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SANDIA REPORT SAND95-2655 UC-920 Unlimited Release Printed May 1996 * 4 Evaluation of Aqueous Cleaners as Alternatives to Vapor Degreasing Ronald A. Guidotti, Thomas W. Schneider, Gregory C. Frye, Stephen J. Martin, George Moore Prepared by Sandia National Laboratories Albuquerque, New Mexico 87185 and Livermore, California 94550 for the United States Department of Energy under Contract DE-AC04-94AL85000 Approved for public release; distribuaon fs unlimited. . ~ I ' DISTRIBUTION OF THIS DOCUMENT tS UNUMtTm ~WST a-

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Page 1: 4 of Alternatives to Vapor Degreasing/67531/metadc663888/m2/1/high_re… · Evaluation of Aqueous Cleaners as Alternatives to Vapor Degreasing Introduction As part of the preparation

SANDIA REPORT SAND95-2655 UC-920 Unlimited Release Printed May 1996 *

4

Evaluation of Aqueous Cleaners as Alternatives to Vapor Degreasing

Ronald A. Guidotti, Thomas W. Schneider, Gregory C. Frye, Stephen J. Martin, George Moore

Prepared by Sandia National Laboratories Albuquerque, New Mexico 87185 and Livermore, California 94550 for the United States Department of Energy under Contract DE-AC04-94AL85000

Approved for public release; distribuaon fs unlimited.

. ~

I '

DISTRIBUTION OF THIS DOCUMENT tS UNUMtTm ~ W S T a-

Page 2: 4 of Alternatives to Vapor Degreasing/67531/metadc663888/m2/1/high_re… · Evaluation of Aqueous Cleaners as Alternatives to Vapor Degreasing Introduction As part of the preparation

Issued by Sandia National Laboratories, operated for the United States Department of Energy by Sandia Corporation. NOTICE. This report was prepared as an account of work sponsored by an agency of the United States Government. Neither the United States Govern- ment nor any agency thereof, nor any of their employees, nor any of their contractors, subcontractors, or their employees, makes any warranty, express or implied, or assumes any legal liability or responsibility for the accuracy, completeness, or usefulness of any information, apparatus, prod- uct, or process disclosed, or represents that its use would not infringe pri- vately owned rights. Reference herein to any specific commercial product, process, or service by trade name, trademark, manufacturer, or otherwise, does not necessarily constitute or imply its endorsement, recommendation, or favoring by the United States Government, any agency thereof or any of their contractors or subcontractors. "he views and opinions expressed herein do not necessarily state or reflect those of the United States Govern- ment, any agency thereof or any of their contractors.

Printed in the United States of America. "his report has been reproduced directly from the best available copy.

Available to DOE and DOE contractors from Office of Scientific and Technical Information PO Box 62 Oak Ridge, TN 37831

Prices available from (615) 576-8401, FTS 626-8401

Available to the public from National Technical Information Service US Department of Commerce 5285 Port Royal Rd Springfield, VA22161

NTIS price codes Printed copy: A03 Microfiche copy: A01

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SAND952655 Unlimited Release Printed May 1996

Distriiution Category UC-920

Evaluation of Aqueous Cleaners as Alternatives to Vapor Degreasing

Ronald A. Guidotti Battery Research Dept.

Thomas W. Schneider, Gregory C. Frye, and Stephen J. Martin Microsensor Research and Development Dept.

Sandia National Laboratories Albuquerque, NM 87185-0614

George Moore. Martin-Marietta Specialty Components, Inc.

Largo, FL 34649-2908

Abstract

As part of the preparation process during assembly of thermally activated batteries, the stainless steel piece parts are nofmauy cleaned by vapor degreasing with trichloroethylene. Severe restrictions on the use of chlorinated and fluorinated hydrocarbons in recent years prompted the evaluation of a number of aqueous cleaners as a replacement technology for this application. A total of seven commercial aqueous degreasers was evaluated in this study at several dilution ratios and temperatures. One organic cleaner was also examined under ambient conditions. The effectiveness of the cleaner was determined by the use of x-ray photoelectron spectroscopy WS), which is a &ce analytical technique that is very sensitive to low levels of s d c e contaminants. A quartz-crystal microbalance (QCM) that is immersed in the cleaning bath was evaluated as a tool for monitoring the bath cleanliness. The best overall cleaning results were obtained with Micro, Impro-Clean 3800, and Sonicor cleaners.

(This paper was presented at the 20th Annual Electronics Manujactm'ng Conference held on February 21-23, I996, at China Lakz, CA.)

*Currently with Sandia National Laboratories, Neutron Generator Dept.

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Acknowledgments

The authors wish to acknowledge the assistance of Carol Phefps, Patrick Benavidez, and Art Andaiola in cleaning of the samples, and Jim Spates for development of the QCM hardware and conrpmtor circuitry.

This work was performed for the U.S. DOE under contract number DE-ACO4-94AL8500 and was partid& fbded by the DOE Office of Technology Development.

