AU640760B2

AU640760B2 - Solvent cleaning of articles

Info

Publication number: AU640760B2
Application number: AU73913/91A
Authority: AU
Inventors: David George Mcbeth; Neil Winterton
Original assignee: Imperial Chemical Industries Ltd
Current assignee: 3M Co
Priority date: 1990-04-04
Filing date: 1991-03-28
Publication date: 1993-09-02
Anticipated expiration: 2011-03-28
Also published as: DE69131737T2; CA2039828A1; EP0450855B1; KR100205296B1; ATE186071T1; DE69131737D1; CA2039828C; EP0450855A2; EP0450855A3; NZ237628A; KR910018532A; JPH05271692A; ES2140382T3; IE911028A1; JP2961924B2; AU7391391A; GB9007645D0

Abstract

Low molecular weight, fluorine-containing ethers of boiling point 20 DEG C to 120 DEG C are used in solvent cleaning applications.

Description

AUSTRALIA

Patents Act COMPLETE SPECIFICATION

(ORIGINAL)

Class Application Number: Lodged: Complete Specification Lodged: Accepted: Published: Priority 640. C7 Int. Class Related Art: @0 @0

S

0 0@ 600 Applicant(s): Imperial Chemical Industries PLC Imperial Chemical House, Millbank, London SW1P 3JF, UNITED KINGDOM S 0 0 0 0 0 0 0 Address for Service is: PHILLIPS OPMONDE FITZPATRICK Patent and Trade Mark Attorneys 367 Collins Street Melbourne 3000 AUSTRALIA Complete Specification for the invention entitled: SOLVENT CLEANING OF ARTICLES Our Ref 212006 POF Code: 1453/1453 The following statement is a full description of this invention, including the best method of performing it known to applicant(s): 1 6006 0 0 0* 0* QM 35692 SOLVENT CLEANING OF ARTICLES This invention relates to solvent cleaning applications in which contaminated articles such as, for example, metals, textiles, glass, plastics, electronic components and printed circuit boards are cleaned using a solvent or solvent vapour and more particularly to the use of low molecular weight ethers as solvents in solvent cleaning applications.

Solvent cleaning applications wherein contaminated articles are immersed in or washed with halogenated hydrocarbon solvents and/or the vapours thereof are well known and are in common use. Applications involving several stages of immersion, rinsing and drying are common and it is well known to use the solvent at ambient temperature (often accompanied by ultrasonic agitation) or at an elevated temperature up to the boiling point of the solvent. Examples of solvents used in these cleaning processes are 1,1,2-trichloro- 20 1,2,2-trifluoroethane, 1,1,1-trichloroethane, trichloroethylene, perchloroethylene and methylene chloride. These solvents are used alone or in mixtures with cosolvents such as aliphatic alcohols or other low molecular weight, polar additives and depending to some extent upon the articles to be cleaned are often stabilised against degradation induced by light, heat and the presence of metals.

In the known common solvent cleaning applications and especially in those applications where the solvent is used at an elevated temperature, there is a tendency for solvent vapour to be lost from the cleaning system into the atmosphere. Further losses may occur in loading and unloading the solvents into cleaning plant and in recovering used solvent by distillation. Whilst care is usually exercised to minimize losses of solvent *0*9 0@r S. S S 0.

0

S.

00 S 0 05 S 2

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So into the atmosphere, for instance by improved plant design and vapour recovery systems, the expense of totally preventing losses is exhorbitant and most practical cleaning applications result in some loss of solvent vapour into the atmosphere.

Until recently, the use of the common cleaning solvents has been regarded as safe practice in that the solvents are stable, of low toxicity, non-flammable materials believed to be environmentally benign.

However recent evidence suggests that some at least of the common solvents may have a long-term deleterious effect on the stratosphere, the so-called ozone layer, so that a replacement solvent is seen to be desirable.

According to the invention there is provided the 15 use in solvent cleaning applications of solvents comprising low molecular weight fluorine-containing ethers of boiling point in the range of about 20 0 C to about 120 0

C.

