Record Display for the EPA National Library Catalog

RECORD NUMBER: 137 OF 254

Main Title Nitrate removal from contaminated water supplies /
Author Guter, Gerald A.
CORP Author McFarland Mutual Water Co., CA. ;Boyle Engineering Corp., Bakersfield, CA.;Environmental Protection Agency, Cincinnati, OH. Water Engineering Research Lab.
Publisher Water Engineering Research Laboratory, Office of Research and Development, U.S. Environmental Protection Agency,
Year Published 1987
Report Number EPA-600/2-86/115 vol. I; EPA/600/2-87/034 vol. II; PB87145470
Stock Number PB87-145470
OCLC Number 16680078
Subjects Nitrates
Additional Subjects Chemical removal(Water treatment) ; Design ; Performance ; Concentration(Composition) ; Waste water ; Ion exchanging ; Tables(Data) ; Water pollution control ; Nitrates
Internet Access
Description Access URL
vol. I https://nepis.epa.gov/Exe/ZyPDF.cgi?Dockey=91024FFR.PDF
vol. II https://nepis.epa.gov/Exe/ZyPDF.cgi?Dockey=91024XRU.PDF
Holdings
Library Call Number Additional Info Location Last
Modified
Checkout
Status
ELBD ARCHIVE EPA 600-2-87-034 v.1 Received from HQ AWBERC Library/Cincinnati,OH 10/04/2023
NTIS  PB87-145470 Some EPA libraries have a fiche copy filed under the call number shown. 07/26/2022
Collation 2 volumes ; 28 cm
Abstract
The report reviews the design, construction, and operation of a 1-mgd nitrate removal plant in McFarland, CA. The plant treats well water for domestic use. Nitrates are reduced from approximately 15.8 mg NO3-N/L to well below the maximum contaminant level of 10 mg NO3-N/L. Continuous daily (24-hr.) operation of the plant was made possible by automatic operation. Automatic nitrate monitoring of product water was performed once an hour through the use of modified ion chromatography. Daily records of flows, water quality, electrical consumption, salt usage, and manhours were kept to determine operating costs. The amount of water treated by each ion exchange vessel before regeneration was 165,900 gal. (260 bed volumes). The amount of salt used per regeneration was 6.35 lb/ft3 of resin. Capital costs totaled $355,638 for a 5-ft, bed system. Operation and maintenance costs were $0.13 per thousand gal. when the system was operating at 1 mgd. Total costs, including operations and maintenance (O&M) and amortized capital, were $0.25 per 1000 gal. when operating at design capacity of 1 mgd.
Notes
"January 1987"--Vol. I. "May 1987"--Vol. II. "Cooperative agreement no. CR808902-02-0"--Vol. I. "Cooperative agreement no. CR808902-01-02"--Vol. II. "Project officer, Richard Lauch, Drinking Water Research Division, Water Engineering Research Laboratory, Cincinnati, Ohio."
Contents Notes
v. 1. Design and initial performance of a nitrate removal plant -- v. 2. Final report.