[1] RUIZ B G, GOMEZ-LAVIN S, DIBAN N, et al. Efficient electrochemical degradation of poly- and perfluoroalkyl substances (PFASs) from the effluents of an industrial wastewater treatment plant[J]. Chemical Engineering Journal, 2017, 322: 196-204. doi: 10.1016/j.cej.2017.04.040
[2] 黄琳琳, 李珊珊, 刘峻峰, 等. 电催化氧化/EGSB/SBR处理养牛场废水的效能研究[J]. 中国给水排水, 2019, 35(23): 1-5.
[3] JUTTER K, GALLA U, SCHMOEDER H. Electrochemical approaches to environmental problems in the process industry[J]. Electrochimica Acta, 2000, 45: 2575-2594. doi: 10.1016/S0013-4686(00)00339-X
[4] LIRA-TECO J E, RIVERA F, FARIAS-MOGUEL O, et al. Comparison of experimental and CFD mass transfer coefficient of three commercial turbulence promoters[J]. Fuel, 2016, 167: 337-346. doi: 10.1016/j.fuel.2015.11.053
[5] 韩金磊. 基于计算流体力学的电化学反应器流场模拟机结构优化[D].长春: 吉林大学, 2011.
[6] BENGOA C, MONTILLET A, LEGENTILHOMME P, et al. Characterization and modeling of the hydrodynamic behavior in the filter-press-type FM01-LC electrochemical cell by direct flow visualization and residence time distribution[J]. Industrial & Engineering Chemistry Research, 2000, 39(7): 2199-2206.
[7] RIVERA E P, RIVERA F F, CRUZ-DIAZ M R, et al. Numerical simulation of mass transport in a filter press type electrochemical reactor FM01-LC: Comparison of predicted and experimental mass transfer coefficient[J]. Chemical Engineering Research & Design, 2012, 90(11): 1969-1978.
[8] WANG J D, LI T T, ZHOU M M, et al. Characterization of hydrodynamics and mass transfer in two types of tubular electrochemical reactors[J]. Electrochimica Acta, 2015, 173: 698-704. doi: 10.1016/j.electacta.2015.05.135
[9] 刘伟京, 李根锋, 徐军, 等. 厌氧折流板反应器的水力流态模拟及优化[J]. 中国给水排水, 2012, 28(11): 6-9. doi: 10.3969/j.issn.1000-4602.2012.11.002
[10] 柳蒙蒙, 陈梅雪, 杨敏, 等. 基于CFD的大型膜生物反应器的设计及运行优化[J]. 环境工程学报, 2018, 12(2): 552-558. doi: 10.12030/j.cjee.201708022
[11] MARTINEZ-DELGADILLO S A, MOLLINEDO-PONCE H, MENDOZA-ESCAMILLA V, et al. Residence time distribution and back-mixing in a tubular electrochemical reactor operated with different inlet flow velocities, to remove Cr(VI) from wastewater[J]. Chemical Engineering Journal, 2010, 165: 776-783. doi: 10.1016/j.cej.2010.09.066
[12] DURAN J E, TAGHIPOUR F, MOHSENI M, et al. CFD modeling of mass transfer in annular reactors[J]. International Journal of Heat and Mass Transfer, 2009, 52(23/24): 5390-5401.
[13] SANTOS J, GERALDES V, VELIZAROV S, et al. Characterization of fluid dynamics and mass-transfer in an electrochemical oxidation cell by experimental and CFD studies[J]. Chemical Engineering Journal, 2010, 157(2/3): 379-392.
[14] 张艺龙. 电催化氧化体系效能预测模型构建及反应器构型优化设计[D]. 哈尔滨: 哈尔滨工业大学, 2013.
[15] SU J, LU H Y, XU H, et al. Mass transfer enhancement for mesh electrode on a tubular electrochemical reactor using experimental and numerical simulation method[J]. Russian Journal of Electrochemistry, 2011, 47: 1293-1298. doi: 10.1134/S1023193511110140
[16] RIVER F F, PONCE D L C, WALSH F C, et al. The reaction environment in a filter-press laboratory reactor: The FM01-LC flow cell[J]. Electrochimica Acta, 2015, 161: 436-452. doi: 10.1016/j.electacta.2015.02.161
[17] GRIFFITHS M, CARLOS P D L. Mass transport in the rectangular channel of a filter-press electrolyzer (The FM01-LC reactor)[J]. AIChE Journal, 2005, 51(2): 682-687. doi: 10.1002/aic.10311
[18] WALSH F C. A First Course in Electrochemical Engineering[M]: Romsey: The Electrochemical Consultancy, 1993.
[19] 苏静. 有机污染物电化学氧化反应器的流体动力学和传质性能研究[D]. 长春: 吉林大学, 2011.