本文介绍了一种新型的耐污染反渗透膜，这种膜的制造工艺更加复杂 亲水性和少带电或带电与污染物相同，以减少疏水性 相互作用和电荷吸引或增加电荷排斥。耐污染 膜最近由韩国的Saehan Industries，Inc.通过涂层反渗透膜制造 与亲水性单体发生聚合和交联反应。耐污染 当两种膜同时存在时，反渗透膜的通量降低比常规反渗透膜小得多 分别使用30 ppm的奶粉、50 ppm的阳离子表面活性剂、50 ppm的非离子表面活性剂和50 ppm的 分别为ppm腐殖酸。 根据膜表面电荷（zeta电位）和表面张力对涂层膜进行了表征 疏水性（接触角）。涂层膜显示出的负电荷比普通膜少得多 普通无涂层膜，但涂层膜的接触角与 普通膜。使用各种涂层化合物控制膜表面电荷。这个 用亚甲基蓝等阳离子染料对膜表面进行染色。这个 染色强度与膜上的负电荷程度呈线性关系。这个 普通的无涂层膜由于带有最多的负电荷而被染色最多。薄膜 阳离子表面活性剂的污垢也与表面的负电荷程度呈线性相关 膜。非离子表面活性剂和腐殖酸对膜的污染有一定的关系 污染物和膜之间的疏水相互作用。膜污染 干牛奶似乎受到疏水效应、电荷效应和一些胶体效应的混合影响 存款。 在使用8040元件的现场试验中，耐污染膜保持了更高的渗透性 与常规膜相比，现代汽车（Hyundai Motor Co.）将两种膜都与工业废水混合，以供使用 大约40天。抗污染反渗透膜已在三星电子有限公司成功用于废水处理。 大约五个月。包括5个参考文献、表格、图表。

This paper deals with new fouling resistant RO membranes which are made more hydrophilic and less charged or charged with the same charge as the foulants to reduce hydrophobic interaction and charge attraction or to increase charge repulsion, respectively. The fouling resistant membranes were recently manufactured by Saehan Industries, Inc. in Korea via coating RO membranes with hydrophilic monomers followed by polymerization and cross-linking reaction. The fouling resistant RO membranes showed much less flux reduction than the regular RO membrane when both membranes were subjected to 30 ppm dry milk, 50 ppm a cationic surfactant, 50 ppm a nonionic surfactant and 50 ppm humic acid, respectively. The coated membranes were characterized in terms of membrane surface charge (zeta potential) and hydrophobicity (contact angle). The coated membranes showed much less negative charge than the regular uncoated membrane, but the contact angle of the coated membrane was about the same as the regular membrane. The membrane surface charge was controlled using various coating compounds. The membranes with various surface charges were dyed with a cationic dye such as methylene blue. The intensity of dyeing was linearly correlated with the degree of the negative charge on the membranes. The regular uncoated membrane was dyed the most since it has the most negative charge. The membrane fouling by the cationic surfactant was also linearly correlated with the degree of the negative charge on the membranes. The membrane fouling by the nonionic surfactant and humic acid had some relation with hydrophobic interaction between the foulants and the membranes. The membrane fouling by the dry milk appeared to be influenced by a mixture of hydrophobic effect, charge effect and some colloidal deposits. In a field test using 8040 elements, the fouling resistant membrane maintained much higher permeability than the regular membrane when both are fed with an industry wastewater at Hyundai Motor Co. for about 40 days. The fouling resistant RO membrane has been successfully in operation for treating wastewater at Samsung Electronics Co. for about five months. Includes 5 references, tables, figures.