Abstract

Decanter centrifuges are frequently used for thickening, dewatering, classification, or degritting in the mining industry and various other sectors. Their use in an industrial process chain requires a sufficiently accurate prediction of the product and the machine behaviour. For this purpose, experiments on a smaller pilot-scale are carried out for scale-up of a decanter centrifuge, which is usually a major challenge. Predicting the process behaviour of decanter centrifuges from laboratory tests is rather difficult. Basically, there are two common ways of scale-up: First, via analytical methods and the law of similarity, which often requires an enormous experimental effort. Second, using numerical models, which demands a mathematically and physically precise description of the multiple processes running simultaneously in such machines. This article provides an overview of both methods for scale-up of a decanter centrifuge. The concept of a previous developed numerical approach is introduced. Pros and cons of both scale-up methods are compared and further discussed. Experiments on lab-scale, pilot-scale, and industrial-scale decanter centrifuges with two different finely dispersed calcium carbonate water suspensions were carried out and simulations were done to investigate and prove the scale-up capability and transferability of the numerical approach.

Highlights

  • Solid-liquid separation is an important part of the process chains in many industry sectors, such as the mining industry

  • The work of Menesklou et al [13] has focused on modelling the conical part, and the results presented in this work are promising but demand further investigations regarding scale-up capability and transferability

  • Simulations are compared to experimental data to discuss the scale-up capability and transferability of this numerical approach

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Summary

Introduction

Solid-liquid separation is an important part of the process chains in many industry sectors, such as the mining industry. For the high throughputs typically expected in such applications, continuously operating decanter centrifuges are a reasonable option. They are frequently used for dewatering and classification of mineral products, such as calcium carbonate water slurries. Stahl [1] has demonstrated that changing operating parameters often has a contrary effect on the performance of solid-bowl centrifuges. The same separation result can be obtained by various parameter combinations of the process behaviour. This causes the geometry and process conditions to be unable to be scaled up linearly

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