Simulation and Experimental Investigation of the Vacuum-Enhanced Direct Membrane Distillation Driven by a Low-Grade Heat Source
文献类型： 外文期刊
作者： Ma, Qingfen 1 ; Tong, Liang 1 ; Wang, Chengpeng 2 ; Cao, Guangfu 1 ; Lu, Hui 3 ; Li, Jingru 1 ; Liu, Xuejin 1 ; Feng, Xin 1 ; Wu, Zhongye 1 ;
作者机构： 1.Hainan Univ, Coll Mech & Elect Engn, Haikou 570228, Hainan, Peoples R China
2.Inst Seawater Desalinat & Multipurpose Utilizat, MNR, 55 Hanghai Rd, Tianjin 300192, Peoples R China
3.Chinese Acad Trop Agr Sci, Inst Environm & Plant Protect, Haikou 571101, Hainan, Peoples R China
关键词： desalination; VEDCMD; transmembrane mass and heat transfer
期刊名称：MEMBRANES （ 影响因子：4.562； 五年影响因子：5.015 ）
ISSN：
年卷期： 2022 年 12 卷 9 期
页码：
收录情况： SCI
摘要： Vacuum-enhanced direct contact membrane distillation (VEDCMD) has been proven experimentally to improve the permeate flux, compared with direct contact membrane distillation (DCMD). However, the theoretical mechanism for its transmembrane transfer process has not been revealed sufficiently. In this paper, with full consideration of the different driving forces of diffusion and Poiseuille flow under the vacuum enhancing condition, a theoretical transmembrane model for mass and heat transfer in VEDCMD is proposed. The CFD model and experimental platform are established to verify the theoretical model. The simulated results agree with the experimental data well, and nearly 200% improvement of the permeate flux is obtained when the permeate pressure drops to 30 kPa. The flow fields of the flow along the membrane surface are obtained and analyzed, with good consistency in the variation of the permeate flux. Since all the parameters of the proposed model are independent of the operating condition, the model is much easier for use and has better adaptability to fluctuating operating conditions.
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