Abstract

A solid-liquid mixing system has a significant role in the suspension polymerization, crystallization, adsorption, and solid-catalyzed reactions. In this study, Electrical Resistance Tomography (ERT) was employed to investigate the effect of the particle size, the design parameters such as impeller type, impeller clearance and impeller diameter as well as operating conditions such as impeller speed, impeller pumping mode, and solids concentration on the mixing of micron sized latex particles in a slurry reactor. The ERT data were used to calculate the concentration profile and the degree of homogeneity in three dimensions, as a function of design parameters and operating within the reactor. In this work, tap water and latex particles (5.2 µm, 8.5 µm, 9.1 µm) were used as liquid and solid phase, respectively. Six axial impellers were utilized (A310, A100, A200, A320, A315, 3AM) with impeller speed (N) varying from 252 rpm to 400 rpm. Impeller diameter to tank diameter ratios (D/T) were in the range of 0.29 to 0.47 while, the impeller clearance (C/T) was changed in the range of T/3.8 to T/2.5. Impeller pumping was tested in both downward and upward directions. The concentration of latex particles was ranged between 15 wt% and 30 wt%. This study shows that the level of homogeneity in a solid-liquid mixing system improved with the increase in impeller speed. However, after achieving the maximum level of homogeneity, any further rise in the impeller speed had a detrimental effect on the level of homogeneity. A310 impeller, wtih D/T ratio of 0.31, demonstrated the highest level of homogeneity while the upward pumping direction was found to be more efficient than the downward one. In addition, a clearance of T/3 proved to create the highest level of homogeneity. Also, the results showed that a rise in the size and concentration of particles decreases the level of homogeneity. Thus, 5.2 µm latex particles with the concentration of 15 wt% demonstrated the highest level of homogeneity. Applying the findings of this study will lead to improved equipment design, chemical cost reduction, increased production rate, improved quality of products, and more efficient use of power in slurry reactors.

Highlights

  • Solid-liquid mixing processes are widely used in industry, such as coal-water slurries, paperpulp slurries, polymer dispersions, ion-exchange resins, and sugar crystal slurries

  • The Electrical Resistance Tomography was successfully used to investigate the quality of solid-liquid mixing in response to any changes in design parameters such as impeller type, impeller diameter, and impeller clearance, as well as operating conditions, and particle size

  • The level of homogeneity was calculated using the concentration distribution data obtained from Electrical Resistance Tomography (ERT) measurements

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Summary

Introduction

Solid-liquid mixing processes are widely used in industry, such as coal-water slurries, paperpulp slurries, polymer dispersions, ion-exchange resins, and sugar crystal slurries. In all these processes, a certain degree of mixing is required to achieve the desired result. The mixing of solid-liquid systems has been extensively studied in the past, the lack of enough information about the optimization of the solid-liquid mixing, especially the mixing of micron sized particles in a liquid is realized This project, with the collaboration of Xerox Research Center of Canada, aims to optimize the mixing of micron sized latex particles in a slurry reactor. The results of this study are expected to improve the quality of products, decrease manufacturing costs, and lead to more efficient use of power in slurry reactors

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