MIXING OF VISCOELASTIC FLUIDS WITH HELICAL-RIBBON AGITATORS. I. MIXING TIME AND FLOW PATTERNSCARREAU PJ; PATTERSON I; YAP CY et al.1976; CANAD. J. CHEM. ENGNG; CANADA; DA. 1976; VOL. 54; NO 3; PP. 135-142; ABS. FR.; BIBL. 25 REF.Article

BLENDING OF NON-NEWTONIAN LIQUIDS BY HELICAL RIBBON SCREW IMPELLERSSINGLA TR; TIWARI KK.1975; CHEM. ENGNG WORLD; INDIA; DA. 1975; VOL. 10; NO 3; PP. 53-55A (5 P.); BIBL. 3 REF.Article

MOC MIESZANIA MIESZADLAMI WSTEGOWYMI W RUCHU LAMINARNYM, PRZEJSCIOWYM ORAZ CZESCIOWO BURZLIUYM = ENERGIE DE MELANGE DES AGITATEURS A RUBAN EN MOUVEMENT INTERMEDIAIRE LAMINAIRE ET PARTIELLEMENT TURBULENTBLASINSKI H; KUNCEWICZ C.1978; INZYNIER. CHEM.; POL; DA. 1978; VOL. 8; NO 4; PP. 807-817; ABS. RUS/ENG; BIBL. 13 REF.Article

THEORETICAL APPROACH TO COMPUTE THE POWER CONSUMPTION IN VISCOUS MIXERS.BIARDI G; DENTE M; LOSCO F et al.1976; QUAD. INGEGNERE CHIM. ITAL.; ITAL.; DA. 1976; VOL. 12; 7-8-9; PP. 125-131; ABS. ITAL.; BIBL. 16 REF.Article

MIXING OF VISCOUS MATERIALSTIWARI KK.1975; CHEM. ENGNG WORLD; INDIA; DA. 1975; VOL. 10; NO 3; PP. 45-52; BIBL. 53 REF.Article

RUEHREN NICHT-NEWTONSCHER FLUESSIGKEITEN. V. DER LEISTUNGSVERBRAUCH FUER DEN BLATT-, SCHNECKEN- UND BANDRUEHRER BEIM RUEHREN PLASTICHER FLUIDER MEDIEN IM LAMINAREN STROEMUNGSBEREICH = AGITATION DES LIQUIDES NON-NEWTONIENS. V. CONSOMMATION D'ENERGIE DES AGITATEURS A LAME, HELICE ET BANDE DANS L'AGITATION DE MILIEUX PLASTIQUES FLUIDES DANS LE DOMAINE D'ECOULEMENT LAMINAIREREHER EO.1975; CHEM. TECH.; DTSCH.; DA. 1975; VOL. 27; NO 6; PP. 343-345; BIBL. 7 REF.Article

POWER REQUIREMENTS OF HELICAL RIBBON MIXERSBLASINSKI H; RZYSKI E.1979; CHEM. ENGNG J.; GBR; DA. 1979; VOL. 19; NO 2; PP. 157-160; BIBL. 18 REF.Article

CALCUL DE LA PUISSANCE ET DES TENSIONS AXIALES DANS LE MELANGEAGE PAR DES AGITATEURS A RUBAN EN MILIEU NEWTONIENBEGACHEV VI; BRAGINSKIJ LN; VASIL'TSOV EH A et al.1977; TEOR. OSNOVY KHIM. TEKHNOL.; S.S.S.R.; DA. 1977; VOL. 11; NO 3; PP. 432-436; BIBL. 10 REF.Article

A GUIDE TO DESIGNING SPECIAL AGITATORSHO FC; KWONG A.1973; CHEM. ENGNG; U.S.A.; DA. 1973; VOL. 80; NO 17; PP. 94-104; BIBL. 48 REF.Serial Issue

Flüssigphasenreaktor mit geringer axialer Durchmischung = Réacteur en phase liquide avec faible mélange axial = Liquid phase reactor with low axial mixingPIPPEL, W; LÖSCHAU, S; OELMANN, H et al.Chemische Technik (Berlin, DDR, 1949). 1983, Vol 35, Num 11, pp 574-579, issn 0045-6519Article

EFFECTS OF GEOMETRICAL VARIABLES OF HELICAL RIBBON IMPELLERS ON MIXING OF HIGHLY VISCOUS NEWTONIAN LIQUIDSTAKAHASHI K; SASAKI M; ARAI K et al.1982; J. CHEM. ENG. JPN.; ISSN 0021-9592; JPN; DA. 1982; VOL. 15; NO 3; PP. 217-224; ABS. JAP; BIBL. 22 REF.Article

