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超重力旋转床气相传质CFD仿真分析及实验验证

周晓伟,张新玉,杨斌,于平安   

  1. 哈尔滨工程大学动力与能源工程学院,黑龙江 哈尔滨 150001
  • 出版日期:2014-04-05 发布日期:2014-04-05

CFD simulation and experimental verification of gas phase mass transfer in rotating packed bed

ZHOU Xiaowei,ZHANG Xinyu,YANG Bin,YU Ping’an   

  1. School of Power and Engineering,Harbin Engineering University,Harbin 150001,Heilongjiang,China
  • Online:2014-04-05 Published:2014-04-05

摘要: 为了研究闭式循环柴油机中超重力旋转床的水吸收二氧化碳过程,开展了仿真与实验研究。建立旋转床三维物理模型,采用欧拉-拉格朗日两相流模型对气液流场进行流体力学计算。以希格比的溶质渗透理论为基础,设置气相源项,对液相吸收二氧化碳过程进行仿真。并通过实验验证不同操作参数对其吸收性能的影响。结果表明:吸收过程在靠近丝网与分布器位置较为强烈,吸收性能随着旋转床转速与吸收因数增加而加强,随着进气浓度增加而降低。仿真中设置的源项能模拟床内吸收的过程,仿真与实验得出的液相传质单元数有较高的一致性,平均相对误差在10%左右,最大误差为20.6%,在高进气浓度下仿真偏差较大。总的来说,仿真能较好地模拟实际二氧化碳在旋转床中的吸收过程。

关键词: 旋转床, 欧拉-拉格朗日, 溶质渗透模型, 二氧化碳吸收

Abstract: Simulation and experimental research were performed to study the mass transfer process of rotating packed bed in closed-cycle diesel engine. A 3-D physical model was set up. Euler-Lagrange model was used to solve the gas-liquid phase flow field in the model. Based on Higbie’s percolation theory,gas phase source term was set up to simulate the process of water dissolving CO2. Experiments were conducted to determine the effect of different operation parameters on absorption ability. The result showed that the mass transfer process was more intense around the distributor and mesh wire. The performance was better with higher absorption factor and faster rotational speed,also with lower inlet CO2 concentration. The number of transfer unit obtained from simulation was similar with that obtained from experiments,and the averaged relative error was around 10% and the maximum error was 20.6% so the source term could simulate the actual absorption process and the actual CO2 absorption process could be simulated.

Key words: rotating packed bed(RPB), euler-lagrange model, percolation model, CO2 absorption

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