kw.\*:("fluidization")
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A fully predictive criterion for the transition between particulate and aggregate fluidizationFOSCOLO, P. U; GIBILARO, L. G.Chemical engineering science. 1984, Vol 39, Num 12, pp 1667-1675, issn 0009-2509Article
Régimes homogène et hétérogène de fluidisationCHERNYAEV, YU. I.Inženerno-fizičeskij žurnal. 1984, Vol 47, Num 3, pp 402-407, issn 0021-0285Article
Particulate and aggregative fluidization - 50 years in retrospectKWAUK, M; JINGHAI LI; DEJIN LIU et al.Powder technology. 2000, Vol 111, Num 1-2, pp 3-18, issn 0032-5910Article
Experimental observation of nonhomogeneity in a liquid-solid fluidized bed of small particlesLIANG-SHIH FAN; KAWAMURA, T; CHITESTER, D. C et al.Chemical engineering communications (Print). 1985, Vol 37, Num 1-6, pp 141-157, issn 0098-6445Article
Modified gas-perturbed liquid model (GPLM) for minimum fluidization velocity in a two-phase inverse fluidized bed reactor with Newtonian and non-Newtonian systemsSIVASUBRAMANIAN, V; VELAN, M.Journal of chemical technology and biotechnology (1986). 2006, Vol 81, Num 7, pp 1232-1238, issn 0268-2575, 7 p.Article
Effect of aspect ratio on bed expansion in particulate fluidizationMAZUMDAR, P; GANGULY, U. P.Canadian journal of chemical engineering. 1985, Vol 63, Num 5, pp 850-852, issn 0008-4034Article
Effect of low velocity liquid pulsations on some hydrodynamic characteristics of liquid and gas-liquid fluidized bedsEL-TEMTAMY, S. A; EPSTEIN, N.AIChE journal. 1986, Vol 32, Num 3, pp 509-512, issn 0001-1541Article
Radial dispersion characteristics of two- and three-phase fluidized bedsYONG KANG; KIM, S. D.Industrial and engineering chemistry. Process design and development. 1986, Vol 25, Num 3, pp 717-722, issn 0019-7882Article
Aggregate behaviour of liquid fluidised bedsGIBILARO, L. G; HOSSAIN, I; FOSCOLO, P. U et al.Canadian journal of chemical engineering. 1986, Vol 64, Num 6, pp 931-938, issn 0008-4034Article
Transfert de matière entre un lit fluidisé homogène et une paroi poreuse = Mass transfer between a homogeneous fluidized bed and a porous wallMONTLAHUC, G; TARODO, B; RIOS, G. M et al.Entropie (Paris). 1985, Vol 21, Num 124, pp 24-27, issn 0013-9084Article
The effect of mechanical vibration on gas fluidization of a fine aeratable powder : Particle technologyBARLETTA, Diego; DONSI, Giorgio; FERRARI, Giouanna et al.Chemical engineering research & design. 2008, Vol 86, Num 4, pp 359-369, issn 0263-8762, 11 p.Article
Layer inversion and mixing of binary solids in two- and three-phase fluidized bedsCHUN, Byung-Soon; DONG HYUN LEE; EPSTEIN, Norman et al.Chemical engineering science. 2011, Vol 66, Num 14, pp 3180-3184, issn 0009-2509, 5 p.Conference Paper
Liquid-solid mass transfer in inverse fluidized bedNIKOV, I; KARAMANEV, D.AIChE journal. 1991, Vol 37, Num 5, pp 781-784, issn 0001-1541, 4 p.Article
Mécanisme de mélange par paquets dans un lit fluidiséBOBKOV, N. N; GUPALO, YU. P.Izvestiâ Akademii nauk SSSR. Mehanika židkosti i gaza. 1983, Num 5, pp 73-84, issn 0568-5281Article
Fluidisationsprozesse und deren apparative Gestaltung = Procédés de fluidisation et arrangement de l'équipement = Processes of fluidization and the arrangement of the equipmentKRELL, L; KUNNE, H.-J; MORL, L et al.Chemische Technik (Berlin, DDR, 1949). 1986, Vol 38, Num 5, pp 183-187, issn 0045-6519Article
Effects of macroscopic hydrodynamics on heat transfer in a three-phase fluidized bedLIN, Tsao-Jen; HUNG-TZU, Chiu.Catalysis today. 2003, Vol 79-80, pp 159-167, issn 0920-5861, 9 p.Conference Paper
Solid-liquid mass transfer in three-phase fixed and fluidized bedsNIKOV, I; DELMAS, H.Chemical engineering science. 1987, Vol 42, Num 5, pp 1089-1903, issn 0009-2509Article
Minimum fluidization velocity at elevated temperature in tapered fluidized bedSAU, D. C; MOHANTY, Swati; BISWAL, K. C et al.Chemical engineering and processing. 2008, Vol 47, Num 12, pp 2391-2394, issn 0255-2701, 4 p.Article
Liquid holdup and heat transfer coefficient in liquid-solid and three-phase fluidized bedsTAI-MING CHIU; ZIEGLER, E. N.AIChE journal. 1985, Vol 31, Num 9, pp 1504-1509, issn 0001-1541Article
TRANSITION ENTRE FLUIDISATION HOMOGENE ET FLUIDISATION HETEROGENE AU COURS DE L'EXPANSION DU LIT FLUIDISEDOJCHEV K; DIMITROV V; TODOROV S et al.1975; FOD. VISSH. KHIM.-TEKHNOL. INST., SOFIJA; BGR; DA. 1975 PUBL. 1977; VOL. 22; NO 2; PP. 205-212; ABS. RUS/ENG; BIBL. 15 REF.Article
Comments on «Application of the Davies-Taylor equation to a large bubble rise in liquid-fluirized beds». ReplyEPSTEIN, N; EL-TEMTAMY, S. A; DE OLIVEIRA MENDES, C. L et al.Chemical engineering journal. 1985, Vol 31, Num 1, pp 55-58, issn 0300-9467Article
Gas holdup above the bed surface and grid gas jet hydrodynamics for three phase fluidized bedsCATROS, A; BERNARD, J. R; BRIENS, C et al.Canadian journal of chemical engineering. 1985, Vol 63, Num 5, pp 754-759, issn 0008-4034Article
Application of the Davies-Taylor equation to a large bubble rise in liquid-fluidized bedsDE OLIVEIRA MENDES, C. L; QUASSIM, R. Y.Chemical engineering journal. 1984, Vol 28, Num 1, pp 21-23, issn 0300-9467Article
Distribution of solid particle in liquid fluidized bedsPATWARDHAN, V. S; CHI TIEN.Canadian journal of chemical engineering. 1984, Vol 62, Num 1, pp 46-54, issn 0008-4034Article
Einsatz der Vierpunkt-Leitfähigkeitsmikrosonde im Dreiphasen-Fliessbett = Utilisation d'une microsonde à conductivité en quatre points, dans un lit fluidisé à trois phases = Use of a four-point conductivity microprobe in a three-phase fluidized bedBRÜCK, J; HEKTOR, K.Chemieingenieurtechnik. 1984, Vol 56, Num 12, pp 920-922, issn 0009-286XArticle