HEAT TRANSFER AND TEMPERATURE DISTRIBUTIONS IN AN AGITATED TANK EQUIPPED WITH HELICAL RIBBON IMPELLERKURIYAMA M; OHTA M; YANAGAWA K et al.1981; J. CHEM. ENG. JPN; ISSN 0021-9592; JPN; DA. 1981; VOL. 14; NO 4; PP. 323-330; BIBL. 10 REF.Article

THE EFFECT OF MIXERS ON THE FORMATION AND STABILITY OF AERATED AMMONIUM NITRATE GELSKEIRSTEAD KF; DE KEE D; CARREAU PJ et al.1980; CAN. J. CHEM. ENG.; ISSN 0008-4034; CAN; DA. 1980; VOL. 58; NO 4; PP. 549-552; BIBL. 13 REF.Article

MIXING WITH HELICAL RIBBON AGITATORS. II. NEWTONIAN FLUIDSPATTERSON WI; CARREAU PJ; YAP CY et al.1979; A.I. CHE. E.J., NEW YORK; USA; DA. 1979; VOL. 25; NO 3; PP. 508-516; BIBL. 29 REF.Article

WERYFIKACJA WLASNEGO MODELU PRZENOSZENIA PEDU I CIEPLA W MIESZALNIKACH Z MIESZADLAMI WACSKOPRZESWITOWYMI = VERIFICATION DU MODELE REEL DE TRANSFERT DE QUANTITE DE MOUVEMENT ET DE CHALEUR POUR LES MELANGEURS AVEC AGITATEURS A FAIBLE JEUHEIM A.1978; INZYNIER. CHEM.; POL; DA. 1978; VOL. 8; NO 3; PP. 507-524; ABS. RUS/ENG; BIBL. 9 REF.Article

CLOSE-CLEARANCE HELICAL IMPELLERS: A PHYSICAL MODEL FOR NEWTONIAN LIQUIDS AT LOW REYNOLDS NUMBERSCHAVAN VV.1983; AICHE JOURNAL; ISSN 0001-1541; USA; DA. 1983; VOL. 29; NO 2; PP. 177-186; BIBL. 43 REF.Article

AXIAL THRUST ACTING ON AGITATORS IN NON-NEWTONIAN FLUIDSRIEGER F; NOVAK V.1978; CHEM. ENGNG J.; GBR; DA. 1978; VOL. 16; NO 1; PP. 27-33; BIBL. 5 REF.Article

POWER CORRELATION FOR ANCHOR AND HELICAL RIBBON IMPELLERS IN HIGHLY VISCOUS LIQUIDSTAKAHASHI K; ARAI K; SAITO S et al.1980; J. CHEM. ENGNG JAP.; JPN; DA. 1980; VOL. 13; NO 2; PP. 147-150; BIBL. 12 REF.Article

MIXING WITH HELICAL RIBBON AGITATORS. III. NON-NEWTONIAN FLUIDSYAP CY; PATTERSON WI; CARREAU PJ et al.1979; A.I. CHE. E.J., NEW YORK; USA; DA. 1979; VOL. 25; NO 3; PP. 516-521; BIBL. 15 REF.Article

A RADIO PILL AND AERIAL SYSTEM TRACKING THE POWDER MOTION IN A HELICAL RIBBON MIXERCOOKER B; MITCHELL FRG; NEDDERMAN RM et al.1983; CHEMICAL ENGINEER; ISSN 0302-0797; GBR; DA. 1983; NO 392; PP. 81-83; BIBL. 16 REF.Article

HEAT TRANSFER IN AGITATED VESSELS WITH SPECIAL TYPES OF IMPELLERSISHIBASHI K; YAMANAKA A; MITSUISHI N et al.1979; J. CHEM. ENGNG JAP.; JPN; DA. 1979; VOL. 12; NO 3; PP. 230-235; BIBL. 14 REF.Article

Mixing in a helical ribbon powder agitatorCOOKER, B; NEDDERMAN, R. M.Powder technology. 1986, Vol 46, Num 2-3, pp 263-269, issn 0032-5910Article

Homogenization efficiency of helical ribbon agitatorsRIEGER, F; NOVAK, V; HAVELKOVA, D et al.Chemical engineering journal. 1986, Vol 33, pp 143-150, issn 0300-9467Article

Power consumption and homogeneization time for e oleoresin suspensionsPANDIT, A. B; TENEFRANCIA, N; JOSHI, J. B et al.Chemical engineering journal. 1984, Vol 28, Num 1, pp 25-38, issn 0300-9467Article

Heat transfer to viscous Newtonian and non-Newtonian fluids for helical ribbon mixersAYAZI SHAMLOU, P; EDWARDS, M. F.Chemical engineering science. 1986, Vol 41, Num 8, pp 1957-1967, issn 0009-2509Article