Imperial College London

Dr Catalina A. Pino-Muñoz

Faculty of EngineeringDepartment of Earth Science & Engineering

Research Associate in Flow Battery Modelling
 
 
 
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Contact

 

c.pino15 Website

 
 
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Location

 

4.93/10Royal School of MinesSouth Kensington Campus

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Summary

 

Publications

Citation

BibTex format

@inproceedings{Yianatos:2012,
author = {Yianatos, J and Bergh, L and Vinnett, L and Pino, C and Díaz, F},
pages = {5935--5946},
title = {Modelling of residence time distribution in regrinding vertimills},
year = {2012}
}

RIS format (EndNote, RefMan)

TY  - CPAPER
AB - The regrinding stage is necessary to achieve the particle size (liberation) for the final upgrade in the cleaning flotation process. At present, vertical mills (Vertimill) are employed at industrial scale, using small steel balls as grinding media. The regrinding process characterization requires mixing regime knowledge along with the mean residence time of the liquid and solid phases. The residence time distribution (RTD) and the actual mean residence time estimations from theoretical relationships are complex due to the presence of three components (solid mineral, balls and water), mass transport characteristics and segregation affecting solid holdup. Therefore, the experimental RTD determination is suitable for industrial mills. In this work, RTD measurements were performed in two different industrial flotation plants. Both plants operate with Vertimills of 1000-1500 HP in the regrinding process with different circuit arrangements according to the plant treatment capacity. The RTD was measured using the radioactive tracer technique. This technique allows for non-invasive tracer detection where the procedure consists of selecting a liquid (Br82 in aqueous solution) or solid (irradiated solid) tracer for RTD data acquisition in real time. The RTD was modelled by the Large and Small Tanks in Series (LSTS) model, which allowed the characterization of the different mixing regimes for both liquid and solids in the regrinding mills. Effective mean residence times in the range 2-11 min were obtained with RTD shapes similar to those obtained in tumbling ball mills. It was found that residence times of liquid and fine particles were similar, which is consistent with results observed in other mixing systems, e.g. mechanical flotation cells. Also, the mean residence times estimated from the RTD allowed the mass balance adjustment to be validated from metallurgical sampling data. RTD estimations are useful for better understanding the Vertimill behaviour and to identify the a
AU - Yianatos,J
AU - Bergh,L
AU - Vinnett,L
AU - Pino,C
AU - Díaz,F
EP - 5946
PY - 2012///
SP - 5935
TI - Modelling of residence time distribution in regrinding vertimills
ER -