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Contents

Introductio n... ................................................................................................................ 5

Experimental P r o ~ u r e s ................................................................................................ 7 Cleaners .............................................................................................................. 7 Cleaning Procedure/ ............................................................................................ 7 X P S Analysis ....................................................................................................... 8 Quartz Crystal Microbalance ................................................................................ 8

Immersible QCM Test Fixture .................................................................. 9

Results and Discussion. ................................................................................................... 9 XPS Examination, ............................................................................................... 9

Preliminary E.... .......................................................................... 9 Follow-up Cmdet Tests ........................................................................ 10 Alternate Cleaner Slwey ....................................................................... 13

Theory ................................................................................................... 16 Results of Cleaning Tests ....................................................................... 17

Bath Temperature of23"C .......................................................... 17 Bath Temperature of 50°C .......................................................... 19

Simplified QCM Instnunentatio a ........................................................... 24

. . QCM Evaluation. .............................................................................................. 16

Future Work ...................................................................................................... 25

Conclusions ................................................................................................................... 25

R e ~ r e n ~ s ..................................................................................................................... 26

Figures 1 2 3

Photo of Assembled Immersible QCM Test Fixture .............................................. 8 Exploded View ofhmersible QCM Test F ~ e ................................................. 9 XPS Spectnun for Untreated, Stainless Steel Disc Coated with an Oil

4

5

6

7

. F h ................................................................................................................... 11 X P S Spectrum fbr Oil-Contaminated Stainless Steel Disc After Cleanhg by

XPS Spectrum fbr Oil-Contaminated Stainless Steel Disc After Cleaning

Cleaning Experiment at 23°C with DI Water

Vapor Degreasbg with TCE ............................................................................... 12

with 100% Citridet at Room Temperature .......................................................... 12

a) Oscillator Frequency Response ...................................................................... 18 b) Damping Voltage Response .......................................................................... 18

a) OscilIator Frequency Response ...................................................................... 20 Cleaning E x p e w at 23°C with 10% Micro

.... ....... __ ...

3

... ...

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b) Damping Voltage Respo nse.....................................,,...,............,.................. 20 Cleaning Experiment at 50°C with DI Water a) Oscillator Frequency Re sponse........................... .............................................

Cleaning Experiment at 50°C with 10% Micro a) Oscillator Frequency Respo ......................................................................... 22 b) Damping Voltage Respo nse........................................................................... 22 Damping Voltage Response of Oscillator at 23°C for 2%, lo%, and 20%

8

b) Damping Voltage Response ........................................................................... 21 9

10 Micro ................................................................................................................. 23

Tables 1 2

3

4

5

6

Cleaners Examined in Cleaning Study .................................................................. .7 Results of PreMnary Cleaning Experiments with Stainless Steel Discs Coated with Vacuum-Pump Oil and Cleaned with Citridet Solutio EL.................. 10 Results of Additional Cleaning Experiments with Citridet and d-Lhnene at 25°C ............................................................................................................... 13 Summary of XPS Data for Stainless Steel Discs Contaminated with

Optimum Cleaning Conditions for Various Cleaners Evaluated in This Study m Order of Decreasing Effectiveness Based on XPS Analyses ................... 15 S v of Results of Cleaning Tests with QCM in DI Water and Micro

Vacuum-- Oil and Cleaned with Various Cleaners ....................................... 14

S o ~ o ............................................................................................................... 24

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Evaluation of Aqueous Cleaners as Alternatives to Vapor Degreasing

Introduction

As part of the preparation process during assembly of thermally activated batteries, a number of stainless steel piece parts require thorough cleaning to remove films of oil, grease, and wax These metal parts include the battery case, current collectors, blank end plates, arrd headers which are metal plates containing glass-to-metal &edthroughs. In the past, these were n o d y cleaned by vapor degreasjng with trichloroethylene, since this provided excellent results. However, severe restrictions as a result of the Montreal Protocol have been imposed on the use of chlorinated and fluorinated hydrocarbons io recent years. These materials bave been linked with destruction of the protective omne layer in the upper atmosphere. The Department of Energy WOE) has mandated that these halogenated organic cleaners can no longer be used at any of the fkcilities within the nuclear-weapon compleq which includes Sandia National Laboratories and, until last year, Martin-Marietta Specialty Components, Inc. (Largo, FL).

A number of alternatives were considered. One p o s s i b i i involved the use of non- halogenated organic solvents. This option would be difficult to implement because of costs and c o ~ m involving environmental &ty and health @S&H) issues at Sandia and the DOE. The flammability and toxicity of such solvents would make themunacceptable.

A second alternative considered was supercritical extraction with CO,. This was deemed too costly and time-consuming for a production environment. In addition, the high pressures and large tanks required were ES&H concerns.

A third option was the use of aqueous cleaners. On 5rst examination, there did not appear to be any serious ES&H issues with this technology. It is relatively easy to use and the cost should be reasonable. There are a i%ir number of commercial aqueous cleaners on the market, with a wide variety of active ingredients. Some of the aqueous cleaners are terpene based, while others contain various proprietary alcohols, activators, and surfactants. Inhiiors are usually added to prevent corrosion of metal parts during cleaning. (Compatibility of the cleaner with the parts to be cleaned can be an important issue for some materials.) Many have little or no volatile organic compounds (VOCs), which increases sa&y by mhimihg flammability and personnel-exposure concerns. Many are biodegradable, which facilitates waste disposal. Consequently, they are considered environmentally benign.