The ether has a boiling point in the range 20 0 C to 120 0 C, preferably from 25 0 C to 85 0 C, such that it may be used in conventional and existing cleaning equipment.

For any particular cleaning application, an ether may be selected having a boiling point close to that of the solvent the ether is replacing.

25 The ethers can be obtained by reaction of a halogenated aliphatic olefin with an optionally halogenated aliphatic alcohol in known manner and thus contain at least three carbon atoms in the molecule.

Usually the ether will contain not more than five carbon atoms although it may contain six or more carbon atoms providing its boiling point is below about 120°C.

The ether contains at least one and will usually contain two or more fluorine atoms but will not -'nerally be perfluorinated. In addition to fluorine atoms, the ether may contain chlorine atoms, bromine 555,

S

55 5*

SS

3atoms and hydrogen atoms. Ethers containing chlorine and/or hydrogen may contain one or two chlorine atoms and/or one or two hydrogen atoms.

Examples of alcohols which may be used to produce the ethers are methanol, ethanol, propanol and butanol and halogenated derivatives thereof. Alkenes which may be used include tetrafluoroethylene, hexafluoropropene, chlorotrifluoroethylene and the chiorofluoropropenes and hydrogen-containing analogues of these compounds for example trifluoroethylene and chiorodifluoroethylene.

Examples of ethers which may be used, and their boiling points, include the following:- 0* S 6 a 0*e*ee 0 *0 *0 9 0.

0@ S 0

B.

S

S..

6S S* S Boiling Point (OC) 15 1,1-difluoroethyl methyl ether 47 1,1,2,2-tetrafluoroethyl methyl ether 36.5 1-chloro-1, 2, 2-trifluoroethyl methyl ether 70.6 1-1-dichloro-2, 2-difluoroethyl methyl ether 104.8 1-chloro-2,2-difluoroethyl methyl ether 27.5 1 1,1,1,2,3, 3-hexafluoropropyl methyl ether 54.5 1,1-difluoroethyl ethyl ether 1,1,2,2-tetrafluoroethyl ethyl ether 56 1-chloro-1,2,2-trifluoroethyl ethyl et!,ier 82 2 1,1,1,2,3,3-hexafluoropropyl ethyl ether 64.5 1,1,2,2-tetrafluoroethyl n-propyl ether 71.7 3 1-chloro-1,2,2-trifluoroethyl n-propyl ether 109 1,1,1,2,3, 3-hexafluoropropyl n-propyl ether 92 1-chloro-1, 2, 2-trifluoroethyl isopropyl ether 100 1-chloro-2,2--difluoroethyl isopropyl ether 53 4 1,1,1,2,3, 3-hexafluoropropyl isopropyl ether 76 1,1,2,2-tetrafluoroethy'. n-butyl ether 49 1,1,1,2,3, 3-hexafluoropropyl n-butyl ether 108 1,2, 2-trifluoroethyl 1,1, 1-trifluoroethyl ether 1,1,2, 2-tetrafluoroethyl 1, 1-difluoroethyl ether 77 di(1,1-difluoroethyl) ether 103 5* B S *5 6S 0 00 50 4 l-chloro-1,2,2-trifluoroethyl 1,1-difluoroethyl ether 102 1,1,2,2-tetrafluoroethyl 1,1di(trifluoromethyl)methyl ether 1 At 130 mm Hg 2 At 630 mm Hg 3 At 627 mm Hg 4 At 121 mm Hg At 113 mm Hg Mixtures of ethers, including azeotropic mixtures, may be used if desired as may mixtures of an ether with one or more cosolvents. The same cosolvents 15 may be used as are used with the principal solvents in known cleaning applications and in particular polar compounds such as alcohols are preferred cosolvents.

Cleaning compositions comprising the ether and a cosolvent, notably a lower alkanol cosolvent, are provided according to another feature of the invention.

