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AXIAL MIXING IN LIQUID-LIQUID SPRAY COLUMNSWIJFFELS JB; RIETEMA K.1972; ADV. CHEM. SER.; U.S.A.; DA. 1972; VOL. 109; PP. 245-251Serial Issue

SCIENCE AND TECHNOLOGY OF DISPERSED TWO-PHASE SYSTEMS. I AND II. I: GENERAL ASPECTS. II: HYDRODYNAMICS OF DISPERSED SYSTEMSRIETEMA K.1982; CHEM. ENG. SCI.; ISSN 0009-2509; GBR; DA. 1982; VOL. 37; NO 8; PP. 1125-1150; BIBL. 86 REF.Article

THE EFFECT OF INTERPARTICLE FORCES ON THE EXPANSION OF A HOMOGENEOUS GAS-FLUIDISED BEDRIETEMA K.1973; CHEM. ENGNG SCI.; G.B.; DA. 1973; VOL. 28; NO 7; PP. 1493-1497; BIBL. 12 REF.Serial Issue

DRYING GRANULAR SOLIDS IN FLUIDIZED BED. I: DESCRIPTION ON BASIS OF MASS AND HEAT TRANSFER COEFFICIENTSHOEBINK JHBJ; RIETEMA K.1980; CHEM. ENG. SCI.; ISSN 0009-2509; GBR; DA. 1980; VOL. 35; NO 10; PP. 2135-2140; BIBL. 21 REF.Article

GROWTH OF YEAST ON N-ALKANES. III: BATCH EXPERIMENTSVERKOOYEN AHM; RIETEMA K.1980; BIOTECHNOL. AND BIOENGNG; USA; DA. 1980; VOL. 22; NO 3; PP. 615-637; BIBL. 11 REF.Article

GAS TRANSFER FROM BUBBLES IN A FLUIDIZED BED TO THE DENSE PHASE. I. THEORYDRINKENBURG AAH; RIETEMA K.1972; CHEM. ENGNG SCI.; G.B.; DA. 1972; VOL. 27; NO 10; PP. 1765-1774; ABS. FR. ALLEM.; BIBL. 14 REF.Serial Issue

MASS TRANSFER FROM SPHERICAL CAP BUBBLES. THE CONTRIBUTION OF THE BUBBLE REARCOPPUS JHC; RIETEMA K.1981; TRANS. INST. CHEM. ENG.; ISSN 0046-9858; GBR; DA. 1981; VOL. 59; NO 1; PP. 54-63; BIBL. 27 REF.Article

THEORETICAL DERIVATION OF THE MASS TRANSFER COEFFICIENT AT THE FRONT OF A SPHERICAL CAP BUBBLECOPPUS JHC; RIETEMA K.1980; CHEM. ENGNG SCI.; GBR; DA. 1980; VOL. 35; NO 6; PP. 1497-1499; BIBL. 5 REF.Article

DIRECT MEASUREMENT OF THE MECHANICAL RESPONSE OF A HOMOGENEOUSLY FLUIDISED BED TO VERTICAL VIBRATION OF AN IMMERSED OBJECTMUTSERS SMP; RIETEMA K.1979; POWDER TECHNOL.; CHE; DA. 1979; VOL. 24; NO 1; PP. 57-63; BIBL. 2 REF.Article

ANALYSIS OF THE INTERACTION BETWEEN A VIBRATING WIRE NETTING AND A HOMOGENEOUSLY FLUIDISED BEDMUTSERS SMP; RIETEMA K.1979; POWDER TECHNOL.; CHE; DA. 1979; VOL. 24; NO 1; PP. 65-71; BIBL. 7 REF.Article

DESCRIPTION OF BUBBLE SHAPE IN TERMS OF DIMENSIONLESS NUMBERSCOPPUS JHC; RIETEMA K.1980; CHEM. ENGNG SCI.; GBR; DA. 1980; VOL. 35; NO 6; PP. 1495-1497; BIBL. 10 REF.Article

GAS TRANSFER FROM BUBBLES IN A FLUIDIZED BED TO THE DENSE PHASE. II. EXPERIMENTSDRINKENBURG AAH; RIETEMA K.1973; CHEM. ENGNG SCI.; G.B.; DA. 1973; VOL. 28; NO 1; PP. 259-273; BIBL. 16 REF.Serial Issue

GROWTH OF YEAST ON N-ALKANES. I: STOCHASTIC MODELVERKOOYEN AHM; RIETEMA K.1980; BIOTECHNOL. AND BIOENGNG; USA; DA. 1980; VOL. 22; NO 3; PP. 571-595; BIBL. 17 REF.Article

