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`r <br /> �r <br /> -y—lX-FLOW The XIGAT"" Concept and Operation Manual <br /> ` The XIGATm Philosophy <br /> Filtration <br /> The XIGAT" element is a PVC cartridge with a central permeate tube, containing membrane capillaries made from <br /> a blend of polyethersulphone and polyvinylpyrrolidone. The membrane capillaries fixated in the PVC-housing with <br /> only 2-3 cm epoxy resin, are fed to the inside with feed water. Particles bigger then the membrane poresize will be <br /> rejected from the membrane surface, keeping it within the capillaries. The liquid containing only ions and particles <br /> smaller than the membrane pore size will pass through the membrane (permeate) and will be collected in the <br /> central permeate tube. <br /> This process mode is called filtration. Filtration is enabled by a pressure difference between the feed side (in the <br /> t capillaries) and the permeate side (out of the capillaries), also called trans membrane pressure or TMP The TMP <br /> %W in a module according to the XIGATV -Concept is very low, most of the time < 0.5 bar. It is important to keep this <br /> TMP level low although it will increase during operation The maximum TMP during the filtration mode is 1 bar. A <br /> %W TMP above 1 bar will cause an irreversible fouling on the membrane surface. <br /> Depending on the feed water quality and the membrane type used, the typical flux rate during filtration is 70-100 <br /> I/mZh and the duration of this mode is 10-60 minutes. <br /> Backwash <br /> If not removed, the particles that remain within the capillaries will -in time- block the membranes, increasing the <br /> TMP. Therefore a periodical backwash is required. During the backwash the water flow will be reversed Clean <br /> permeate water will be forced from the outside of the capillaries to the inside, and will transport the foulant out of <br /> %W the capillaries. Also during the backwash mode it is important to keep monitor the TMP. The maximum TMP <br /> during backwash is 3 bar During the backwash the TMP is not the only important factor. The speed within the <br /> capillaries to transport the dirt out of the capillaries is also important. Therefore it is recommended to perform a <br /> backwash with a flux rate of 250-300 I/mZh. Furthermore it is important that the duration of the backwash is <br /> sufficient to remove all dirt, not only out of the membrane element but also out of the membrane system (pressure <br /> �' vessel). In general the actual duration of a backwash is approximately 30-40 seconds. <br /> Feed Feed <br /> %W <br /> Permeate Permeate <br /> Feed <br /> � Feed � �� <br /> L <br /> %W 'ermeate Permeate <br /> w Fcvvi • �• 6 Retentate <br /> Permeate <br /> Permeate <br /> i Filtration mode Backwash mode <br /> L Schematic view on waterflow in XIGA'm —Concept <br /> Chemically Enhanced Backwash <br /> t If a backwash is insufficient to remove all foulants, the backwash efficiency can be enhanced by adding chemicals <br /> into the backwash (Chemically Enhanced Backwash). When using disinfectants, the system can also be <br /> disinfected by the CEB The CEB mode consists of a normal backwash procedure, a backwash with chemicals <br /> (these can be dosed after the backwash pump with a dosing unit), a soaking period and a backwash to flush-out <br /> the chemicals. <br /> CAPF-XIGA-0143 <br />