Azeotropic mixtures of ethers and alcohols represent preferred embodiments of the invention. Lower aliphatic alcohols containing 1 to 4 carbon atoms are useful in such mixtures.

The ethers used according to the invention tend to be more stable than the commonly-used solvents and generally will not require stabilisation against degradation. However, stabilisers may be added if desired or if required for particularly onerous cleaning applications and the stabilisers used in the common solvents may be employed, notably nitroalkanes and epoxides.

The ethers may be used as replacements for the solvent(s) used in any of the known cleaning applications and have the advantage of being generally 5 0

S

*r S

B.

S

more stable towards aluminium than the solvents they replace. The ethers may be used to replace part of the solvent(s) used in known cleaning applications.

The invention is illustrated by the following examples.

EXAMPLE 1 This Example illustrates the use of 2-chloro-1,1,2-trifluoroethyl methyl ether in cleaning flux residues from copper-coated boards.

A known weight of solder cream was applied to test boards (5 cm x 7 cm) cut from copper-coated FR4 (epoxy/glass fibre laminate) board and the cream was reflowed in a MICRO VPS soldering unit. The solder cream used was a 62% tin/38% lead solder available as 15 Multicore PRAB 3.

2-chloro-1,1,2-trifluoroethyl methyl ether (boiling point 65*C at 630mm Hg) was boiled in a beaker fitted with an upper cooling coil through which cold water was circulated to create a boiling liquid phase and a vapour phase and the contaminated board was dipped into the boiling liquid for 60 seconds and then held in the vapour for 30 seconds.

Residual ionic contamination of the test board, expressed as mg sodium chloride per square centimetre 25 was determined using a Protonique Contaminometer. The ionic contamination of an unwashed test board was determined and the removal of ionic contamination was calculated. 61% of the ionic flux residues were removed from the test boards.

The ether was heated to 190 0 C and the vapour pressures above the ether were determined over the range 190 0 C. A slight increase in vapour pressure was observed at approximately 120 0 C but there was no visible evidence of solvent breakdown at this temperature.

0*SS~

S

S 0 0, SS S 6

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a *o C *0 0 S.oo In a Comparative Test, using 1,1,2-trichloro-1,2.--trifluoroethane as the solvent, of the ionic flux residues were removed.

EXAMPLE 2-3 These Examples illustrate the use of mixtures of 2-chloro-l,1,2-trifluoroethyl methyl ether and methanol for cleaning flux residues from copper coated printed circuit boards.

In Example 2, a mixture of 2-chloro-1,1,2trifluoroethyl methyl ether and methanol was boiled until a constant boiling mixture was obtained. This azeotrope contained 18.5% by weight of methanol and boiled at 56.8 0 C at normal pressure.

The azeotropic mixture was used to remove ionic 15 residues from the test boards as described in Example 1.

66.9% of the ionic resudes were removed.

In Example 3, the procedure of Example 2 was repeated except that a mixture of the ether (95% by weight) and methanol by weight) was used instead of the azeotropic mixture. 65.1% of the ionic residues were removed.

EXAMPLE 4 This Example demonstrates the stability of 2-chloro-1,1,2- trifluoroethyl methyl ether in the 25 presence of aluminium.

The ether was refluxed in contact with aluminium for 48 hours. The aluminium test piece was partly immersed in the liquid and partly in the vapour above the liquid.

In the test, no increase in chloride ion or fluoride ion was observed in the liquid phase and the GC trace of the solvent after the test showed no change.

There was no significant weight change in the metal test piece which emerged from the test clean and bright with no evidence of corrosion.

a..

55 *r S 0

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*r 0 06 5 66 C0 7 b, 00

S

*d C S 00 00 The results demonstrate that the ether has high stability in the presence of aluminium and is suitable for use in aluminium cleaning applications. Stabilisers may be added to inhibit the build up of acidity in the ether when it is used to clean metals.

EXAMPLE This Example illustrates the use rL tetrafluoroethyl methyl ether in cleaning flux residues from copper-coated boards.

