kw.\*:("DISK AGITATOR")
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THE FLOW OF LIQUID IN A STREAM FROM THE STANDARD TURBINE IMPELLERFORT I; MOCKEL HO; DRBOHLAV J et al.1979; COLLECT. CZECHOSL. CHEM. COMMUNIC.; CSK; DA. 1979; VOL. 44; NO 3; PP. 700-710; BIBL. 15 REF.Article
ZUR FRAGE DER AUSTAUSCHFLAECHE IM MIT SCHEIBENRUEHRERN BEGASTEN RUEHRKESSEL = SURFACE D'ECHANGE DANS UN RECIPIENT AGITE A L'AIDE D'AGITATEURS A DISQUE AVEC INSUFFLATION DE GAZKUERTEN H; ZEHNER P.1977; V.D.I. BER.; DEU; DA. 1977 PUBL. 1978; NO 315; PP. 281-288; BIBL. 10 REF.Article
HYDRODYNAMICS AND MASS TRANSFER CHARACTERISTICS OF A LIQUID/LIQUID STIRRED CELLSTOWE LR; SHAEIWITZ JA.1981; CHEM. ENG. COMMUN.; ISSN 0098-6445; USA; DA. 1981; VOL. 11; NO 1-3; PP. 17-26; BIBL. 24 REF.Article
TROPFENVERTEILUNG IN GERUEHRTEN FLUESSIG/FLUESSIG - DISPERSIONEN = DISPERSION DES GOUTTELETTES DANS LES DISPERSIONS LIQUIDE-LIQUIDE AGITEESKIPKE KD.1981; VT, VERFAHRENSTECH.; ISSN 0341-2644; DEU; DA. 1981; VOL. 15; NO 8; PP. 563-566; BIBL. 10 REF.Article
RUEHRLEISTUNG BEIM DISPERGIEREN VON GASEN, EINE NEUE APPROXIMATION NE(QG, FR, D/D) FUER DEN SCHEIBENRUEHRER MIT 6 SCHAUFELN. = EFFICACITE DE L'AGITATION DANS LA DISPERSION DES GAZ - UNE NOUVELLE APPROXIMATION NEQG, FR, D/D) POUR LES AGITATEURS A DISQUES A SIX LAMESJUDAT H.1976; CHEM.-INGR-TECH.; DTSCH.; DA. 1976; VOL. 48; NO 10; PP. 865-867; BIBL. 7 REF.Article
EFFECT OF THE STIRRER CLEARANCE ON PARTICLE SUSPENSION IN AGITATED VESSELSCONTI R; SICARDI S; SPECCHIA V et al.1981; CHEM. ENG. J.; ISSN 0300-9467; CHE; DA. 1981; VOL. 22; NO 3; PP. 247-249; BIBL. 8 REF.Article
ANALYSE RHEODYNAMIQUE ET ETUDE EXPERIMENTALE D'UNE TURBINE A DISQUE DOTEE D'AILETTES RADIALESBEDER LM.1979; TEOR. OSNOVY KHIM. TEKHNOL.; SUN; DA. 1979; VOL. 13; NO 1; PP. 91-97; BIBL. 13 REF.Article
Mixing and Dissolution Times for a Cowles Disk Agitator in Large-Scale Emulsion PreparationRODGERS, Thomas L; COOKE, Michael; SIPERSTEIN, Flor R et al.Industrial & engineering chemistry research. 2009, Vol 48, Num 14, pp 6859-6868, issn 0888-5885, 10 p.Article
Gas-liquid interaction in an apparatus with a disk mixerGNILUSHA, I. I; SHCHUPLYAK, I. A.Chemical and petroleum engineering. 1996, Vol 32, Num 3, pp 190-194, issn 0009-2355Article
GAS-LIQUID MASS TRANSFER IN A MULTI-STAGE PERFORATED-DISK TYPE STIRRING CASCADE.WEN JEI YANG.1976; LETTERS HEAT MASS TRANSFER; G.B.; DA. 1976; VOL. 3; NO 5; PP. 433-441; BIBL. 7 REF.Article
Power consumption of multiple shaft agitatorsPAHL, M. H; BRENKE, A; LUO, Y et al.Chemical engineering & technology. 1996, Vol 19, Num 6, pp 503-509, issn 0930-7516Article
The dependency on scale of power numbers of Rushton disc turbinesBUJALSKI, W; NIENOW, A. W; CHATWIN, S et al.Chemical engineering science. 1987, Vol 42, Num 2, pp 317-326, issn 0009-2509Article
Studies on three-phase mixing: a review and recent resultsNIENOW, A. W; KONNO, M; BUJALSKI, W et al.Chemical engineering research & design. 1986, Vol 64, Num 1, pp 35-42, issn 0263-8762Article