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We decided to pursue the last option, as it appeared to be the most viable one fbr implementation at Sandia and for the DOE m the long run to address cleanhg needs, based on preliminary work at Sand& Martin-Wet@ and Allied Signal Kansas Cityy MO. A total of seven commercial aqueous degreasers was evaluated m our study. A commercial organic solvent was added later m the studyy fix comparative purposes, iblly realizing that it was unlikely to be used.

To be practical, it was envisioned that parts would be cleaned in a batch mode, rather than using a once-though technique. Since the contamman ts would continue to accrue with repeated use, some means of monitoring the bath would be necessary. The bath could be monitored either directly fbr the contamman ts or indirectly for the concentration of the active cleaning ingredients. This information would be necessary for deciding when to replace the bath. Ideally, it was desirable to be able to monitor the bath in real time, to gauge the rate of cleaning.

One analytical technique that was considered for solution monitoring was Fourier transfbrm infhred spectroscopy (FTIR). There are a number of difliculties associated with such a technique fbr aqueous cleaners. First, the bath is composed of many ingredients that would be active in the lR region. The nature of the organic contamhint that is to be removed is not always known and can varyy depending on the sample history; ie., the component for which an IR signature could be tracked during cleaning was undefined. What is more important, the small of amount of organic contaminant would be lost in the noise of the large IR signal that would be generated by the active organic ingredients m the aqueous cleaners. Similw problems would result with related spectroscopic techniques.

What was desired was a measurement technique that was not con tamhint specific. A p o s s i b i i that showed very good promise was the quartz-crystal microbalance (QCM). Earlier work at Sandia bad shown that this technique to be a viable option. The use of an immersed QCM was explored as a potential monitoring device in this study.

The efktiveness of the cleaner was determined by x-ray photoelectron spectroscopy (XPS), which is an analytical technique that is very sensitive to low levels of &w contamiuants. For our applications, the maifl element of interest was carbon The atomic ratio of FelC or the atomic concentration of carbon on the surface provided by XE'S were used as metrics for quantifjing the level of cleanliness.

This paper presents the results of the evaluation of select commercial aqwous cleaners as well as the initial results of the use of the QCM for monitoring bath cleanliness.

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Experimental Procedures

Cleaners

The cleaners that were evaluated in the study are listed in Table 1.

TABLE 1. Cleaners h m i n e d in Cleaning Study.

Cleaner me Company

MiCrO

Inpro-Clean 3800 Citridet RB Degreaser Sonicor Uniclean VII d-limonene D-Oree~ 500

Aqueous

Aqueous Aqueous Aqueous Aqueous Pure

Aqueous

organic

International Products Corp., Burlington, NJ Oakite Products, Inc., Berkeley Heights, NJ Oakite Products, Inc., Berkeley Heights, NJ Em, Inc., Sdord, FL Sonicor Imtmments Corp., Copiague, NY Uniclean Products, Inc. Florida Chemical Co., Inc., Lake M e d , FL Solvent Kleene, Peabody, MA

Cleaning Procedure

The test coupons were 304L stainless steel discs, 3.18 cm (1.25”) in diameter by 0.0254 cm (0.010”) thick These were dipped into vacuum pump oil (Sargent Welch DuoSeal) and the excess allowed to drain away onto a paper toweL This resulted in a thin ijhn of oil remaining afterwards. The test coupons were then cleaned under the various test conditions.

The cleaners were evaluated at ambient temperature (-25°C) and under hot conditions (55”-60°C) at dilutions of 1:5 and 1:lO by volume, as well as at fidl strength. Typically, the cleaning process involved ultrasonic agitation for 10-15 min at room temperature or 60°C in the cleaning sohxtion, followed by a dip rinse with clean, hot (5O0-6OoC) deionized @I) water. The dip rinse was M h e d with a rinse of hot DI water &om a squeeze bottle. The excess water was allowed to drain onto a clean absorbent towel and the parts were then dried in an oven at 100°C. Not all the cleaners were exposed to the fidl range of test conditions, however, due to time constraints. For comparison, a number of oil- contaminated stainless steel discs were cleaned by normal vapor degreasing with trichloroethylene (TCE) or by cleaning in Jiquid (boiling) trichloroethane.

7 I

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In the case of the single organic solvent that was evaluated, the solvent was agitated by blowing a stream of air through it while the part to be cleaned was suspended m it. After removal &om the solvent, the part was blown dry with a stream of clean dry &r or nitrogen, as recommended by the manuilicturer.

I

XPS Analysis

The XPS spectra were taken with a Model 5400LS x-ray photoelectron spectroscope (Physical Electronics), using a monochromatic Al x-ray source and position-sensitive detector.

