INTERNATIONAL CLEANER PRODUCTION INFORMATION CLEARINGHOUSE

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 )