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首页> 外文期刊>Powder Technology: An International Journal on the Science and Technology of Wet and Dry Particulate Systems >Application of CPFD method in the simulation of a circulating fluidized bed with a loop seal Part II—Investigation of solids circulation
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Application of CPFD method in the simulation of a circulating fluidized bed with a loop seal Part II—Investigation of solids circulation

机译:CPFD方法在带环封的循环流化床模拟中的应用第二部分:固体循环研究

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摘要

The Computational Particle Fluid Dynamics (CPFD) numerical method was used to study the gas solid flow characteristics in a circulating fluidized bed (CFB) with a loop seal in this work. The influences of operating parameters, including loop seal aeration rate (Q_l), fluidized air velocity in the riser (U_r) and total bed inventory (M_p) on the solid circulation characteristics were mainly investigated in this part. The solid circulating rate (G_s), total pressure drop in the riser (ΔP_r), particle packed height (H_s), pressure gradient (ΔP_s/H_s) and gas flow rate (G_g) in the stand-pipe, as well as the particle concentration and pressure distributions in the loop were carefully analyzed under different operating conditions. The simulation results were compared with the experimental results also reported in this work and good agreements were obtained. The results showed that the increase of Q_l resulted in a decrease of H_s and increases of G_s, AP_r and ΔP_s/H_s. By increasing U_r, the increase of G_s was limited and the maximum value was approaching. An increase of M_p also had a positive effect on G_s while an elevated H_s was obtained as a result of mass and pressure balance. No gas bypass flow phenomenon occurred in the operating cases of this work from the simulation results. The pressure drop in the riser could be properly predicted while the gas-solid interactions in the standpipe and loop seal were slightly underestimated by the CPFD method, where a relatively lower ΔP_s/H_s was obtained for CFB modeling. KCFB;; Solids circulation;; Pressure distribution;; CPFD;; Modeling
机译:在这项工作中,使用计算粒子流体动力学(CPFD)数值方法来研究具有环形密封件的循环流化床(CFB)中的气固流动特性。这部分主要研究了运行参数,包括环路密封充气率(Q_1),立管中的流化空气速度(U_r)和总床存量(M_p)对固体循环特性的影响。固体循环速率(G_s),立管中的总压降(ΔP_r),颗粒堆积高度(H_s),竖管中的压力梯度(ΔP_s/ H_s)和气体流速(G_g)以及颗粒在不同的操作条件下,仔细分析了回路中的浓度和压力分布。将仿真结果与该工作中报告的实验结果进行了比较,并获得了良好的协议。结果表明,Q_l的增加导致H_s的减少和G_s,AP_r和ΔP_s/ H_s的增加。通过增加U_r,G_s的增加受到限制,最大值接近。 M_p的增加也对G_s产生积极影响,而质量和压力平衡导致H_s升高。从模拟结果来看,在这项工作的运行情况下没有发生气体旁路流动现象。通过CPFD方法可以略微低估立管和环路密封中的气固相互作用,而可以适当地预测立管中的压降,对于CFB建模,ΔP_s/ H_s相对较低。 K CFB ;;固体循环;压力分布; CPFD ;;造型

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