Quartz Crystal Microbalance

The 1” AT-cut QCM used m this study had a nominal fundamental ljrequency of 5 MHZ and was purchased from Maxteck (Torrance, CA). The electrodes were fabricated by first vapor depositing 15-mn-thick chrornium film to act as an adhesion layer ibr a 160-m- thick gold film. The electrode which served as the ground of the QCM was modified to sitnulate a stainless steel surfixe by coating the gold with an addition 15-m-thick chromium film. Thh was to provide a more-valid basis for comparison of the cleaning efficacy of the various system with the stainless-steel piece parts. The electrode d c e exposed to the liquid cleaner was 0.66 cm m diameter (0.34 cm‘). The electrode surhce on the reverse side of the crystal was 1.29 cm m diameter. The output signal from an oscillator running at 5 MHz was connected across the quartz crystal to maintain it at its resonance frequency.

rr

Figure 1. Photo of Assembled Immersible QCM Test Fixture.

Immersible QCM Test Fixture A photo of the immersible fkture that incorporates the QCM is shown in Figure 1. The fixture is shown s c h e e y in an exploded view m Figure 2. (Details regarding the construction can be found in reference 1.) These electrodes were connected to an oscillator circuit board that was an integral part of the 6xture. The oscillator board was built in house and was designed to allow the use of the QCM in liquids with viscosities of up to 200 cP; excessive signal dampening occurs with viscosities higher than this. Power and sensing leads to the sensor were contained in a stainless steel tube attached to the sensor housing.

The response of the QCM was obtained from two

8

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1

d. Conductor O-Rlng

B. Sulnlrrs Stool Cover

b. Toflon Washer

c.QCM

-

1. L o u n lnaulator

h. Oscillator Board

0 1.0-Ring

J. Stainless S-1 Plug

Figure 2. Exploded View of Immersible QCM Test Fixture.

output signals *om the oscillator board. One signal provided the peak resonance ii-equency, indicating any shift m the natural resonance fiequency of 5 MHz as a result of addition or removal of contarmnant films. A vohge signal was also obtained which was directly proportionaI to the magdude of the damped resonance signal. The resonant fiequency was measured with an HP5384A fkquency counter and the voltage was measured with an HP3478A digital muhheter. Together, these responses provide good metrics on theQCMperfbrmance.

Results and Discussion

XPS Examination

Preliminary Experiments In earlier preliminary work, a citnrs-based solvent containing pure d-limonene (a terpene) was evaluated as a replacement for Freon@l13 for cleaning soldering flux fiom printed- circuit boards?. The results showed that d-limonene was more e&cthe than Freon@ll3 as a solvent at room temperature.

Based on these encouraging results, M e r work was undertaken to evaluate aqueous solutions of Citridet, which contains d-limonene as the active cleaning ingredient. Ceramic parts and stainless steel bolts were first contaminated with vacuurn-pump oil (Sanovac), parafEn wax, and silicone oil (Dow-Corning 705). The contaminated parts were then cleaned in 50% and 100% Citridet solutions at room temperature and at 60°C, as before. For control purposes, similar samples were also cleaned in boiling trichloroethane.

The samples were examined by XPS for &ce cleanliness. Tests results are shown in Table 2 for the atomic concentration of carbon on the surf&. (The lower the carbon value, the cleaner the d e . ) The values for trichloroethane were taken as reference

9

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poiuts. The relative efEctiveness of the aqueous cleaning solutions varied depending on the contaminant involved. "he pump oil was the most difficult material to remove, followed by the silicone oil.

The 50% Citridet solution showed *roved cleaning at the higher temperature for all contarmnants . The temperatwe effect was not as pronounced for the 100% Citridet, however. For the par&h, both Citridet solutions were better or equal to tricbloroethane m cleaning efficiency at 60°C. For the punrf, 05 the best results were obtained using 100% Citridet hot. For the silicone oil, better r e d s were obtained with 100% Citridet.

Tabler 2. Results of Preliminary Cleaning Experiments with Stainless Steel Discs Coated with Vacuum-Pump Oil and Cleaned with Citridet Solutions.

Treatment Surface Carbon Concentration, Atomic Percent

ParafEin Pump Oil Silicone Oil

None (contaminated) Trichloroethane, boiling

100% Citridet, 25°C 100% Citridet, 60°C

50% Citridet, 25°C 50% Citridet, 6OoC

52.2 29.0

22.3 27.0

30.8 26.2

70.3 48.1

50.3 45.3

56.3 51.2

73.6 49.4

42.7 43.0

53.3 44.8

By proper selection of parameters, the parts could be more eExtiveIy cleaned with the aqueous cleaner than with trichloroethaue.

Follow-up Citridet Tests The very promisji results &om the initial cleaning tests with C i d e t (Table 2) made this material-ur mat& based on d-limonene-very attractive candidates for replacement of the TCE vapor-degreasing process that we were currently using. In addition, the ES&H issues were minimal with these materials. This encouraged us to do fbrther tests but with the actual stainless steel discs (current collectors) used in thermal batteries. These were coated with a film of vacuum-pv oil (see Cleaning Procedures) and cleaned in a similar manner as those in the initial tests with 100% Citridet and d-limonene, but at room temperature. (It was desirable to avoid heating the samples, ifpossible, to reduce the overall cleaning time.) As befire, X P S was used to check for &ce cleanliness. In this series of experiments, samples that had been vapor degreased with TCE were also included as controls.

