[0001] In pending U.S. patent application Serial No. 07/297,366, filed February 15, 1989,
constant-boiling, azeotrope-like compositions comprising 1,1-dichloro-2,2,2-trifluoroethane
(HCFC-123) and 1,1-dichloro-1-fluoroethane (HCFC-141b) with methanol and ethanol are
described as effective cleaning solvent compositions, particularly with regard to
the cleaning of electronic circuit boards.
[0002] As described in the aforementioned application, current industrial processes for
soldering electronic components to circuit boards involve coating the entire circuit
board with a flux composition and, thereafter, passing the coated side of the board
over preheaters and then through molten solder. The flux composition cleans the conductive
metal parts and promotes solder adhesion. Commonly used fluxes consist, for the most
part, of rosin used alone or rosin with activating additives, such as amine hydrochlorides
or oxalic acid derivatives.
[0003] After soldering, which thermally degrades part of the rosin, flux and flux residues
are often removed from the board with an organic solvent composition. Since requirements
for the removal of contaminants from circuit boards are very stringent, most current
industrial circuit board cleaning processes involve the use of vapor defluxing techniques.
In the conventional operation of a vapor defluxer, the soldered circuit board is passed
through a sump of boiling organic solvent, which removes the bulk of the rosin---including
thermally degraded rosin --and thereafter, through a sump which contains freshly distilled
solvent and finally through solvent vapor above the boiling sump, which condenses
on the circuit board to provide a final rinse with a clean, distilled solvent. Additionally,
the circuit board could also be sprayed with distilled solvent, if required, before
the final rinse.
* equivalent to EP-0392668-A
[0004] While constant-boiling, azeotrope-like compositions of 1,1-dichloro-2,2,2-trifluoroethane
and 1,1-dichloro-1-fluoroethane, as described in pending U.S. Patent Application Serial
No. 07/335,946, filed April 10, 1989*, are excellent solvent systems for cleaning
circuit boards, for practical industrial use these solvent systems, as is the case
with many solvent systems, should be stabilized against compositional changes during
both use and long term storage. Changes, such as oxidation, polymerization, component
interactions, and the like, may generate products which adversely affect the circuit
boards being cleaned or the solvent compositions themselves.
[0005] It is therefore an object of the present invention to provide constant-boiling, azeotrope-like
compositions of 1,1-dichloro-2,2,2-trifluoroethane and 1,1-dichloro-1-fluoroethane,
which are compositionally stable during use and long term storage and which minimize
the formation of undesirable reaction products, which may adversely affect electronic
circuit board cleaning.
INVENTION SUMMARY
[0006] What has been discovered is a stabilized azeotrope-like composition comprising an
azeotrope-like composition consisting of effective amounts of 1,1-dichloro-2,2,2-trifluoroethane
and 1,1-dichloro-1-fluoroethane, such azeotrope-like composition having a boiling
point of about 31°C at substantially atmospheric pressure and a stabilizer package
comprising one or more of effective stabilizing amounts of nitromethane, diisopropylamine,
1,2-butylene oxide and/or 4-methoxyphenol. The stabilizer package may also comprise
effective stabilizing amounts of 1,2-propylene oxide and nitromethane with or without
one or more of diisopropylamine, 1,2-butylene oxide and/or 4-methoxyphenol.
DETAILED DESCRIPTION OF THE INVENTION
[0007] By effective amounts is meant the amounts of 1,1-dichloro-2,2,2-trifluoroethane (HCFC-123)
and 1,1-dichloro-1-fluoroethane (HCFC-141b), which, when combined, result in the formation
of the azeotrope-like compositions of the instant invention as disclosed in U.S. Patent
Application Serial No. 07/335,946, filed April 10, 1989, incorporated herein by reference,(EP-0392668-A).
[0008] By effective stabilizing amounts is meant at least some of one or more of nitromethane,
diisopropylamine, 1,2-butylene oxide and/or 4-methoxyphenol. Also, by effective stabilizing
amounts is meant at least some of 1,2-propylene oxide and nitromethane with or without
one or more of diisopropylamine, 1,2-butylene oxide and/or 4-methoxyphenol. When the
effective stabilizing amounts of the disclosed compounds are combined with the azeotrope-like
composition of 1,1-dichloro-2,2,2-trifluoroethane (CHCl₂CF₃) and 1,1-dichloro-1-fluoroethane
(CCl₂FCH₃), they allow such azeotrope-like composition to be used and stored commercially,
i.e., provide commercially acceptable appearance, corrosivity and resistance to loss
of integrity of the azeotrope-like composition.
