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Drinking water process design

As above mentioned, in Sect. 2.3.2, none of the wide range of drinking water treatment processes available have been designed to remove pharmaceuticals that may be present in source waters. Therefore, its worldwide presence in drinking water generates a growing concern due to the possible human exposure [52, 106, 107],... [Pg.228]

A process that was no more than a laboratory phenomenon when the Office of Saline Water was authorized in 1952 has been rapidly developed to the point where it is now one of the most economical processes for the conversion of brackish water to fresh. This process, electrodialysis, was selected for the third demonstration plant. It will be located at Webster, S. D. The Bureau of Reclamation Laboratories in Denver, Colo., prepared the specifications for this plant which will be designed to produce 250,000 gallons of fresh water per day. Operating on water containing between 1500 and 1800 parts of salt per million parts of water, this plant will remove more than 1 ton of salt daily to produce product water with less than 500 parts of salt per million parts of water which is required to meet U. S. Public Health Standards for good drinking water. Construction specifications for this plant were available August 1, and sealed bids will be opened on October 4, 1960. [Pg.8]


See other pages where Drinking water process design is mentioned: [Pg.23]    [Pg.508]    [Pg.535]    [Pg.25]    [Pg.804]    [Pg.50]    [Pg.50]    [Pg.274]    [Pg.332]    [Pg.358]    [Pg.546]    [Pg.473]    [Pg.735]    [Pg.21]    [Pg.164]    [Pg.408]    [Pg.246]    [Pg.180]    [Pg.2]    [Pg.20]    [Pg.219]    [Pg.192]    [Pg.212]    [Pg.22]    [Pg.284]    [Pg.188]    [Pg.44]    [Pg.84]    [Pg.166]    [Pg.3950]    [Pg.54]    [Pg.56]    [Pg.363]    [Pg.29]    [Pg.305]    [Pg.345]    [Pg.431]    [Pg.138]    [Pg.533]    [Pg.25]    [Pg.209]    [Pg.285]    [Pg.533]    [Pg.81]    [Pg.47]    [Pg.241]    [Pg.247]   
See also in sourсe #XX -- [ Pg.237 ]




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Drinking water

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