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鼓泡塔中离子液体一空气两相流的CFD-PBM耦合模拟
  • ISSN号:0438-1157
  • 期刊名称:《化工学报》
  • 时间:0
  • 分类:TQ028.8[化学工程]
  • 作者机构:[1]中国科学院过程工程研究所多相复杂系统国家重点实验室,北京100190, [2]中国科学院研究生院,北京100049
  • 相关基金:国家自然科学基金重点项目(21036007).
中文摘要:

针对咪唑类离子液体介质,采用Euler—Euler双流体模型与群平衡模型(PBM)耦合的方法,引入由实验结果拟合获得的适用于该介质的气液相间曳力系数模型,对内径0.203m、高2m的鼓泡塔中离子液体一空气两相流进行计算流体力学模拟,研究了不同表观气速下塔内气液两相速度场分布、气含率和气泡尺寸分布等流体动力学性质。与现有的相间曳力系数模型Schiller-Naumann模型模拟结果对比,采用本文模型得到的气含率与实验值吻合更好,气泡尺寸分布与实验结果一致。

英文摘要:

Abstract: Ionic liquids have been regarded as a new and effective solvent and absorbent, however, the fluid dynamics of ionic liquids have not been thoroughly investigated. Computational fluid dynamics (CFD) is an increasingly important method to understand the fluid dynamics of multiphase fluid. In this work, the gas holdup, bubble size distribution and flow velocities of ionic liquid-air two-phase flow in bubble column were investigated by using Euler-Euler method and population balance model (PBM) coupled numerical model. Considering the special properties of ionic liquids, ionic liquid drag coefficient and Schiller-Naumann model were both used as interphase drag coefficient. The numerical simulation results showed that the general gas holdup and the uniformity of gas distribution both increased with increasing superficial gas velocity. The predicted general gas holdup with ionic liquid drag coefficient agreed with the experimental data better than that of Schiller-Naumann model. Ionic liquid drag coefficient overestimated the general gas holdup and the average error of simulation result with drag coefficient was 8.1~//00. Schiller-Naumann underestimated general gas holdup and the average error of simulation result with Schiller-Naumann model was 22.8~/6o. The bubble size distribution was studied by using PBM model, discrete method was used to solve the population balance equations, and the bubbles in the column were divided into 10 groups ranging from 1 mm to 9.85 mm. The simulated bubble size distributions agreed with experimental results. The bubbles of low superficial gas velocity were larger than those of high superficial gas velocity, and the bubblesize range o{ low gas velocity was wider than that of high gas velocity. This was caused by different bubble coalescence and breakup rates of different superficial gas velocities The study of bubble and liquid velocity distribution showed that the uniformity of liquid velocity in the column increased with increasing gas velocity.

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期刊信息
  • 《化工学报》
  • 中国科技核心期刊
  • 主管单位:中国科学技术协会
  • 主办单位:中国化工学会 化学工业出版社
  • 主编:李静海
  • 地址:北京市东城区青年湖南街13号
  • 邮编:100011
  • 邮箱:hgxb126@126.com
  • 电话:010-64519485
  • 国际标准刊号:ISSN:0438-1157
  • 国内统一刊号:ISSN:11-1946/TQ
  • 邮发代号:2-370
  • 获奖情况:
  • 中国科协优秀期刊二等奖,化工部科技进步二等奖,北京全优期刊奖,中国期刊方阵“双效”期刊,第三届中国出版政府奖
  • 国内外数据库收录:
  • 俄罗斯文摘杂志,美国化学文摘(网络版),荷兰文摘与引文数据库,美国工程索引,日本日本科学技术振兴机构数据库,中国中国科技核心期刊,中国北大核心期刊(2004版),中国北大核心期刊(2008版),中国北大核心期刊(2011版),中国北大核心期刊(2014版),中国北大核心期刊(2000版)
  • 被引量:35185