๐”– Bobbio Scriptorium
โœฆ   LIBER   โœฆ

A circulating liquid fluidised bed

โœ Scribed by L.G. Gibilaro; R. Di Felice; P.U. Foscolo


Publisher
Elsevier Science
Year
1988
Tongue
English
Weight
286 KB
Volume
43
Category
Article
ISSN
0009-2509

No coin nor oath required. For personal study only.


๐Ÿ“œ SIMILAR VOLUMES


Hydrodynamic modelling of circulating fl
โœ J.J. Niewland; P. Huizenga; J.A.M. Kuipers; W.P.M. van Swaaij ๐Ÿ“‚ Article ๐Ÿ“… 1994 ๐Ÿ› Elsevier Science ๐ŸŒ English โš– 754 KB

one-dimensional model for the riser section of a circulating fluidised bed has been developed which describes the steady-state hydrodynamic key variables in the radial direction for fully developed axisymmetric flow. Both the gas and the solid phase are considered as two continuous media, fully pene

Gas mixing in the cocurrent downflow cir
โœ Assoc. Prof. Fei Wei; Prof. Yong Jin; Prof. Zhiqing Yu; Dr. Jinzhong Liu ๐Ÿ“‚ Article ๐Ÿ“… 1995 ๐Ÿ› John Wiley and Sons ๐ŸŒ English โš– 321 KB

An experimental study on the gas dispersion behaviour of a cocurrent downflow gas-solids suspension in a 140 mm i.d. circulating fluidised bed (CDCFB) using the steady-state tracer method is presented. The influence of gas velocity, solids circulating rate and particle density on radial gas dispersi

Particle segregation in liquid-solid flu
โœ A.K.A Juma; J.F. Richardson ๐Ÿ“‚ Article ๐Ÿ“… 1979 ๐Ÿ› Elsevier Science ๐ŸŒ English โš– 544 KB

Shorter Commumcations 137 those presented m Ref [l] The range of values of 4 over which muIt& solutions exist, ti Indeed they do exist, may be located by first computmg the two real roots of T(y) on the Interval I < y C I+ j? and subsequently usmg those roots m eqn (1) to compute duectly the endpomt