✍ Scribed by A.N. Singh; H.R. Takhalate; A. Storck; P.Sen Gupta
No coin nor oath required. For personal study only.
📜 SIMILAR VOLUMES
A simple empirical model was established which allows solids holdup in a gas-liquid-solid fluidized bed containing large and dense particles to be readily predicted based on the equation of Richardson and Zaki (1954, Trans. Inst. Chem. Engrs 32, 35) for liquid-solid Auidized bed systems. The approac
yield of soot formed during laboratory isothermal pyrolysis of both benzene and coal tar at 1200' were practically the same. It was concluded that dispersion of soot formed during incomplete combustion depends mainly on temperature and feedstock pyrolysis process. ## 97102132 Correlations for the
The mass transfer from a wall to a fluid in a liquid-solid fluidized bed has become of special interest with a novel cell culture bioreactor, aerated by a membrane module inside the reactor. This bioreactor has been used as an experimental setup for mass transfer experiments. A large set of data was