Designing For Paste Thickening

Canadian Institute of Mining, Metallurgy and Petroleum
Ian Arbuthnot Brad Garraway Richard Triglavcanin Tim Edwards Darren Colwell Ken Roberts
Organization:
Canadian Institute of Mining, Metallurgy and Petroleum
Pages:
32
File Size:
7784 KB
Publication Date:
Jan 1, 2005

Abstract

"In the mineral processing industries, there is an increasing need to design thickeners which are able to produce high density underflows usually referred to as “paste”.The behaviour of a flocculated suspension in compression needs to be well understood in order to arrive at a reliable thickener tank configuration (i.e. diameter, cone angle and depth) for a required paste result.As a suspension approaches paste consistency, it’s fluid characteristics change markedly. It develops a high yield stress, and may have an increased tendency to form agglomerates, which lead to a phenomenon known as “rotating beds”, “donuts”, or “islands”. These characteristics present challenges to the designer of the rake mechanism.The subject paper addresses the requirements for designing a paste thickener, covering the following topics:o Testwork for thickener sizingo Design of rake mechanismso Suspension rheology and effect on designo Case studiesTESTWORK AND SIZING FOR PASTE THICKENERSThickening slurries to the maximum possible density (paste) is becoming increasingly common. Applications such as Autoclave feed thickeners, paste backfill and some counter current washing (CCD) circuits are all examples of potential paste thickening applications. The principle of paste thickeners is that the compression zone is much deeper than on either high rate (HRT) or high compression (HCT) units; generally 3 metres or more. As the compression zone gets deeper, theunderflow density for a given flux rate (tph/m2) increases, as a result of two factors:1. Longer bed settling time. Settling flocs move relative to one another and release interstitial fluid when they are in compression. Increasing bed residence time achieves higher density underflow as more fluid is removed.2. The nett weight of the bed creates a compressive force on the settling flocs. This force increases with depth, so that the flocs at the bottom of the bed experience the highest compressive force. This represents the driving force to expel interstitial fluid and hence increase bed density."
Citation

APA: Ian Arbuthnot Brad Garraway Richard Triglavcanin Tim Edwards Darren Colwell Ken Roberts  (2005)  Designing For Paste Thickening

MLA: Ian Arbuthnot Brad Garraway Richard Triglavcanin Tim Edwards Darren Colwell Ken Roberts Designing For Paste Thickening. Canadian Institute of Mining, Metallurgy and Petroleum, 2005.

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