在四种不同的地表水处理综合膜系统（IMS）方案中，对生产力和污染控制进行了研究，包括:方案1——池滤、曝气、双介质过滤、曝气、快速砂滤和纳滤；方案2——混凝、沉淀、快速砂滤、输送、慢速砂滤和反渗透；方案3——混凝、沉淀、快速砂滤、输送、臭氧氧化、生物活性炭过滤、慢速砂滤和反渗透；方案4——储存、微染色、混凝、沉淀、上流过滤、超滤和反渗透。 在所有四个经过测试的IMS方案中，MTC在9到14个月的运行时间内都出现了下降。一年一次到十二次的清洁频率是可以接受的。方案4在运行9个月后出现硫酸钡结垢。目前的清洁程序不成功。因此，防垢剂将在下一次测试中使用。在方案1和4中观察到进料浓缩液压降偶尔增加。纳滤和反渗透元件的清洗非常费力。因此，应避免进料浓缩液压降增加。 在18个月的时间内，使用预处理地表水的超滤装置的生产率可维持在85 l/m2h左右。包括7个参考文献、表格、图表。

Productivity and fouling control were investigated in four different Integrated Membrane System (IMS) schemes for surface water treatment that that included: scheme 1 - bankfiltration, aeration, dual media filtration, aeration, rapid sand filtration and nanofiltration; scheme 2 - coagulation, sedimentation, rapid sand filtration, transport, slow sand filtration and reverse osmosis; scheme 3 - coagulation, sedimentation, rapid sand filtration, transport, ozonation, biological activated carbon filtration, slow sand filtration and reverse osmosis; and, scheme 4 - storage, microstraining, coagulation, sedimentation, upflow filtration, ultrafiltration and reverse osmosis. In all four tested IMS schemes, MTC-decline was observed in operation times ranging from 9 to 14 months. Applied cleaning frequencies ranging from one to twelve times a year were quite acceptable. Bariumsulfate scaling occurred in scheme 4 after 9 months of operation. Current cleaning procedures were not successful. As a consequence antiscalant will be applied in the next test runs. Occasional increases in feed-concentrate pressure drop were observed in schemes 1 and 4. Cleanings of the nanofiltration and reverse osmosis elements were laborious. Consequently increases in feed-concentrate pressure drop should be avoided. Productivity of the ultrafiltration unit fed with pretreated surface water could be maintained at about 85 l/m2h, during a period of 18 months. Includes 7 references, tables, figures.