Experimental investigation of the fluid motion in a cylinder driven by a flat-plate impellerBOHL, Douglas.Journal of fluids engineering. 2007, Vol 129, Num 6, pp 737-746, issn 0098-2202, 10 p.Article
Non-ideal flow characteristics, power input and oxygen transfer in sectioned bubble columns provided with twin dispersing disc agitatorsSTERBACKOVA, M; STERBACEK, Z.Chemical engineering journal. 1986, Vol 33, Num 1, pp B11-B18, issn 0300-9467Article
Mahlvorgang und Energieaufnahme einer vertikalen Mehrscheiben-Perlmühle für Satzbetrieb = Processus de broyage et consommation d'énergie dans un broyeur à perles discontinu, vertical, à disques multiples = A study on grinding and energy input in a vertical multi-disk batch pearl millHEIM, A; LESZCZYNIECKI, R.Aufbereitungs-Technik. 1985, Vol 26, Num 10, pp 594-604, issn 0004-783XArticle
Critical impeller speed for solid suspension in mechanically agitated contactorsRAGHAVA RAO, K. S. M. S; REWATKAR, V. B; JOSHI, J. B et al.AIChE journal. 1988, Vol 34, Num 8, pp 1332-1340, issn 0001-1541Article
Gas hold-up in stirred tank reactorsYAWALKAR, Archis A; PANGARKAR, Vishwas G; BEENACKERS, Anthony A. C. M et al.Canadian journal of chemical engineering. 2002, Vol 80, Num 1, pp 158-165, issn 0008-4034Article
Disintegration of microorganisms in a horizontal ball mill with a multi-disk impellerHEIM, A; SOLECKI, M.European Federation of Chemical Engineering. EventEuropean symposium on comminution. 1998, pp 677-686, 2VolConference Paper
Flow generated by a disc turbine. III: Effect of impeller diameter, impeller location and comparison with other radial flow turbinesMISHRA, V. P; JOSHI, J. B.Chemical engineering research & design. 1993, Vol 71, Num 5, pp 563-573, issn 0263-8762Article
Application of fuzzy multiobjective optimization for self-sucking impellers in a bioreactorKRASŁAWSKI, A; RZYSKI, E; STELMACH, J et al.Bioprocess engineering (Berlin, West). 1991, Vol 6, Num 3, pp 109-116, issn 0178-515XArticle
Use of time-resolved Raman spectroscopy for measuring mixing times and concentrationsCOOK, B. W; LOUDEN, J. D; LORRIAUX-RUBBENS, A et al.Journal of Raman spectroscopy. 1987, Vol 18, Num 3, pp 163-169, issn 0377-0486Article
Breaking characteristics of different materials and their effect on stress intensity and stress number in stirred media millsKWADE, Arno; SCHWEDES, Joerg.Powder technology. 2002, Vol 122, Num 2-3, pp 109-121, issn 0032-5910Article
Influence of the stirrer initial position on emulsion morphology. Making use of the local water-to-oil ratio concept for formulation engineering purposeSALAGER, Serge E; TYRODE, Eric C; CELIS, Maria-Teresa et al.Industrial & engineering chemistry research. 2001, Vol 40, Num 22, pp 4808-4814, issn 0888-5885Article
Determination of the most important grinding mechanism in stirred media mills by calculating the stress intensity and the stress numberKWADE, A.European Federation of Chemical Engineering. EventEuropean symposium on comminution. 1998, pp 667-676, 2VolConference Paper