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首页> 外文期刊>Chemical Engineering Science >Numerical simulation of the gas-particle turbulene flow in riser reactor based on k-#epsilon#-k_p-#epsilon#_p-#THETA# two-fluid model
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Numerical simulation of the gas-particle turbulene flow in riser reactor based on k-#epsilon#-k_p-#epsilon#_p-#THETA# two-fluid model

机译:基于k-#epsilon#-k_p-#epsilon#_p-#THETA#两流体模型的立管反应器中气体颗粒湍流的数值模拟

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摘要

A k-#epsilon#-k_p-#epsilon#_p-#THETA# two-fluid modcl is established to simulate thegas-article turbulent flow in the riser section of a circulating fluidized bed (CFB) reactor. The model, based on the kinetic theory of granular flow simulates both the gas phase and particle phase by low Reynolds number turbulent model, taking into account the trubulent interaction between gas and particles. The model is coded and solved using a computational fluid dynamic software package CFX4 by AEAT to simulate the two-dimensional, isothermal flow in a riser reactor. The predicted results show satisfactory agreements with experimental data. Moreover, the detailed analysis indicates that the interaction between the turbulence of ga sand that of particles is a crucial factor that influences the predicted results.
机译:建立了k-ε-k-p-ε-p-#THETA#两流体模型,以模拟循环流化床(CFB)反应器提升管段中的气体-湍流。该模型基于颗粒流动力学理论,通过考虑气体和颗粒之间的湍流相互作用,通过低雷诺数湍流模型模拟了气相和颗粒相。使用AEAT的计算流体动力学软件包CFX4对模型进行编码和求解,以模拟提升管反应器中的二维等温流动。预测结果表明与实验数据令人满意。此外,详细的分析表明,颗粒的湍流之间的相互作用是影响预测结果的关键因素。

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