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Particle mass transfer and liquid hold-up in packed beds with upward concurrent gas-liquid flow

S. Mochizuki
- 01 Jan 1981 - 
- Vol. 36, Iss: 1, pp 213-215
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This article is published in Chemical Engineering Science.The article was published on 1981-01-01. It has received 7 citations till now. The article focuses on the topics: Packed bed.

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Citations
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Residence time distribution of the liquid in gas-liquid cocurrent upflow fixed-bed reactors

TL;DR: In this paper, the residence time distribution (RTD) of the liquid in a gas-liquid upflow fixed-bed reactor with porous and nonporous particles and air/Newtonian or non Newtonian systems was investigated.
Journal ArticleDOI

Axial dispersion of liquid in gas-liquid cocurrent downflow and upflow fixed-bed reactors with porous particles

TL;DR: In this article, a tracer injection technique was used and the dynamic responses were interpreted using the piston-dispersion-exchange model with Danckwerts' boundary conditions.
Journal ArticleDOI

Analysis of trickle bed and packed bubble column bioreactors for combined carbon oxidation and nitrification

TL;DR: In this article, a transient diffusion model of the tracer in the porous particle coupled with the piston-dispersion-exchange model was used to interpret the residence time distribution curves obtained.
References
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Mass transfer from spheres in various regular packings to a flowing fluid

TL;DR: In this paper, mass transfer coefficients have been determined for fluids flowing around single spheres, which were part of a regular arrangement of similar, but inactive spheres, and eight different kinds of packing were used.
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