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It also gives much more control over the process that a conventional CIL plant without a thickener. The CIL process is viable if there is sufficient gold content, carbonates/clays in the ore which will "rob" some gold in solution, and it leaches in 8 13 hours.

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The UF its in The range of 50 56 %solids and they have auto dilution in the feedwell for big capacity, the conventional its in the range of 50 54 % of solids. If you need a bigger %solid in the underflow you must think in a paste thickener. But (it's a good idea) you can increase %solids in the UF of a thickener putting a dewatering screen.

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About conventional thickener sizing methods(C C, T F, W N) these methods use the desired underflow solids concentration while in an especial case, accurate prediction of underflow solids concentration in a green field project may be not possible in practical point of view. Furthermore, in conventional methods lowest settling flux is considered

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The underflow from both thickeners were combined with tailings stream No.1, a coarser solids stream from the magnetic separators, before being split into another two 53m diameter conventional thickeners. The final underflow at 40 45% solids was pumped to the tailings dam, with overflow from each thickener

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Conventional Thickeners are generally incorporated in heavy duty applications when the underflow density is high and substantial torques are required to convey the settled solids from the periphery to the central outlet for pumping away. Likewise, thickeners are often used for storage to facilitate the continuous feeding of downstream filters

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No. 188, Xinhai Street, Fushan high-tech industrial development district, Yantai, Shandong, China
 

Beijing Branch

D501/D505, Lifi Space, Sixinzhuang Street, Chaoyang District Beijing, China
 

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