10

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A typical XPS spectrum is shown m Figure 3 for a stainless steel disc after contamination with vacuum-pump oil. The comsponding spect~um fbr the sample after vapor degreasing with TCE is shown in Figure 4 and that d e r cleaning with Citridet is shown in Figure 5. (The XPS spectnun for the sample cleaned with d-limonene was very similar to that cleaned in Citridet.) The carbon contamination was readily fbllowed by monitoring the intensity of the Cls peak, located at an energy of -290 eV. This peak was considerably reduced after the sample was vapor degreased (Figure 4) and when it was cleaned with the Citridet (Figure 5). The Fe 2p3 peak was used to monitor the Fe concentration. I

10

9

8

7

6

, * <cis '

I

-- -- -- --

I -

le00

4 5

3

2

1

0 7 : : : Y

-- -- --

800 300 188 0

Figure 3. X P S Spectrum for Untreated, Stainless Steel Disc Coated with an Oii Film.

The measured smfhe-carbon concentrations are swnmarized m Table 3 for the various samples before and after cleaning. Pure d-limonene was not as efktive as vapor degreasing with TCE. The sample with the lowest carbon level (ie., the cleanest) was the one cleaned with the Citridet solution, which contains d-limonene along with swf8ctants.

Because the efEctiveness of Citridet had been demonstrated, we began using it at full strength for our cleaning needs, as we were no longer able to use vapor degreasing with TCE. While no obvious problems were encountered der ushg the bath fbr six months or more, there was an increasing concern with the projected Hetime for the bath. The bath tended to darken with use, which was indicative of some chemical breakdown occurring with thwthe most likely being oxidation ofthe d-limonene component. Lacking any

11

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10

9

8

7

6

5

4 +

3

2

I

0 7

--

-- -- --

1OOO 300 860

4

L 0

5

4 +

3

2

I

0 7

--

-- -- --

1OOO 300 860 780 a0 500 400 380 200 190 e BDOIHCENERGY. eV

4

L 0

780 a0 500 400 380 200 190 e BDOIHCENERGY. eV

Figure 4. XPS Spectrum for Oil-Contaminated Stainless Steel Disc After Cleaning by Vapor Degreasing with TCE,

le

9

8

7

6 e 8 5 h

I

4

3

L L

VI

4 VI B T

VI 2

1

-- --

e T :

Figure 5. XPS Spectnun for Oil-Contaminated Stainless Steel Disc M e r Cleaning with 100% Citridet at Room Temperature.

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Table 3. Results of Additional Cleaning Experiments with Citridet and d-limonene at 25OC.

Treatment Surface Carbon Concentration, Atomic Percent

None (contaminated) Trichloroethylene 100% Citridet d-limonene

100" 45.5 33.8 49.8

Data are nonnalized to 100% C for the oil-contaminated sample

suitable monitoring technique at the time, we were fbrced to consider replacing the bath at someperiodichterval, which could become costly. (The monitorbg issue will be discussed in detail in the following section on the QCM.). This, coupled with the l%ct that some of the bath operators found the strong citrus smell objectionable, encouraged us to consider alternate aqueous cleaners.

Alternate Cleaner Survey In surveying the market, we became aware of other aqueous cleaners that could be suitable for our purposes. These could be diluted by up to 1O:l in some cases, which would make their use economical if we were forced to replace the cleaning bath on a regular basis. The additional cleaners that we examined included Micro, Impro-Clean 3800, RB Degreaser, and Uniclean MI. We also examined D-Greeze 500 which was a nonaqueous, organic-solvent cleaner. We tested these alternate cleaners with our oil- coated stainless steel discs at 25°C and 60°C at full strength and diluted to 10% and 20%. The results of the XPS analyses of these cleaning tests are summmed in Table 4 in the form of the measured Fe/C atomic ratios.

The best overall results were obtained with Micro. It was ine&ctive at fbll strength, but worked as well at a concentration of 10% and 20%. The cleaning efficiency of Micro decreased when it was used at the higher temperature. The best conditions for using Micro are at room temperature and a concentration of 10%.

The next best cleaners were Sonicor and Impro-Clean 3800. The cleaning efficiency of Inpro-Clean 3800 was better at elevated temperature. There was little effect of concentration evident over the range of 10%-20%. The limited data for Sonicor indicate it was comparable to Inpro-Clean 3800 when used at 20% concentration at 60°C. (No data at room temperature were generated with Sonicor.)

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Citridet at fdl strength was a reasonable good cleaner, although not as good as Micro, Sonicor, and Inpro-Clean 3800. When diluted to 20%, however, Citridet &o=d poorly as a cleaner. Its efficiency also dropped when it was used at room

Table 4. Summary of XPS Data for Stainless Steel Discs Contaminated with Vacuum-Pump Oil and Cleaned with Various Cleaners.

Concentration, Temperature, FdC, Sample o/. "C a/a

Micro

Impro-Clean 3800

RBDegreaser

Citridet

Sonicor

UnichVzI

D-Greeze 500

Trkhloroethane

100 20 10

100 20 10

20 10

100 20 10

20 10

20 20

100

20

33 10

100

100

25 25 25 60 60 60

25 25 60 60 60

60 60

25 60 60

55

25 25

25

114

0.087 0.58 0.59 0.043 0.45 0.35

0.31 0.33 0.091 0.39 0.36

0.191 0.208

0.0174 0.060

>0.228

0.374

0.082 0.014

0.30

N.A."

