Record Display for the EPA National Library Catalog

RECORD NUMBER: 2 OF 2

OLS Field Name OLS Field Data
Main Title Investigation of treating electroplaters cyanide waste by electrodialysis /
Author Tuwiner, Sidney B. ; Tuwiner, Sidney Bertram,
CORP Author RAI Research Corp., Long Island City, N.Y.
Publisher U.S. G.P.O.,
Year Published 1973
Report Number EPA-R2-73-287; EPA-12010-DFS; W74-06522
Stock Number PB-231 263
OCLC Number 00851674
Subjects Electroplating--Waste disposal. ; Electrodialysis. ; Factory and trade waste.
Additional Subjects Electroplating ; Cyanides ; Industrial waste treatment ; Electrodialysis ; Design ; Cost estimates ; Waste water ; Electrodeposited coatings ; Copper coatings ; Rinsing ; Performance evaluation ; Materials recovery ; Water pollution control
Internet Access
Description Access URL
http://nepis.epa.gov/Exe/ZyPDF.cgi?Dockey=9101ZHXE.pdf
Holdings
Library Call Number Additional Info Location Last
Modified
Checkout
Status
EJAD  EPA R2-73-287 Region 3 Library/Philadelphia, PA 02/16/1996
EJBD ARCHIVE EPA R2-73-287 Headquarters Library/Washington,DC 11/27/2018
ESAD  EPA R2-73-287 Region 10 Library/Seattle,WA 12/26/2018
NTIS  PB-231 263 Most EPA libraries have a fiche copy filed under the call number shown. Check with individual libraries about paper copy. NTIS 01/01/1988
Collation vii, 48 pages : illustrations ; 27 cm.
Abstract
An electrodialysis procedure is developed whereby the discharge of rinsewater is eliminated. The final rinse contains a concentration of cyanide of 1/10,000 of that of the plating. These concentrations are maintained by the use of electrodialysis to transport cyanides continuously from the second rinse solution back to the first rinse solution and also from the first rinse back to the plating bath. In this way, all cyanide is recovered and returned to the bath. Design parameters are determined, and costs are estimated. The experimental system used in this study was a prototype of a commercial size electrodialysis unit operated continuously under conditions which simulated those of the projected two-stage commercial system using a cyanide copper plating bath. (Modified author abstract)
Notes
Includes bibliographical references (pages 37-38).