Numerical investigation of the separation behaviours of fine particles in large dense medium cyclones

Research output: Contribution to journalArticleResearchpeer-review

Abstract

Use of large dense medium cyclones (DMCs) is a potential trend in the coal industry but its usage is limited by the poor separation efficiency of fine particles. This paper presents a numerical study of the multiphase flows and performance of DMCs used for coal preparation by means of the two-fluid model. The validity of the model has been verified by various applications. It is used here to study the behaviours of fine particles in a 2-m DMC that is larger than the biggest DMCs reported thus far in the coal industry. The numerical results show that in the extra-large DMC, the poor separation efficiency of fine particles gets worse compared to that of a widely used 1-m DMC. This deficiency is found to be attributed to the strong vortexes developed and the asymmetrical separation zone that can be characterised by the correlation between pressure gradient and tangential velocity. Several modifications with respect to mounting degree, operational Head, conical section length, and inlet number are introduced to improve the performance of the 2-m DMC. It is shown that the separation efficiency of fine particles in the 2-m DMC can be better compared to the 1-m DMC by increasing the Head or conical section length, because such modifications reduce the asymmetrical separation zone and/or amount of vortexes.
Original languageEnglish
Pages (from-to)35-45
Number of pages11
JournalInternational Journal of Mineral Processing
Volume142
DOIs
Publication statusPublished - 10 Sep 2015

Keywords

  • Dense medium cyclone
  • Fine particles
  • Separation
  • Two-fluid model
  • Simulation

Cite this

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title = "Numerical investigation of the separation behaviours of fine particles in large dense medium cyclones",
abstract = "Use of large dense medium cyclones (DMCs) is a potential trend in the coal industry but its usage is limited by the poor separation efficiency of fine particles. This paper presents a numerical study of the multiphase flows and performance of DMCs used for coal preparation by means of the two-fluid model. The validity of the model has been verified by various applications. It is used here to study the behaviours of fine particles in a 2-m DMC that is larger than the biggest DMCs reported thus far in the coal industry. The numerical results show that in the extra-large DMC, the poor separation efficiency of fine particles gets worse compared to that of a widely used 1-m DMC. This deficiency is found to be attributed to the strong vortexes developed and the asymmetrical separation zone that can be characterised by the correlation between pressure gradient and tangential velocity. Several modifications with respect to mounting degree, operational Head, conical section length, and inlet number are introduced to improve the performance of the 2-m DMC. It is shown that the separation efficiency of fine particles in the 2-m DMC can be better compared to the 1-m DMC by increasing the Head or conical section length, because such modifications reduce the asymmetrical separation zone and/or amount of vortexes.",
keywords = "Dense medium cyclone, Fine particles, Separation, Two-fluid model, Simulation",
author = "Z. Qi and S.B. Kuang and A.B. Yu",
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Numerical investigation of the separation behaviours of fine particles in large dense medium cyclones. / Qi, Z.; Kuang, S.B.; Yu, A.B.

In: International Journal of Mineral Processing, Vol. 142, 10.09.2015, p. 35-45.

Research output: Contribution to journalArticleResearchpeer-review

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AB - Use of large dense medium cyclones (DMCs) is a potential trend in the coal industry but its usage is limited by the poor separation efficiency of fine particles. This paper presents a numerical study of the multiphase flows and performance of DMCs used for coal preparation by means of the two-fluid model. The validity of the model has been verified by various applications. It is used here to study the behaviours of fine particles in a 2-m DMC that is larger than the biggest DMCs reported thus far in the coal industry. The numerical results show that in the extra-large DMC, the poor separation efficiency of fine particles gets worse compared to that of a widely used 1-m DMC. This deficiency is found to be attributed to the strong vortexes developed and the asymmetrical separation zone that can be characterised by the correlation between pressure gradient and tangential velocity. Several modifications with respect to mounting degree, operational Head, conical section length, and inlet number are introduced to improve the performance of the 2-m DMC. It is shown that the separation efficiency of fine particles in the 2-m DMC can be better compared to the 1-m DMC by increasing the Head or conical section length, because such modifications reduce the asymmetrical separation zone and/or amount of vortexes.

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