Not available.

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temperature. The inability to use Citridet at other than 111 strength makes it more expensive to use than the other aqueous cleaners. This, coupled with its strong odor, and need to be used at elevated temperatures to be effective in cleaning, makes it unattractive for our use.

When diluted to 10%-20%, RB Degreaser at 60°C was comparable to Citridet at the same temperature. (No room-temperature data were generated for this cleaner.) The cleaning power was not dependent upon concentration over this range, which is similar to what was observed with Micro and Impro-Clean 3800. It was still inferior to these latter two cleaners, however.

The least'effective aqueous cleaner was Uniclean VII. It was inefkctive at room temperature and its cleaning efficiency was degraded when it was diluted. It would be totally unacceptable for our cleaning applications.

The D-Greeze 500 organic-solvent cleaner was comparable to Inpro-Clean 3800 in cleaning power which could make it a reasonable candidate for our needs. As indicated earlier, however, its flammability would make it unsuitable for our use, because of the ES&H concerns that would have to be addressed-concerns that wouldn't exist with the use of aqueous cleaners that are equal or better in their cleaning effectiveness.

Based on the results of the XPS analyses, the cleaners evaluated in this study are ranked in Table 5 in the order of their efkctiveness. Micro had excellent cleaning capabilities at room temperature at relatively low concentration. This, coupled with its environmental fiiendliness, makes it a good candidate for cleaning stainless steel parts for thermal batteries as a replacement for vapor degreasing with TCE.

Table 5. Optimum Cleaning Conditions for Various Cleaners Evaluated in This Study in Order of Decreasing Effectiveness Based on XPS Analyses.

Cleaner Temuerature. "C Concentration. YO

Micro Inpro-Clean 3800 Sonicor D-Greeze 500 Citridet RB-Degreaser Uniclean VII

25 60 55 25 60 60 25

10 20 20

100 100 10 33

15

i

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It should be noted here that the lifetime of baths made with any of the aqueous cleaners has not been addressed at this time; ie., the relative eWiveness with continued use is unknown. This is an area where bath mnitoring with the QCM would be ideally suited.

QCM Evaluation

Theory The resonance frequency of the QCM will be affected by any changes to its &e, such as the addition of athin oil film or contatninatlt . The deposition of a film of oil, for example, will cause the oscillation fiequency to be damped, resulting m a shift to a lower resonance fkquemy. At the same time, the voltage signal from the oscillator circuit incorporated into the immem'ble QCM text fixture will increase.

The shift in frequency of the QCM in the case of an oil 5lm has been measured and compared to that calculated using the Sauerbrey equation.'J The Sauerbrey equation can be r e d d to the following:

Af= -cfAm (1)

where -Gis the sem%v&y &or and is equal to 56.6 Hz-cmz/pg at 5 MHz and Am is the change in the f k t mass? For oil &.I thicknesses up to 1.15 pm, the calculated shift m resonance fiequency was in good agreement with that calc- with the Sauerbrey equation. That is, the shift in fiequency was found to be %rly linear fir oil film thicknesses up to 1.15 pm. Above about 3 jm, the frequency response levels off and the acoustic signaI becomes completely damped by the slm.

When the hmersible QCM fixture is immersed in a liquid, such as an aqueous cleaning bath, a considerable negative shift m resonance frequency of the QCM to lower values will take place. In the case of a QCM that has a film of oil Wing cleaned off the &e, an ofktting shift to higher frequency will occur-along with 0 corresponding decay in the voltage of the oscillator circuit-while the film of oil is being removed during aqueous cleaning. Though this ShiR is small, the oscillator circuit incorporated into the test fixture is sensitive enough to detect this ofl%et. As an example, for a ilhn of oil 1.5 pm thick and a sensitivity fixtor of 56.6 Hz-cm2/pg, the corresponding shift in the QCM frequency will be 6,500 Hz.

Thus, ifthe QCM is coated with a thin fdm of the expected contaminan-oil, in the case of the stainless steel current collectors fbr thermal batteries-the response of the QCM during aqueous cleaning can be used to determine when all of the oil has beenremoved.

The rate of decay of the damping voltage from the oscillator output circuit can be used to obtain kinetic data about the cleaning process. Generally, the decay can be f3ted to an

16

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exponential firnction of the type:

The time constant for the cleaning process, 2, can be extracted by 6itting the voltage decay to Equation 2. The d e r that z is, the faster the Sufface of the QCM is being cleaned. This provides a means of comparing Merent cleaners under various cleaning conditions.

Results of cleaning Tests The suitability of the QCM for monitoring of aqueous cleaning baths was examined with several of the cleaniug solvents. The tests conducted with Micro at concentrations of 2%, IO%, and 20% at 23OC and 5OoC will be reported dong with simiIar data for Impro-Clean 3800, Similar tests were conducted with DI water fbr control purposes.

Bath TemDerature of 23°C - The fiequency and voltage response of the QCM when it was covered with a thin film of oil and then immersed into a bath of DI water at 23°C are shown in Figures 6a and 6b, respectively. The figures are partitioned hto five distinct regions for ease of discussion.

