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WRRCSR No.12:28:84 Brackish Groundwater Desalting Tests Using Low Pressure Reverse Osmosis Membranes, Wai'anae, O'ahu, Hawai'i

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Title: WRRCSR No.12:28:84 Brackish Groundwater Desalting Tests Using Low Pressure Reverse Osmosis Membranes, Wai'anae, O'ahu, Hawai'i
Authors: Gee, Henry K.
Lau, L. Stephen
LC Subject Headings: Brackish waters.
Groundwater -- Hawaii -- Oahu.
Saline water conversion -- Reverse osmosis process.
Waianae (Hawaii)
Issue Date: Dec 1984
Publisher: Water Resources Research Center, University of Hawaii at Manoa
Citation: Gee HK, Lau LS. 1984. Brackish groundwater desalting tests using low pressure reverse osmosis membranes, Wai'anae, O'ahu, Hawai'i. Honolulu (HI): Water Resources Research Center, University of Hawaii at Manoa. WRRC special report, 12:28:84.
Series/Report no.: WRRC Special Reports
12:28:84
Abstract: A desalting test using low pressure, reverse osmosis (RO) FT-30 and FT-50 membranes was conducted on Pump 10 well water at Oahu Sugar Company near Campbell Industrial Park on O'ahu. The brackish test water from the
Waianae basalt aquifer had a chloride (Cl-) concentration of 450 mg/l and a total dissolved solids (TDS) concentration of 1250 mg/l. The applied pressure ranged from 40 to 75 psi with a daily incrementof 5 psi. The
test operation duration was 239 hr. The FT-30 membrane demonstrated high rejection of Cl-, TDS, and silica (>90%), thus producing an excellent potable water. The permeate water production was slow, averaging 10.3 gpd or 4.6% of the feedwater. The production rate increased with pressure.
The fouling rate was slow and longer runs could be made before cleaning became necessary. The FT-50 membrane yielded high permeate production (approximately four times that of FT-30), but was of poor (sub-potable) water quality with average rejection of Cl- at 17% and TDS at 25%. The
fouling rate of the membrane was high, seriously reducing the permeate production in a short time. Cleaning with dilute phosphoric acid followed by Wisk and NaOH solution restored about 45% of the production rate. A large-scale RO module (element) should be tested for a longer period of time to determine sustainable performance of fouling rate. After reaching
15% reduction in the permeate production rate, various cleaning agents should be tested to restore the rate and to determine the type of fouling. By using a full-size commercial element, uncertainties of scale-up from small laboratory units can be eliminated. A longer operating period using
the available pump pressure would yield more meaningful design data than the short, 2-wk test period using laboratory-size elements.
Sponsor: Water Resources Research Center, University of Hawaii at Manoa
Pages/Duration: iv + 21 pages
URI/DOI: http://hdl.handle.net/10125/8736
Appears in Collections:WRRC Special Reports



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