化工学报 ›› 2015, Vol. 66 ›› Issue (5): 1642-1648.DOI: 10.11949/j.issn.0438-1157.20141651

• 流体力学与传递现象 • 上一篇    下一篇

排气管直径与深度对水力喷射空气旋流器传质性能的影响

程治良, 徐飞, 全学军, 邱发成, 代明星   

  1. 重庆理工大学化学化工学院, 重庆 400054
  • 收稿日期:2014-11-03 修回日期:2015-02-05 出版日期:2015-05-05 发布日期:2015-05-05
  • 通讯作者: 全学军
  • 基金资助:
    国家自然科学基金项目(21176273);重庆理工大学基金项目(2014ZD04,2014XH16)。

Effect of diameter and length of vortex finder in water-sparged aerocyclone reactor on its mass transfer performance in air stripping of ammonia

CHENG Zhiliang, XU Fei, QUAN Xuejun, QIU Facheng, DAI Mingxing   

  1. School of Chemistry and Chemical Engineering, Chongqing University of Technology, Chongqing 400054, China
  • Received:2014-11-03 Revised:2015-02-05 Online:2015-05-05 Published:2015-05-05
  • Supported by:
    supported by the National Natural Science Foundation of China (21176273) and the Research Project of Chongqing University of Technology (2014ZD04, 2014XH16).

摘要: 对水力喷射空气旋流器(WSA)的中心排气管直径De和排气管插入深度S进行了设计优化研究,实验考察了不同DeS对WSA脱氨传质系数KLa和气相压降的影响,提出了综合评价传质过程效率的概念——单位压降传质效率ηp,讨论了DeS的设计取值。研究表明,当De增大时,KLa和气相压降均随之降低,较小De的WSA具有较高的气液传质性能,但气相压降比较大,而KLa和气相压降均随S增大而增大。综合能效关系表明,随着De的增大ηp增大,随着S的增大ηp出现先增大后降低的趋势,WSA设计中De与WSA直径D之比De/D宜为0.42~0.53,S与WSA筒体长度H之比S/H适宜取值约为0.70。

关键词: 脱氨, 空气旋流器, 废水, 传质, 气液两相流

Abstract: Water-sparged aerocyclone (WSA) is a new gas-liquid mass transfer equipment, which takes the advantage of coupling effect of air cyclone and liquid jet fields. In order to improve its mass transfer performance and establish design principles, the effect of diameter (De) and length (S) of the vortex finder in the WSA on its mass transfer performance and air pressure drop in air stripping of ammonia was investigated and optimized. A new concept, mass transfer efficiency per gas pressure drop, ηp, and its calculation equation were put forward. The WSA with smaller De and longer S showed higher mass transfer efficiency than that with larger De and shorter S in air stripping of ammonia. However, this kind of WSA had higher air pressure drop, which would consume more energy. Calculation of ηp, which was a comprehensive indicator considering energy consumption and mass transfer efficiency, showed that it increased with the increase of De/D and S/H,but it deceased a little when S/H increased from 0.71 to 0.93. The optimal De/D and S/H should be 0.43 to 0.53 and 0.70, respectively. These results could be used as a guide for the design of WSA with good mass transfer performance.

Key words: ammonia removal, aerocyclone, wastewater, mass transfer, gas-liquid flow

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