Influence of current density on transfer characteristics in electrolysis cell of chlor-alkali industry

被引:0
|
作者
School of Chemical Engineering, Shenyang University of Chemical Technology, Shenyang [1 ]
Liaoning
110142, China
不详 [2 ]
100176, China
不详 [3 ]
Liaoning
110015, China
机构
[1] School of Chemical Engineering, Shenyang University of Chemical Technology, Shenyang, 110142, Liaoning
[2] Bluestar (Beijing) Chemical Machinery Co. Ltd., Beijing
[3] Bluestar Shenyang Research Institute of Light Industry Machinery, Shenyang, 110015, Liaoning
来源
Huagong Xuebao | / 3卷 / 915-923期
关键词
CFD; Current density; Electrolysis cell; Numerical simulation; Two-phase flow;
D O I
10.11949/j.issn.0438-1157.20141360
中图分类号
学科分类号
摘要
To investigate the influence of current density on transfer characteristics in the electrolysis cell of chlor-alkali industry, the fluid flow, heat and mass transfer of anode chamber at different current densities were simulated numerically using computational fluid dynamics software. The distributions of velocity, temperature and concentration in a grille of the anode chamber were obtained. Taking liquid circulation rate, maximum velocity near the membrane, temperature and concentration at the membrane surface as indices, the performance of the electrolysis cell at different current densities was evaluated. Liquid circulation rate and temperature of membrane surface increased and concentration of brine decreased with increasing current density. Under typical working conditions for current density of 4.5 kA·m-2, average temperature of the electrolysis cell and of the membrane surface were 86.39℃ and 87.40℃, respectively. Average temperatures of the electrolysis cell and the membrane surface could be maintained at the values of the typical working conditions by lowering inlet temperature of brine when current density increased. ©, 2015, Chemical Industry Press. All right reserved.
引用
收藏
页码:915 / 923
页数:8
相关论文
共 25 条
  • [1] Zhou Q., Wang Q., Jiang Y., Research on operation technologies of Asahi Kasei NCZ zero-polar distance electrolyzers, Chlor-Alkali Industry, 48, 10, pp. 13-16, (2012)
  • [2] Zhang H., Li G., Hao S., Comparison of running between membrane electrode-distance electrolyzers and high-current density electrolyzers, Chlor-Alkali Industry, 50, 6, pp. 12-15, (2014)
  • [3] Sui Y., The impact factors of current efficiency of ionic membrane electrolyzer, Guangzhou Chemical Industry, 42, 2, (2014)
  • [4] Li Z., Dong L., Problems and solutions of ionic membrane electrolyzer operation, China Chlor-Alkali, 4, pp. 5-7, (2013)
  • [5] Pang Z., Operating points of NBH-2.7 type natural circulation bipolar type high current density ion-exchange membrane electrolysis device, China Chlor-Alkali, 3, (2014)
  • [6] Zhu J., Zhang Z., Luo J., Technical reformation and running effect of NCH ion-exchange membrane electrolyzer, China Chlor-Alkali, 12, pp. 5-6, (2012)
  • [7] Cai D., Xiong P., Ma L., Zhou J., Process control and running improvement of electrolyzers transformed into membrane-electrode distance type, Chlor-Alkali Industry, 50, 5, pp. 6-9, (2014)
  • [8] Aldas K., Application of a two-phase flow model for hydrogen evolution in an electrochemical cell, Applied Mathematics and Computation, 154, pp. 507-519, (2004)
  • [9] Mat M.D., Aldas K., Application of a two-phase flow model for natural convection in an electrochemical cell, International Journal of Hydrogen Energy, 30, pp. 411-420, (2005)
  • [10] Farshad A., Hasan R., Applying a modified two-fluid model to numerical simulation of two-phase flow in the membrane chlor-alkali cells, Iranian Journal of Chemistry & Chemical Engineering-International English, 27, 3, pp. 51-61, (2008)