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Flow pattern maps for particle-fluid mixture transport in a horizontal pipe - application of a three-layer model

机译:水平管中颗粒流体混合物输送的流动模式图 - 应用三层模型

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摘要

A modified three-layer model was applied to model particle-fluid mixture flow in a horizontal pipe, the viscoelastic properties of carrier polymer solution were taken into consideration, and the Deborah number was used to calculate solid-fluid friction factor. An energy equation was applied to determine temperature distribution of carrier fluid along a horizontal pipe to accurately represent the rheological properties of carrier fluid. During the transport process, particles quickly settle out of carrier fluid and accumulate on pipe bottom forming a particle bed, so a particle bed load flow is observed. The transport mechanisms of particles in moving particle bed are govern by fluidization, which causes the height of this layer to be small and equal to 2~5 times of particle diameter. In addition, the pressure drop is composed of solid-fluid and solid-solid friction loss, which dominate the hydrodynamic performance at different stages.
机译:将改性的三层模型应用于模型水平管中的颗粒流体混合物流动,考虑了载体聚合物溶液的粘弹性特性,使用脱古拉数来计算固体流体摩擦系数。 施加能量方程以确定沿水平管的载体流体的温度分布,以精确地代表载体流体的流变性质。 在运输过程中,颗粒在载体流体中快速沉降并积聚在管底上形成颗粒床,因此观察到颗粒床载荷流动。 移动颗粒床中的颗粒的传输机制是通过流化的控制,这使得该层的高度小并且等于粒径的2〜5倍。 此外,压降由固体流体和固体固体摩擦损失构成,其在不同阶段的水动力学性能中占主导地位。

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