Mass transfer area in a multi-stage high-speed disperser with split packing

Tao Ai; Aslam M. Mudassar; Ziqi Cai; Zhengming Gao

doi:10.1016/j.cjche.2018.10.012

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Mass transfer area in a multi-stage high-speed disperser with split packing

Fluid Dynamics and Transport Phenomena | Updated：2026-01-06

- Mass transfer area in a multi-stage high-speed disperser with split packing
- Mass transfer area in a multi-stage high-speed disperser with split packing
- 中国化学工程学报（英文版） 2019年27卷第4期页码：772-780
- Affiliations：
  
  1. State Key Laboratory of Chemical Resource Engineering, School of Chemical Engineering, Beijing University of Chemical Technology,Beijing,China,100029
  2. Beijing Advanced Innovation Center for Soft Matter Science and Engineering, Beijing University of Chemical Technology,Beijing,China,100029
- Author bio：
- Funds：
- DOI：10.1016/j.cjche.2018.10.012
  中图分类号：
- 纸质出版：2019
- Accepted：
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Tao Ai, Aslam M. Mudassar, Ziqi Cai, 等. Mass transfer area in a multi-stage high-speed disperser with split packing[J]. 中国化学工程学报（英文版）, 2019,27(4):772-780.

Tao Ai, Aslam M. Mudassar, Ziqi Cai, Zhengming Gao. Mass transfer area in a multi-stage high-speed disperser with split packing[J]. Chinese Journal of Chemical Engineering, 2019, 27(4): 772-780.
Tao Ai, Aslam M. Mudassar, Ziqi Cai, 等. Mass transfer area in a multi-stage high-speed disperser with split packing[J]. 中国化学工程学报（英文版）, 2019,27(4):772-780. DOI： 10.1016/j.cjche.2018.10.012.

Tao Ai, Aslam M. Mudassar, Ziqi Cai, Zhengming Gao. Mass transfer area in a multi-stage high-speed disperser with split packing[J]. Chinese Journal of Chemical Engineering, 2019, 27(4): 772-780. DOI： 10.1016/j.cjche.2018.10.012.

摘要

Abstract

In this study

the mean droplet diameter in the cavity zone and the total mass transfer area of a multi-stage highspeed disperser (HSD) reactor with different packing combinations were measured and evaluated. The effects of rotational speed and packing radius

as well as the packing ring radius and numbers

on the mean droplet diameter and the total mass transfer area were evaluated. A model was established to calculate the mass transfer area in the cavity zone in the HSD reactor

and it was found that the packings contribute 61%-82% of the total mass transfer area. A correlation for predicting the mass transfer area in the packing zone was regressed by the dimensionless analysis method. An enhancement factor based on the mass transfer area in the packing zone was proposed to evaluate the effect of packing combination on mass transfer area. Two optimum packing combinations were proposed in consideration of the mean droplet diameter and the enhancement factor.

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