scispace - formally typeset
Open AccessJournal ArticleDOI

Liquid phase velocity in A 5.5M diameter bubble column.

Reads0
Chats0
TLDR
In this paper, a bubble column 5.5 m in diameter and approximately 7 m in liquid height was measured and the velocity distribution was analyzed by a circulating flow model, with values of the turbulent viscosity in the range from 3000 to 4000 g/cm • sec.
Abstract
Liquid Telocity distribution was measured in a bubble column 5.5 m in diameter and approximately 7 m in liquid height. Liquid flow was upward in the column center and downward near the wall. The upward velocities were from 52 to 115 cm/sec in the superficial gas velocity range from 2.4 to 8.5 cm/sec. The liquid velocity distribution is analyzed by a circulating flow model. Values of the turbulent viscosity-the parameter of the model-are in the range from 3000 to 4000 g/cm • sec. These values agree well with those estimated by an empirical formula for turbulent viscosity proposed by Miyauchi and Shyu for smaller-diameter bubble columns.

read more

Citations
More filters
Journal ArticleDOI

Computational flow modelling and design of bubble column reactors

TL;DR: In this article, the authors reviewed the modelling efforts on the flow patterns published in the last 30 years with relatively more focus on the last 10 years, focusing on cylindrical bubble columns where results on flow pattern could be extended to the design.
Journal ArticleDOI

Sparged loop reactors

TL;DR: In this paper, the performance of external loop air lift reactors (EL-ALR) has been analyzed and a reliable and generalised circulation model has been presented, which depends on the accuracy of the predictive methods for the gas hold-up and the two-phase fractional pressure drop.
Book ChapterDOI

Fischer-Tropsch Reactors

TL;DR: In this article, four types of Fischer-Tropsch (FT) Reactor are discussed: circulating fluidized bed (FLB), tubular fixed bed (TBF), slurry phase (SPS), and slurry-phase (SLP) this article.
Journal ArticleDOI

A correlation for gas holdup in turbulent coalescing bubble columns

TL;DR: A review of existing literature for the purpose of comparing correlations which allow the explicit predictiosn of gas holdup in two- or three-phase bubble columns shows wide disagreement concerning the effect of various variables as mentioned in this paper.
Journal ArticleDOI

Liquid phase mixing in bubble columns with Newtonian and non-Newtonian fluids

TL;DR: In this article, a hydrodynamic model for the liquid phase in bubble columns is developed based on an energy balance and the mixing length theory, and the predictions of the model are in reasonably good agreement with data on liquid velocity at the column axis and the axial dispersion coefficient.