATION AND SCALE-UP ON CRYSTAL GROWTH RATES AND ON SECONDARY NUCLEATION.NIENOW AW.1976; TRANS. INSTIT. CHEM. ENGRS; G.B.; DA. 1976; VOL. 54; NO 3; PP. 205-207; BIBL. 12 REF.Article

PARTICLE MIXING AND SEGREGATION IN GAS FLUIDISED BEDS. A REVIEW.ROWE PN; NIENOW AW.1976; POWDER TECHNOL.; SWITZ.; DA. 1976; VOL. 15; NO 2; PP. 141-147; BIBL. 10 REF.Article

FLOW OVER DISC TURBINE BLADESNIENOW AW; WISDOM DJ.1974; CHEM. ENGNG SCI.; G.B.; DA. 1974; VOL. 29; NO 9; PP. 1994-1997; BIBL. 11 REF.Article

PARTICLE GROWTH MECHANISMS IN FLUIDISED BED GRANULATION. I: THE EFFECT OF PROCESS VARIABLESSMITH PG; NIENOW AW.1983; CHEMICAL ENGINEERING SCIENCE; ISSN 0009-2509; GBR; DA. 1983; VOL. 38; NO 8; PP. 1223-1231; BIBL. 21 REF.Article

CONTINUOUS MIXING OF TWO PARTICULATE SPECIES OF DIFFERENT DENSITY IN A GAS FLUIDISED BEDNIENOW AW; NAIMER NS.1980; TRANS. INSTIT. CHEM. ENGRS; GBR; DA. 1980; VOL. 58; NO 3; PP. 181-186; BIBL. 11 REF.Article

PARTICLE ABRASION AT HIGH SOLIDS CONCENTRATION IN STIRRED VESSELSNIENOW AW; CONTI R.1978; CHEM. ENGNG SCI.; GBR; DA. 1978; VOL. 33; NO 8; PP. 1077-1086; BIBL. 15 REF.Article

GAS RECIRCULATION RATE THROUGH IMPELLER CAVITIES AND SURFACE AERATION IN SPARGED AGITATED VESSELSNIENOW AW; CHAPMAN CM; MIDDLETON JC et al.1979; CHEM. ENGNG J.; GBR; DA. 1979; VOL. 17; NO 2; PP. 111-118; BIBL. 3 REF.Article

PARAMETER ESTIMATION FOR A SOLIDS MIXING/SEGREGATION MODEL FOR GAS FLUIDISED BEDSNAIMER NS; CHIBA T; NIENOW AW et al.1982; CHEM. ENG. SCI.; ISSN 0009-2509; GBR; DA. 1982; VOL. 37; NO 7; PP. 1047-1057; BIBL. 29 REF.Article

PARTICLE SUSPENSION IN A GAS SPARGED RUSHTON-TURBINE AGITATED VESSELCHAPMAN CM; NIENOW AW; MIDDLETON JC et al.1981; TRANS. INST. CHEM. ENG.; ISSN 0046-9858; GBR; DA. 1981; VOL. 59; NO 2; PP. 134-137; BIBL. 10 REF.Article

ACTION OF SHEAR ON ENZYMES: STUDIES WITH ALCOHOL DEHYDROGENASETHOMAS CR; NIENOW AW; DUNNILL P et al.1979; BIOTECHNOL. AND BIOENGNG; USA; DA. 1979; VOL. 21; NO 12; PP. 2263-2278; BIBL. 39 REF.Article

THE INTERACTION OF YIELD STRESS AND VISCOELASTICITY ON THE WEISSENBERG EFFECTELSON TP; SOLOMON J; NIENOW AW et al.1982; J. NON-NEWTON. FLUID MECH.; ISSN 0377-0257; NLD; DA. 1982; VOL. 11; NO 1-2; PP. 1-22; BIBL. 23 REF.Article

SOME EFFECTS OF PSEUDOPLASTICITY ON HOLD-UP IN AERATED, AGITATED VESSELSMACHON V; VLCEK J; NIENOW AW et al.1980; CHEM. ENGNG J.; GBR; DA. 1980; VOL. 19; NO 1; PP. 67-74; BIBL. 23 REF.Article

PARTICLE-GAS-LIQUID MIXING IN STIRRED VESSELS. III: THREE PHASE MIXINGCHAPMAN CM; NIENOW AW; COOKE M et al.1983; CHEMICAL ENGINEERING RESEARCH AND DESIGN; ISSN 51263X; GBR; DA. 1983; VOL. 61; NO 3; PP. 167-181; BIBL. 19 REF.Article

CAVERN SIZES IN AGITATED FLUIDS WITH A YIELD STRESSSOLOMON J; ELSON TP; NIENOW AW et al.1981; CHEM. ENG. COMMUN.; ISSN 0098-6445; USA; DA. 1981; VOL. 11; NO 1-3; PP. 143-164; BIBL. 25 REF.Article

PARTICLE-GAS-LIQUID MIXING IN STIRRED VESSELS. IV: MASS TRANSFER AND FINAL CONCLUSIONSCHAPMAN CM; NIENOW AW; COOKE M et al.1983; CHEMICAL ENGINEERING RESEARCH AND DESIGN; ISSN 51263X; GBR; DA. 1983; VOL. 61; NO 3; PP. 182-185; BIBL. 11 REF.Article

FLUIDIZED BINARY MIXTURES IN WHICH THE DENSER COMPONENT MAY BE FLOTSAMCHIBA S; NIENOW AW; CHIBA T et al.1980; POWDER TECHNOL.; CHE; DA. 1980; VOL. 26; NO 1; PP. 1-10; BIBL. 8 REF.Article

A STIRRED TANK FOR CONTINUOUS CRYSTALLIZATION STUDIESZACEK S; NYVLT J; GARSIDE J et al.1982; CHEM. ENG. J.; ISSN 0300-9467; CHE; DA. 1982; VOL. 23; NO 1; PP. 111-113; BIBL. 7 REF.Article

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