INTERNATIONAL CLEANER PRODUCTION INFORMATION CLEARINGHOUSE

CASE STUDY # 199

1. Headline: 1,1,1-Trichloroethane is eliminated from the

Production Process by Aqueous-based Cleaning at A

Fastening Parts Manufacturing Facility.

2. Background: See below.

3. Cleaner Production Principle: Process modification.

4. Description of Cleaner Production Application: The clean

technology involved initially reducing

1,1,1-trichloroethane use and finally eliminating its use

by installing aqueous cleaning systems.

Case Study Summary

Process and Waste Information: This facility manufactures

nails, staples, and the tools to drive these fasteners.

The fastening tools are made of aluminum, magnesium and

carbon steel. To produce these fastening parts, grinding,

milling, drilling, lathe working, heat treatment and metal

finishing operations are employed. Prior to many of these

operations, parts are cleaned in a cold application using

1,1,1-trichloroethane (TCA). TCA was being discharged in

the wastewater at levels twice as high as the allowable

limit. Absorbents used around the machine tools also

showed levels of TCA that prevented disposal in the

regular trash. The company decided to attempt to

eliminate the use of TCA from the manufacturing of

fastening tools.

A task force identified for potential causes for excessive

TCA cleaning wastes: too much availability of cleaners,

unnecessary dumping of TCA, lack of operator awareness,

and unnecessary parts cleaning. Initially, the firm

reduced the number of cleaning stations from 37 to 27.

Costs associated with dumping of cleaners were make the

responsibility of each department. Operators were

surveyed to identify TCA use and determine opinions for

alternatives.

The selected pollution prevention measure was to use a

heated tank with liquid agitation, provided the necessary

chip removal and oil removal systems were present. In the

machine maintenance areas, two mineral spirit cleaners

were installed and the company is in the process of

installing aqueous-based cleaning systems. At the time of

this case study, they had installed 13 aqueous washing

systems and two (2) mineral spirits cleaning systems.

They expect to have a total of 15 aqueous systems, which

are centralized within departments which will replace 37

former TCA locations.

Other processes implemented in addition to the processes

for reducing TCA included treating soapy water by oil

separation, and in-house pH neutralization. Also, a

precision grinder was replaced by an older piece of

grinding equipment which does not require virgin material.

A "procedure" (not further described) was also recommended

that would prevent the spoilage of coolants.

Scale of Operation: Approximately 6500 gallons per year of

TCA were used. No other measure of the scale of

operations was provided.

Stage of Development: The clean technology is in the

implementation stages - all equipment is not yet fully

installed.

Level of Commercialization: The technology is fully

commercialized

Material/Energy Balances and Substitutions:

Quantity Quantity

Material Category Before After

Waste Generation:

1,1,1-trichloroethane 400 ppb in waste- not

water discharge detectable

Feedstock Use:

1,1,1-trichloroethane 6500 gallons 0

Water Use: N/A N/A

Energy Use: N/A N/A

5. Economics

Investment Costs: The anticipated capital expenditures

during 1990-1991 on this project are $80,000. This

includes costs for aqueous cleaning systems, waste water

collection equipment, and equipment installation.

Operational & Maintenance Costs: $15,000 in utility costs

are required for heating and pumping aqueous fluids.

Payback Time: With an approximate annual savings of

$56,500 and $80,000 in capital costs, the pay back period

is approximately 1.4 years.

6. Advantages

A net savings of $7,000 is expected from reduced disposal

costs, since the disposal costs in 1988 were $9,000 and

they expect that the cost for disposal of separated oils

will be $2,000. In addition, the annual cost saving

associated with the disposal of absorbents no longer

contaminated with TCA is $34,000.

A net savings from replacing virgin TCA and aqueous

cleaners will be $7,000. This was calculated from the

difference in the 1988 cost of virgin TCA ($27,000) and

the 1991 costs for aqueous cleaning solution ($20,000).

Other processes implemented, in addition to the processes

for reducing TCA, included treating soapy water by oil

separation and in-house pH neutralization. The annual

savings from segregation and in-house treatment are

$20,000. The savings from changing to an older grinder

lead to an annual savings of $1,200 from reuse of the

coolant. The annual savings from preventing spoilage of

coolants are $1,300.

Overall, the potential savings from eliminating TCA is

approximately $56,500 per year (including the extra

utility costs presented below in 8.0).

There are also regulatory advantages that cannot be

directly quantified. Permit concerns associated with TCA

discharge were greatly diminished by successfully

negotiating with the regulatory agencies to tie the metal

finish discharge into the nearby town sewer system. The

company will no longer have to report under SARA for TCA

which will save considerable time. Eliminating TCA will

also allow the company to present a strong example to the

State and local communities that they are doing their part

to decrease overall emissions, thus increasing community

relations. Finally TCA air discharges will be eliminated.

This may be especially important since TCA has come under

intense scrutiny and regulation because of its ozone

depletion and air toxics potential.

7. Constraints

There is an extra electrical cost associated with heating

and pumping aqueous cleaning fluids equal to $15,000 per

year. TCA cold cleaning had no utility cost.

8. Contacts and Citation

Type of Source Material: EPA Conference Proceedings

Citation:

American Electroplaters and Surface Finishers Society,

Inc., and the Environmental Protection Agency; "12th

AESF/EPA Conference on Environmental Control for the

Surface Finishing Industry"; January, 1991; pp. 165-181.

Level of Detail of the Source Material: Additional

information is provided on the identification of the

problem and task force that decided on the solutions.

Industry/Program Contact and Address:

Kevin P. Vidmar, Div. Manager, Environmental Affairs,

Stanley Fastening Systems, Route 2, East Greenwich, RI

02818, United States.

9. Keywords: United States, USA, metal, plating, process

modification, trichloroethane, TCA, tank, coolant,

electroplating, ISIC 3400, ISIC 3471, water saving.

10. Reviewer's Comments: This case study was originally

abstracted form the document cited above for the US EPA's

Pollution Prevention Information Clearinghouse. In 1994

it underwent a UNEP IE funded review for quality and

completeness. It was edited for the ICPIC diskette in

August 1995.

DOCNO: UNEP 14 Document No.: 222-003-001C