In region I, a thin flm of oil is applied to the QCM &e in air. This causes a rapid damping of the resonance fiequency by -3,400 Hz and a corresponding increase m oscillator voltage of - 0.5 V. The change continues as the film redistriibutes itself across the s h of the QCM, S h sorption of moisture may also be occurring at the same time.

In region II, the QCM is inserted into the DI water. The final steady-state resonance kquency will reflect the loading of the signal damping by the water and any o&ts (increases) caused by oil removal.

In region III, the QCM is removed fiom the bath and physically cleaned by repeated spraying with aqueous cleaning solution followed by rinses with DI water. The erratic signal during this external cleaning process is due to the rapid changes taking place on the surfkce of the QCM as the sufface is alternately wet and then dry.

Region IV shows the response of a clean QCM when immersed in clean DI water. The &rence in the steady-state fiequency in region IV with that in region II allows the amount of oil remaining to be determined. When all the oil has been removed by the cleaning process, the two values will be identical. The poor removal of oil that would be expected for DI water is reflected m the large &reme in the steady-state hquency values for these two regions.

17

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_ _ _

-500

-4000 2.17

2.1 0

2.03

> ̂ 1.96

& 1.89

e 1.82

1.75

1.68

1.61

J

CG

3

1

I I I

Region I

I

I I I I I I I I I

I I I I I I I I I I I I I I I I I I a)

0 500 1000 1500 200

Time (s)

Figure 6. cleaning Experiment at 23°C with DI Water. a) Oscillator Frequency Response. b) Damping Voltage Resonse.

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Region V shows the response of the QCM after removal fiom the bath, cleaning, and drying. The accuracy of the test results are verified ifthe response in region V is identical to that for region I. This serves as a check on instnunentation and the experimental procedure.

The response of the QCM during coating with a thin film of oil and subsequent cleaning at mom te-rature in 10% Micro is shown in Figures 7a and 7b. Note that the steady-state fiequency in region II during cleaning is very close to that in region IV as a r e d of effective oil removal. The relative response with 20% Micro as well as solutions of Inpro- Clean 3800 was very simifat to that of 10% Micro.

Bath Temnerature of 50°C - The response of the QCM when immersed in a DI water at 50°C is shown iri Figures 8a and 8b. The application of the initial 03 film at room temperature is shown in region I. The QCM jixture was then immersed in the hot bath of DI water, The stability of the ftequency signal was not as good as at room temperature because of thermal eExts. This resulted in the large overshoot in the frequency response. A similar overshoot (spike) is evident m the vohage response. Still, when the QCM was thermally equi l i ied at room temperature, (regions III and V), the fiequency and voltage responses returned to the original values.

The response of the QCM when immersed in a bath of 10% Micro at 50°C is shown in Figures 9a and 9b. The overshoot in the ftequency and voltage is similar to that observed with the DI water under the same conditions. The data in region fv indicate that the sensor may not have reached thermal equiliirium during this test. The similar ofiets m frequency in regions II and N indicate effective removal of the oil.

As discussed previously, analysis of the voltage response during the cleaning process provided i n f o d o n of the kinetics of the cleaning process. The effect of Micro concentration on the rate of cleaning at room temperature is shown in Figure 10 for three cent concentrations. This same infbnnation is presented in tabular form in Table 6 as part of the summary of the cleaning tests. As can be seen, the cleaning rate was much M e r (lower z) in 10% Micro than in 2% Micro, with only a slight increase in going to 20% Micro.

The results of the QCM experiments indicate that cleaning efkctiveness increased with increase in concentration for both cleaners at both temperatures. The cleaning rate constant, 7, decreased with increasing concentration for both Micro and Inpro-Clean 3800 at 23"CY which reflects the enhanced kinetics at higher concentrations. The values of z at 50°C were much lower than their counterparts at 23°C which shows that higher temperatures also improved the cleaning rate. The effect of concentration at 50°C upon z was simitm to that at 23°C for Inpro-Clean 3800 but was reversed for Micro. This may be due to degradation of the active cleaner in Micro at elevated temperatures.

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1000

0

n N I -1000 U

h 0

=I b a, 2 -3000 4

5 -2000

-4000

-5000 2.17

2.10

2.03

> ̂ 1.96

1.89

.)lr 1.82

1.75

U

a

P 1.68

1.61

I

- I I

- - -

D I I I

Region I I

F

.

I I I I I

I I I I I I I I I I I I I I

0 200 400 600 800 I000 1200 1400 1600

Time (s)

Figure 7. cleaning Experiment at 23°C with 10% Micro. a) OsciIlator Frequency Response.' b) Damping Voltage Resonse.

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Time (s)

Figure 8. cleaning Experiment at 50°C with DI Water. a) Oscillator Frequency Response. b) Damping Voltage Resonse.

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0

-500

-1000

-1500

-2000 u, -4 -2500

n N I

SI S

L

-3000

-3509 2.1

2.10

2.03

1.96

& 1.89 m = 1.82

1.75

J

8

1.68

1.61

800 I000 1200

Time (s)

Figure 9. Cleaning Experiment at 50°C with 10% Micro. a) Oscillator Frequency Response. b) Damping Voltage Resonse.

