Zobrazeno 1 - 10
of 15
pro vyhledávání: '"D. V. Vuković"'
Autor:
Howard Littman, Zeljko Grbavcic, John D. Paccione, S.Dj. Jovanovic, D. V. Vuković, M.H. Morgan
Publikováno v:
Powder Technology. 84:49-56
Extending earlier work [1], effective drag coefficients for particles in steady turbulent gas-solids transport in a 28.45 mm vertical transport pipe 5.49 m long have been determined for 1 and 2 mm glass spheres and 1.99 mm rapeseed. The data are well
Publikováno v:
Powder Technology. 79:217-225
Mass transfer coefficients between fluid and immersed surfaces in liquid fluidized beds of spherical inert particles have been studied experimentally using fluidization columns 40 mm and 70 mm in diameter. Mass transfer data were obtained in three ex
Publikováno v:
Chemical Engineering Science. 47:2120-2124
We are concerned with measurements of the effective buoyancy and fluid-dynamic drag on large particles of varying density settling or rising in a water-fluidized bed of monodisperse spheres of smaller size
Publikováno v:
Scopus-Elsevier
A model for predicting the ratio of the maximum spoutable bed height in a spout-fluid bed to the maximum spoutable bed height in a spouted bed is presented and experimentally verified. The model is a further extension of the basic Mamuro and Hattori
Publikováno v:
Chemical Engineering Science. 46:773-779
The axisymmetric model previously developed for spouted beds is adapted to describe fluid flow in the annulus of a spout-fluid bed at the minimum spout-fluid flow rate. Experimental axial pressure profiles provide the boundary condition at the spout-
Publikováno v:
The Canadian Journal of Chemical Engineering. 55:497-501
A theory is presented for predicting the maximum spoutable height, in a spouted bed where fluidization of the annular solids limits the penetration of the fluid jet entering the bed. The quantity (Hmds/(D – d) is found to be a function of ds/Dc onl
Publikováno v:
The Chemical Engineering Journal. 17:227-236
Experiments were carried out to determine the liquid side mass transfer coefficient in spout-fluid beds of ion exchange resin. The ratio (Sh S—F ) overall /Sh fluidized is correlated with the ratio of the flow rate through the nozzle to the total f
Publikováno v:
The Canadian Journal of Chemical Engineering. 54:33-42
This study extends the theory of Mamuro and Hattori to beds of less than the maximum spoutable height. The new model gives predictions for the fluid flow pattern, minimum spouting velocity and spouting pressure drop which are in agreement both with e
Publikováno v:
The Canadian Journal of Chemical Engineering. 52:174-179
Data on the minimum spout-fluid flowrates and the pressure drop in the annulus at that flowrate are presented as a function of bed height and nozzle diameter for a bed spout-fluidized with water. The column was 62.6 mm. in diameter and contained 3.09
Publikováno v:
The Canadian Journal of Chemical Engineering. 57:684-687