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Particulate flows at moderate particle Reynolds numbers are important in critical engineering and geological applications. This experimental study explores neutrally buoyant suspensions in an outer-rotating coaxial rheometer for solid fractions, φ , from 0.1 to 0.5, and particle Reynolds number, $Re$ , from 0.5 to 800, covering laminar, transitional and turbulent regimes; $Re$ is defined in terms of the square of the particle diameter and the shear rate. For 0.1 < φ < 0.4 and $0.5 < Re <10$ , the direct torque measurements normalised by the laminar flow torque, M/Mₗₐₘ , are independent of $Re$ , but depend on φ . For the same range of φ and for $10< Re<100$ , the normalised torques depend on both φ and $Re$ , and show an increasing dependence on $Re$ . As $Re$ increases, the flow transitions to turbulence. Small particles delay the turbulent transition for φ 0.3 , while large particles augment the transition. A modified Reynolds number, Re^ , that depends linearly on the particle diameter and the maximum velocity, Uₒ , is introduced for both laminar and turbulent flows and shows a better correlation of the results as compared with $Re$ . For φ = 50\,% , the normalised torque minus the torque at zero rotational speed is nearly independent of Re^ . Rheological models based on Re^ and the Krieger–Dougherty relative viscosity are proposed in the laminar regime for 10< Re^ <500 ; in the turbulent regime, a correlation is proposed in terms of Re^ and φ for 1000< Re^ < 6000 .
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Song et al. (2024) studied this question.
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