Abstract

The present study examines the possibility of using an industrial stirred chemical reactor, originally employed for liquid–liquid mixtures, for operating with two-phase liquid–solid suspensions. It is critical when obtaining a high-quality chemical product that the solid phase remains suspended in the liquid phase long enough that the chemical reaction takes place. The impeller was designed for the preparation of a chemical product with a prescribed composition. The present study aims at finding, using a numerical simulation analysis, if the performance of the original impeller is suitable for obtaining a new chemical product with a different composition. The Eulerian multiphase model was employed along with the renormalization (RNG) k-ε turbulence model to simulate liquid–solid flow with a free surface in a stirred tank. A sliding-mesh approach was used to model the impeller rotation with the commercial CFD code, FLUENT. The results obtained underline that 25% to 40% of the solid phase is sedimented on the lower part of the reactor, depending on the initial conditions. It results that the impeller does not perform as needed; hence, the suspension time of the solid phase is not long enough for the chemical reaction to be properly completed.

Highlights

  • MMUT, Faculty of Mechanical Engineering, Politehnica University Timisoara, 300006 Timisoara, Romania; Citation: Stuparu, A.; Susan-Resiga, Abstract: The present study examines the possibility of using an industrial stirred chemical reactor, originally employed for liquid–liquid mixtures, for operating with two-phase liquid–solid suspensions

  • The impact of the hydrodynamic chemical multiphaseofreactions, the hydrodynamic plays a major role in the field For upon the performances an industrial stirred reactor field is determined by the specific mixing of the two phases and in the mass transfer

  • For reactors operating with a two-phase flow, solid and liquid,field it is upon the performances of an stirred reactor is determined by the specific geomrecommended to monitor theindustrial solid particle distribution to check if the distribution is in etry with of the

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Summary

Introduction

MMUT, Faculty of Mechanical Engineering, Politehnica University Timisoara, 300006 Timisoara, Romania; Citation: Stuparu, A.; Susan-Resiga, Abstract: The present study examines the possibility of using an industrial stirred chemical reactor, originally employed for liquid–liquid mixtures, for operating with two-phase liquid–solid suspensions It is critical when obtaining a high-quality chemical product that the solid phase remains suspended in the liquid phase long enough that the chemical reaction takes place. The sedimentation of the solid particles must be prevented by the stirring mechanism and must ensure a homogenous distribution of the solid particles in the entire volume of liquid Another important aspect for obtaining a quality product from the chemical reaction inside the reactor is to prolong the contact time between the solid particles and the liquid phase, and the impeller plays a major role in this matter. A great number of studies from all over the world have performed numerical

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