State Key Laboratory of Environmental Aquatic Chemistry, Research Center for Eco-Environmental Sciences, Chinese Academy of Sciences, P.O. Box 2871, Beijing 100085, People's Republic of China.
Water Sci Technol. 2010;61(12):3178-87. doi: 10.2166/wst.2010.878.
The direct contact membrane distillation (DCMD) applied for fluoride removal from brackish groundwater is presented. The self-prepared polyvinylidene fluoride membrane exhibited high rejection of inorganic salt solutes and a maximum permeate flux 35.6 kgm(-2) h(-1) was obtained. The feed concentration had no marked impact on the permeate flux and the rejection of fluoride. The precipitation of CaCO3 would clog the hollow fiber inlets and foul the membrane surface with the increase of concentration factor when natural groundwater was used directly as the feed, which resulted in a rapid decline of the module efficiency. This phenomenon was diminished by acidification of the feed. The experimental results showed that the permeate flux and the quality of obtained distillate kept stable before concentration factor reached 5.0 with the acidified groundwater as feed. The membrane module efficiency began to decline gradually when the feed continued to be concentrated, which can be mainly attributed to the formation of CaF2 deposits on the membrane surface. Finally, a 300 h continuous fluoride removal experiment on acidified groundwater was carried out with concentration factor at 4.0, the permeate flux kept stable and the permeate fluoride was not detected.
直接接触式膜蒸馏(DCMD)应用于从微咸地下水中去除氟化物。自制的聚偏氟乙烯膜对无机盐溶质具有高截留率,最大渗透通量为 35.6 kgm(-2) h(-1)。进料浓度对氟化物的渗透通量和截留率没有明显影响。当直接将天然地下水用作进料时,碳酸钙的沉淀会堵塞中空纤维入口,并随着浓缩因子的增加而污染膜表面,从而导致模块效率迅速下降。酸化进料可以减轻这种现象。实验结果表明,在浓缩因子达到 5.0 之前,用酸化地下水作为进料,渗透通量和获得的馏出物质量保持稳定。当进料继续浓缩时,膜组件效率开始逐渐下降,这主要归因于膜表面形成 CaF2 沉积物。最后,在浓缩因子为 4.0 时对酸化地下水进行了 300 h 的连续氟化物去除实验,渗透通量保持稳定,未检测到渗透氟化物。