Experiment for Partial Reflux Axial-Flow Cyclone Separator with Two-Stage Separation

被引：0

作者：

Liu B. ^{[1
]}

Feng J. ^{[1
]}

Xia Z. ^{[1
]}

Chang Y. ^{[1
]}

Peng X. ^{[1
]}

机构：

[1] School of Energy and Power Engineering, Xi'an Jiaotong University, Xi'an

来源：

Hsi An Chiao Tung Ta Hsueh | / 7卷 / 84-89期

关键词：

Axial-flow cyclone separator; Droplet diameter distribution; Liquid droplet; Reflux; Separation efficiency;

D O I：

10.7652/xjtuxb201707013

中图分类号：

学科分类号：

摘要：

To further enhance the efficiency of demister in a flue-gas after desulfuration by wet processes for power plant, a new type of partial reflux cyclone separator with two separation stages is proposed. An experiment rig is constructed to test the performance of cyclone separator, and a droplets generator is designed to produce liquid droplets with different diameters. Malvern particle size analyzer is adopted to obtain the droplet diameter distribution at the inlet and outlet of the separator, and the separation efficiency and resistance loss are measured for different separator parameters under various working conditions. The experiments show that the separation efficiency rises with the increasing number of reflux tanks. At the inlet velocity of 3.9 m/s, the efficiency of separator rises by 66.78% in the case of doubled number of reflux tanks. The efficiency of separator with reflux tanks centered on the separator top reaches higher than that with reflux tanks scattered along the separator. At the inlet velocity of 3.94 m/s, the efficiency rises by16.9%. The height of guide tube affects the efficiency of separator and there exists an optimum ratio of 0.32 between the height of guide tube and the separator. © 2017, Editorial Office of Journal of Xi'an Jiaotong University. All right reserved.

引用

页码：84 / 89

页数：5

共 9 条

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