Tetrafluoroethyl methyl ether, boiling point 33-35 0 C (630 mm Hg) and density (25 0 C) 1.28g/ml, was used to clean flux residues from copper coated boards as described in Example 1. 62% of the ionic flux residues were removed.

15 EXAMPLE 6-8 These Examples illustrate certain azeotropic mixtures suitable for use in the process according to the present invention.

Tetrafluoroethyl methyl ether forms an azeotrope with methanol containing 4% by weight methanol and boiling at 34.5 0

C.

The ether forms an azeotrope with 1,1,2-trichloro- 1,2,2 -trifluoroethane containing 39.5% by weight of the haloethane and boiling at about 34.9 0

C.

The ether forms a ternary azeotrope with 1,1,2-trichloro- 1.2,2-trifluoroethane and methanol containing 41% by weight of the haloethane and 3% by weight of methanol and boiling at about 34.5 0

C.

EXAMPLE 9 This Example illustrates the use of a ternary azeotropic mixture in the process according to the present invention.

The ternary azeotropic mixture of tetrafluoroethyl methyl ether, l,1,2-trichloro-1,2,2-trifluoroethane and methanol prepared in Example 8 was used to remove solder flux .4 S d.

60 d

A

8 residues from circuit boards by the procedure described in Example 1. 48.2% of the ionic flux residues were removed.

EXAMPLE 10-11 These Examples illustrate further azeotropic mixtures for use in the process according to the present invention.

Tetrafluoroethyl ethyl ether, boiling point 56°C and density 1.21 g/ml, forms an azeotrope with methanol containing 10,6% by weight of methanol and boiling at 48.6 0

C.

The ether forms an azectrope with ethanol containing 38.5% by weight of 1,1,2-trichloro-1,2,2trifluoroethane and boiling at 46.3 0

C.

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Claims

1. A process for cleaning articles which comprises contacting the articles with a solvent composition including a low molecular weight fluorine-containing ether of boiling point in the range of about 20 0 C to about 120 0 C, or the vapour thereof or both.

2. A process for cleaning article/s a'i claimed in claim 1 wherein the ether contains at least 3 carbon atoms.

3. A process for cleaning articles as claimed in claim 1 carried out at elevated temperature. S 13 4. A process for cleaning articles as claimed in claim I wherein the said ether has a boiling point in the range S of from 25 0 C to 80 0 C. A process as claimed in claim 1 wherein the solvent composition further includes a co-solvent.

6. A process as claimed in claim 5 wherein the co-solvent is a lower alkanol having up to 4 carbon atoms.

7. A process as claimed in claim 6 wherein the ether and the alcohol form an azeotropic mixture.

8. A solvent cleaning composition comprising a low molecular weight fluorine-containing ether having a boiling point in the range of 20 0 C to 120 0 C and a co-solvent.

9. A composition as claimed in claim 8 wherein the co-solvent is a lower alkanol having up to 4 carbon atoms.

10. A composition as claimed in claim 9 wherein the ether and the alcohol form an azeotropic mixture.

11. A compositoin as claimed in claim 8 wherein the low molecular weight fluorine-uontaining ether is at least one f4 1DN 9 -9 of 2-chloro-1,1,2-trifluoroethyl methyl ether, tetrafluoroethyl methyl ether, or tetrafluoroethyl ethyl ether.

12. A composition as claimed in claim 11 in the form of an azeotrope wherein the co-sclvent is at least one of methanol, ethanol or 1,1,2-trichloro-l,2,2-trifluoroethane.

13. A process as claimed in claim 1, substantially as hereinbefore described with reference to any one of the examples.

14. A solvent as claimed in claim 8, substantially as hereinbefore described with reference to any one of the examples. *0 S DATED: 29 June 1993 PHILLIPS ORMONDE FITZPATRICK Attorneys for: IMPERIAL CHEMICAL INDUSTRIES PLC *00 3282N S WDN 10