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SU0005344 ENG DES PLN
Environmental Health - Public
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SU0005344 ENG DES PLN
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Last modified
10/29/2020 5:18:25 PM
Creation date
12/27/2019 8:23:37 AM
Metadata
Fields
Template:
EHD - Public
ProgramCode
2600 - Land Use Program
FileName_PostFix
ENG DES PLN
RECORD_ID
SU0005344
PE
2627
FACILITY_NAME
PA-0500531
STREET_NUMBER
4620
Direction
E
STREET_NAME
WOODBRIDGE
STREET_TYPE
RD
City
ACAMPO
APN
01709002
ENTERED_DATE
8/26/2005 12:00:00 AM
SITE_LOCATION
4620 E WOODBRIDGE RD
RECEIVED_DATE
8/26/2005 12:00:00 AM
P_LOCATION
99
P_DISTRICT
004
QC Status
Approved
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\MIGRATIONS\W\WOODBRIDGE\4620\PA-0500531_PA-0300206\SU0005344\ENG DES PLN.PDF
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7_61X-FLOW The XIGAT"° Concept and Operation Manual <br /> The XIGATm Philosophy <br /> Filtration <br /> The XIGATm 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 /> capillaries) and the permeate side (out of the capillaries), also called trans membrane pressure or TMP. The TMP <br /> in a module according to the XIGATM -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 /> 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/M2h. 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 /> 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 /> Permeate Permeate <br /> Feed <br /> Feed �— <br /> ermeate Permeate <br /> Feed dui Retentate :. ; • <br /> Permeate <br /> Permeate <br /> Filtration mode Backwash mode <br /> Schematic view on waterflow in XIGATM —Concept <br /> Chemically Enhanced Backwash <br /> 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 />
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