Centrifugal slurry pumps are widely used for hydraulic transportation of solids in the mining and dredging industries. The performance of these pumps degrades when handling a slurry flow. The level of complexity increases for a pump handling non-Newtonian (non-settling) slurries, especially when these slurries exhibit a high yield stress. The viscous effect is the primary source of performance loss in non-Newtonian slurries, and this loss is more pronounced in efficiency than in head. In sets of experiments conducted at GIW Industries, Inc. [1], the measured pump performance and pipeline friction loss were captured while testing a phosphate clay slurry at different solids concentrations. This slurry was tested at a range of yield stresses from 100–600 Pa, established by varying the solids concentration. The tested pump was a GIW-LCC-M 80-300 type, featuring a three-vane, closed-shroud impeller with a 0.3-m diameter. A high-fidelity CFD simulation was developed and simulated, with the measured rheology used as an input to the CFD simulations. The simulation results showed a good agreement with the tested performance. The outcome of these simulations could be used as a resource for predicting the pump derate within the testing range, as the results could help in selecting the pump size and determining the power requirement.
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Garman et al. (2024) studied this question.
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