... - .

22

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I I I 1 I I 1

0 50 100 150 200 250 300

l ime (s) Figure 10. Damping Voltage Resonse of Oscillator at 23°C for 2%, lo%, and 20% Micro.

The data in Table 6 show that the relative amount of oil removed at 23°C was enhanced with increase in cleaner concentration for both cleaners. The amount removed was greater for the 10% and 20% Micro solutions compared to the corresponding Inpro-Clean 3800 solutions. This is consistent with the XPS data (Table 4). At 5OoCy however, oil removal was more complete with the Inpro-Clean 3800 and the efiiency of Micro decreased. Again, this is in generally good agreement with the results of X P S analysesy when the

23

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Table 6. Summary of Results of Cleaning Tests with QCM in DI Water and Micro Solutions

Temperature, Amount of Oil Cleaning Solution "C Removed, '90 Constant (T), s

DI Water 23 86.0 42

2% Micro 23 98.4 29 10% Mcro 23 98.9 16 20% Micro 23 100 12

10% Inpro-Clean 23 94.7 20% Inpro-Clean 23 97.1

6.5 6.1

DI Water 50 88.0 4.9

2% Micro 50 94.3 10% Micro 50 97.3 20% Micro 50 100

10% Inpro-Clean 50 100 20% Inpro-Clean 50 100

3.9 4.5 7.0

1.4 0.7

experimentat error is considered. Inpro-Clean 3800 was M e r in cleaning oil fiom the QCM but it was not as complete as Micro unless elevated temperatures were used.

The repeatability and sensitivity of the QCM have been shown to be exceptional. The noise associated with the frequency response of the QCM in a liquid medium amounts to only 1 HZ. his translates to a mass change of only 20 ng/cm2. What is more important, this change can be measured in real time during cleaning. Experiments perfbrmed during which the QCM was repeatedly wet and dried to remove liquid e m s have shown a reproducibii of 0.6 Hz. This is equivalent to a mass change of 12 ng/cm*. The

- 4 sensitivity of the QCM is p t enough to detect less than a monolayer of contamman t.

Simplified QCM Instrumentation The experimental setup used for monitoring the response of the QCM for this study would be more complicated than desired for routine bath surveillance, in t e r n of instrumentation

24

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required. A prototype comparator circuit has been developed that would not require added tioa The circuit was designed to use the damping voltage to fbllow the cleatkg process. A & . i o n is necessary to determine the voltage thresholds for "dirty", "clean", and "dry" states of the QCM. Once the threshold cdiitions have been done, simple LED readouts on the control panel are used to fbllow the cleaning process.

Such a circuit would be more tban adequate fix our cleaning purpose and would provide instant visual indication to the operator when to remove the parts from the cleaning bath. "hi$ wouId not require the .training that operation ofthe more-complicated system entails.

Future Work

Additional work is necessary to correlate the results of the XPS measurements with those made with the QCM Initially, experiments were planned where the immersible QCM would be placed in the cleaning bath dong with the oilaated stainless steel discs during cleaning. The res& of the XPS analyses could then be directly compared to the cleanhg data &om the QCM. This would allow a one-to-one comparison of data generated under the same conditions.

Another area that merits further work is the incorporation of a thermistor (or similar temperature-dependent device) and associated circuitry mto the QCM test fixture to automatically compensate the response parameters of the sensor for temperature. This should provide greater signal stability over varying temperatures.

Conclusions

XPS is a sensitive tool fbr monitoring the clanliness of metal parts after being subjected to various cleaning processes. The XPS data show that aqueous cleaners perform as well as or even better than conventional vapor degreasing with trichloroethylene or solution cleaning with trichloroethane. A number of commercial aqueous cleaners can be considered as cleaning alternatives. Comparable cleaning can be attained depending on the temperature and concentrations used. For roomtemperature applications at a reasonable cost, a 10% Micro solution provides excellent cleaning. This material is environmentally i?k~.~dly, which makes it attractive for cleaning applications within the DOE nuclear-weapon complex

The QCM was shown to be a viable, sensitive, and accurate technique fbr monitoring the cleanliness of an aqueous cleaning bath. The prototype developed at Sandia provides both a frequency and voltage output that allow the cleaning process to be monitored in real time. The voltage relaxation during cleaning provides a means of monitoring the kinetics of the cleaning process. fnpro-Clean 3800 is faster than Mcro in cleaning but is not as thorough. The QCM data were in generalty good agreement with the results of the X P S

25

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analyses. More work is needed to obtain a one-to-one comparison for the two types of data fbr ultimate validation.

References

1. T. W. Scbneider, G. C. Frye, S. J. Martin, and J. J. Spates, Anal. Chim. Acta, 309,53 (1995). 2. G. Moore, ‘Wnted Wire Boards Cleaned with d-limonene,” General Electric Co., Neutron Devices Dept.,. Laboratory Operation Internal RepoH CHM90-056, September 13,1990.

3. P. T. Varheau and D. A. Buttrey, J. P@s. Chem., 91, 1292 (1987).

4. T. W. Schneider and D. A. Buttrey, J. Am. Chem. Soc., 115,12391 (1993).

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