DAS WACHSTUM VON HEFEN AUF ERDOEL = CROISSANCE DES LEVURES A PARTIR DE PETROLERIETEMA K; VERKOOYEN AHM.1974; CHEM.-INGR-TECH.; DTSCH.; DA. 1974; VOL. 46; NO 16; PP. 693Article

DRYING GRANULAR SOLIDS IN A FLUIDISED BED. II: THE INFLUENCE OF DIFFUSION LIMITATION ON THE GAS-SOLID CONTACTING AROUND BUBBLESHOEBINK JHBJ; RIETEMA K.1980; CHEM. ENG. SCI.; ISSN 0009-2509; GBR; DA. 1980; VOL. 35; NO 11; PP. 2257-2265; BIBL. 14 REF.Article

GAS-SOLIDS FLUIDIZATION IN A CENTRIFUGAL FIELD. THE EFFECT OF GRAVITY UPON BED EXPANSION.MUTSERS SMP; RIETEMA K.1977; POWDER TECHNOL.; SWITZ.; DA. 1977; VOL. 18; NO 2; PP. 249-256; BIBL. 2 REF.Article

THE EFFECT OF INTERPARTICLE FORCES ON THE EXPANSION OF A HOMOGENEOUS GAS-FLUIDIZED BED.MUTSERS SMP; RIETEMA K.1977; POWDER TECHNOL.; SWITZ.; DA. 1977; VOL. 18; NO 2; PP. 239-248; BIBL. 27 REF.Article

TRANSIENT PHENOMENA IN FLUIDIZED BEDS WHEN SWITCHING THE FLUIDIZING AGENT FROM ONE GAS TO ANOTHER.RIETEMA K; HOEBINK J.1977; POWDER TECHNOL.; SWITZ.; DA. 1977; VOL. 18; NO 2; PP. 257-265; BIBL. 6 REF.Article

SEGREGATION OF LIQUID-FLUIDIZED SOLIDSVAN DUIJN G; RIETEMA K.1982; CHEM. ENG. SCI.; ISSN 0009-2509; GBR; DA. 1982; VOL. 37; NO 5; PP. 727-733; BIBL. 15 REF.Article

ON THE MOMENTUM EQUATIONS IN DISPERSED TWO-PHASE SYSTEMSRIETEMA K; VAN DEN AKKER HEA.1983; INTERNATIONAL JOURNAL OF MULTIPHASE FLOW; ISSN 0301-9322; GBR; DA. 1983; VOL. 9; NO 1; PP. 21-36; BIBL. 8 REF.Article

FLOW PATTERNS AND AXIAL MIXING IN LIQUID/LIQUID SPRAY COLUMNS. III: THE REDUCTION OF AXIAL MIXING BY APPLYING A POSITIVE TEMPERATURE GRADIENTVAN DEN AKKER HEA; RIETEMA K.1979; TRANS. INSTIT. CHEM. ENGRS; GBR; DA. 1979; VOL. 57; NO 2; PP. 84-93; BIBL. 53 REF.Article

WAKE PHENOMENA BEHIND SPHERICAL-CAP BUBBLES AND SOLID SPHERICAL-CAP BODIES.COPPUS JHC; RIETEMA K; OTTENGRAF SPP et al.1977; TRANS. INST. CHEM. ENGRS; G.B.; DA. 1977; VOL. 55; NO 2; PP. 122-129; BIBL. 22 REF.Article

CONTINUOUS SEDIMENTATION THEORY. EFFECTS OF DENSITY GRADIENTS AND VELOCITY PROFILES ON SEDIMENTATION EFFICIENCY.WOUDA TWM; RIETEMA K; OTTENGRAF SPP et al.1977; CHEM. ENGNG SCI.; G.B.; DA. 1977; VOL. 32; NO 4; PP. 351-358; BIBL. 7 REF.Article

The effect of interstitial gas on millingCOTTAAR, W; RIETEMA, K.Powder technology. 1984, Vol 38, Num 2, pp 183-194, issn 0032-5910Article

FLOW PATTERNS AND AXIAL MIXING IN LIQUID/LIQUID SPRAY COLUMNS. IV: DETECTION OF A MULTIPLE CIRCULATION PATTERN GENERATED BY THE APPLICATION OF A POSITIVE TEMPERATIVE GRADIENTVAN DEN AKKER HEA; RIETEMA K.1979; TRANS. INSTIT. CHEM. ENGRS; GBR; DA. 1979; VOL. 57; NO 3; PP. 147-155; BIBL. 9 REF.Article

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