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Desalination of agricultural tile drainage

Author: Bryan R Sword; Robert S. Kerr Water Research Center.; United States. Environmental Protection Agency. Office of Research and Monitoring.
Publisher: Washington, DC : U.S. G.P.O., 1972.
Series: Water pollution control research series.
Edition/Format:   Print book : National government publication : EnglishView all editions and formats
Summary:
Investigations were made to determine the technical feasibility of desalination of tile drainage. Reverse osmosis (RO) and electrodialysis (ED) processes were studied. Two RO membrane stacks were investigated. The first, a high salt rejection, low product yield, was operated on variable quality (3000-7000 mg/l TDS) irrigation return water. The second RO stack and also the ED unit were operated on return waters that  Read more...
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Additional Physical Format: Online version:
Sword, Bryan R.
Desalination of agricultural tile drainage.
Washington, DC : U.S.G.P.O., 1972
(OCoLC)870260414
Material Type: Government publication, National government publication, Internet resource
Document Type: Book, Internet Resource
All Authors / Contributors: Bryan R Sword; Robert S. Kerr Water Research Center.; United States. Environmental Protection Agency. Office of Research and Monitoring.
OCLC Number: 1108479
Notes: "13030 ELY 05/12-12. REC-R2-71-12. DWR NO. 174-15."
Description: ix, 32 pages : illustrations ; 27 cm.
Series Title: Water pollution control research series.
Other Titles: Bio-engineering aspects of agricultural drainage San Joaquin Valley, California
Responsibility: by Bryan R. Sword.

Abstract:

Investigations were made to determine the technical feasibility of desalination of tile drainage. Reverse osmosis (RO) and electrodialysis (ED) processes were studied. Two RO membrane stacks were investigated. The first, a high salt rejection, low product yield, was operated on variable quality (3000-7000 mg/l TDS) irrigation return water. The second RO stack and also the ED unit were operated on return waters that were controlled to have a 3000 mg/l TDS. The second RO stack was designed for a high product rate and low salt rejection. The ED data are based on a single pass through the membrane stack. Costs are reported.

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