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Plating Waste Treatment C. F. PAULSON Special Applications Department The Permutit Company New York, New York Treatment of electroplating rinse waters by ion exchange has been one of the most attractive methods considered in recent years for the elimination of a very serious water pollution problem. First attempts at this problem go back approximately 12 years, but until recently, all attempts have been uniformly unrewarding. Most of the difficulties were due to shortcomings in the properties of the ion exchange resins themselves. With the recent advent of a broader range of ion exchangers, these shortcomings have been virtually eliminated. The most successful of the ion exchange processes applied to electroplating waste recovery has been the use of cation and anion exchangers in the recovery of chromic acid. This was discussed at the Seventh Purdue Industrial Waste Conference by the author and several others. There are really two separate ion exchange processes. One is the use of a cation exchanger to remove metallic cations from strong chromic acid solutions such as are used for bright dipping, stripping, chromium plating, chromic acid anodizing, etc. The second is the use of an anion exchanger in series with a cation exchanger to recover the chromic acid from the rinse solutions following the above treatments. The rinse water may be reused virtually indefinitely and the chromic acid is eventually returned to the treatment bath. Since the announcement of the cation exchange process several years ago, this process has developed rapidly, and there are now more than a dozen large plants throughout the country applying either all or a part of this process successfully. In this connection, it can now be reported that it is now feasible to remove metallic cations from chromic acid solutions all the way up to the 40 percent plating tanks by cation exchange. Whether for any given installation this is economically attractive depends upon the overall layout and scale of operation. The anion exchange process has recently been extended to the treatment of mixed chromate rinse water. A process for the recovery of cyanide from cyanide plating rinse baths, very similar in operation to the chromate rinse recovery process, has been developed under one of the research projects of the American Electroplaters Society. In essence, the process consists of passing all of 215
Object Description
Purdue Identification Number | ETRIWC195324 |
Title | Plating waste treatment |
Author | Paulson, C. F. |
Date of Original | 1953 |
Conference Title | Proceedings of the eighth Industrial Waste Conference |
Conference Front Matter (copy and paste) | http://earchives.lib.purdue.edu/cdm4/document.php?CISOROOT=/engext&CISOPTR=3119&REC=9 |
Extent of Original | p. 215-221 |
Collection Title | Engineering Technical Reports Collection, Purdue University |
Repository | Purdue University Libraries |
Rights Statement | Digital object copyright Purdue University. All rights reserved. |
Language | eng |
Type (DCMI) | text |
Format | JP2 |
Date Digitized | 2008-09-22 |
Capture Device | Fujitsu fi-5650C |
Capture Details | ScandAll 21 |
Resolution | 300 ppi |
Color Depth | 8 bit |
Description
Title | page 215 |
Collection Title | Engineering Technical Reports Collection, Purdue University |
Repository | Purdue University Libraries |
Rights Statement | Digital object copyright Purdue University. All rights reserved. |
Language | eng |
Type (DCMI) | text |
Format | JP2 |
Capture Device | Fujitsu fi-5650C |
Capture Details | ScandAll 21 |
Transcript | Plating Waste Treatment C. F. PAULSON Special Applications Department The Permutit Company New York, New York Treatment of electroplating rinse waters by ion exchange has been one of the most attractive methods considered in recent years for the elimination of a very serious water pollution problem. First attempts at this problem go back approximately 12 years, but until recently, all attempts have been uniformly unrewarding. Most of the difficulties were due to shortcomings in the properties of the ion exchange resins themselves. With the recent advent of a broader range of ion exchangers, these shortcomings have been virtually eliminated. The most successful of the ion exchange processes applied to electroplating waste recovery has been the use of cation and anion exchangers in the recovery of chromic acid. This was discussed at the Seventh Purdue Industrial Waste Conference by the author and several others. There are really two separate ion exchange processes. One is the use of a cation exchanger to remove metallic cations from strong chromic acid solutions such as are used for bright dipping, stripping, chromium plating, chromic acid anodizing, etc. The second is the use of an anion exchanger in series with a cation exchanger to recover the chromic acid from the rinse solutions following the above treatments. The rinse water may be reused virtually indefinitely and the chromic acid is eventually returned to the treatment bath. Since the announcement of the cation exchange process several years ago, this process has developed rapidly, and there are now more than a dozen large plants throughout the country applying either all or a part of this process successfully. In this connection, it can now be reported that it is now feasible to remove metallic cations from chromic acid solutions all the way up to the 40 percent plating tanks by cation exchange. Whether for any given installation this is economically attractive depends upon the overall layout and scale of operation. The anion exchange process has recently been extended to the treatment of mixed chromate rinse water. A process for the recovery of cyanide from cyanide plating rinse baths, very similar in operation to the chromate rinse recovery process, has been developed under one of the research projects of the American Electroplaters Society. In essence, the process consists of passing all of 215 |
Resolution | 300 ppi |
Color Depth | 8 bit |
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