CASE STUDY # 147
1. Headline: Recovery of chromium from plating bath at
Industrial Electroplaters eliminates need for chemical
treatment.
2. Background: See below.
3. Cleaner Production Principle: internal recycling
4. Description of Cleaner Production Application: The Model
C12-X Chromic Acid Recovery Unit operates as a closed-
loop system to recover chromic acid from plating baths.
The rinsewater is filtered to remove solids and then
pumped through three reciprocating-flow ion-exchange
columns. An anion-exchange resin removes the chromate and
polychromate ions, and the water is then reused for
rinsing. The effluent passes through a second
cation-exchange bed, where a concentrated chromic acid
solution is collected. The cation and anion resins are
regenerated with sulfuric acid and sodium hydroxide,
respectively.
Material/Energy Balance and Substitution
FEEDSTOCKS: Spent electroplating bath
WASTES: Contaminated rinsewater
MEDIUM: Water
5. Economics:
CAPITAL COST: Not reported
OPERATION/MAINTENANCE: $8,055/yr for materials
DISPOSAL & FEEDSTOCK: $11,000/yr in recovered chromic
acid $5400/yr in chemical treatment eliminated, $400/yr in
sludge disposal, $6,980/yr in water consumption.
6. Advantages
FEEDSTOCK REDUCTION: 2300 kg/yr chromic acid recovered,
water consumption reduced by 2.4 million gals/yr
WASTE PRODUCTION: 2300 kg/yr chromic acid not disposed as
waste, large volumes of wastewater eliminated
IMPACT/PROBLEMS: The rinsewater used to be diluted at a
rate of 10 gallons per minute to reduce the chromium
content to 5 ppm to meet local effluent regulations.
Chromium in the plant effluent is now less than 2.0 ppm,
eliminating the need for chemical treatment. Rinsing of
the plated parts is also more efficient.
7. Constraints: No information provided.
8. Contact and Citation: "Catalogue of Successful Hazardous
Waste Reduction/Recycling Projects", Energy Pathways Inc.
and Pollution Probe Foundation, prepared for Industrial
Programs Branch, Conservation & Protection Environment
Canada, March, 1987, page .
9. Keywords: United States, USA, metal, electroplating,
recycling, ISIC 3000, chrome, acid, ion exchange, rinsing,
chromic acid.
10. Reviewer's Comments: This case study was originally
abstracted for the US EPA's Pollution Prevention
Information Clearinghouse from the Canadian publication
"Catalogue of Successful Hazardous Waste
Reduction/Recycling Projects." It underwent a UNEP IE
funded technical review in 1994 for quality and
completeness. It was edited for the ICPIC diskette in
July 1995.
( Docno unep05: 450-003-A-348 )