[0009] Commercially available HCFC-123 may contain minor amounts of 1,2-dichloro-1,1,2-trifluoroethane,
e.g., as much as about 20.0 weight percent 1,2-dichloro-1,1,2-trifluoroethane (HCFC-123a)
which mixture is intended to be covered by the language 1,1-dichloro-2,2,2-trifluoroethane
(HCFC-123) as well as the inclusion of minor amounts of other materials which do not
significantly alter the azeotrope-like character of the cleaning solvent compositions.
[0010] The stabilized compositions of the present invention may comprise admixtures of effective
amounts of 1,1-dichloro-2,2,2-trifluoroethane and 1,1-dichloro-1-fluoroethane, which
compositions form azeotrope-like compositions which may contain one or more of about
0.1 to 0.8 weight percent of nitromethane, about 0.05 to 0.4 weight percent 1,2-propylene
oxide, about 0.025 to 0.2 weight percent diisopropylamine and about 0.002 to 0.016
weight percent 4-methoxyphenol, said stabilizer weight percentages are based on the
weight of the azeotrope-like compositions.
[0011] The present azeotrope-like compositions comprise admixtures of 1,1-dichloro-2,2,2-trifluoroethane
and 1,1-dichloro-1-fluoroethane, more specifically, the present compositions comprise
mixtures of about 1-99 weight percent 1,1-dichloro-2,2,2-trifluoroethane and about
99-1 weight percent 1,1-dichloro-1-fluoroethane.
[0012] The present azeotrope-like compositions may also comprise admixtures of about 20-80
weight percent 1,1-dichloro-2,2,2-trifluoroethane and about 80-20 weight percent 1,1-dichloro-1-fluoroethane
which boil at about 31°C, at substantially atmospheric pressure.
[0013] It has been found that azeotrope-like compositions of the instant invention which
contain a minimum of about weight percent 1,1-dichloro-2,2,2-trifluoroethane are nonflammable,
as determined by a flammability test similar to ASTM E918.
[0014] A preferred azeotrope-like composition of the instant invention has the following
composition: about 65 weight percent 1,1-dichloro-2,2,2-trifluoroethane and about
35 weight percent 1,1-dichloro-1-fluoroethane. The azeotrope-like composition boils
at about 31°C, at substantially atmospheric pressure.
[0015] The above azeotrope-like compositions are effective solvents for cleaning electronic
circuit boards. Such solvent compositions are characterized by desirable properties
of relatively low boiling points, non-flammability, relatively low toxicity and high
solvency for flux and flux residues. The components also permit easy recovery and
reuse without loss of their desirable characteristics because of their azeotrope-like
natures and relatively low boiling points.
[0016] While the azeotrope-like compositions of 1,1-dichloro-2,2,2-trifluoroethane and 1,1-dichloro-1-fluoroethane
perform well in printed circuit board vapor defluxing-degreasing applications, it
is recognized that in order to take practical advantage of the unique properties of
these solvent compositions, certain other desirable properties should be imparted
to the compositions, particularly, when the solvent systems are to be used commercially.
[0017] One such desirable property is storage stability. It is recognized that any material
which is to be used commercially must usually be inventoried. Such storage can be
for short intervals or for longer periods of months or even years. Thus, for solvent
compositions to be useful, they should be stabilized against any significant deleterious
changes which may be brought about by oxidation, polymerization or component interaction
during storage or use. Such changes may result in solvent discoloration, the formation
of undesirable by-products, such as chloride ions and acids and/or the formation of
insoluble polymeric materials. It has been found that the addition of an one or more
of the compounds listed above, in the aforementioned concentration ranges, perform
as effective storage stabilizers.
[0018] Another commercially desirable characteristic to be imparted to the solvent system
is in-use stability. For example, as described above, in the vapor defluxing cleaning
procedure, the circuit board to be cleaned is first passed through a sump which contains
boiling solvent, for removal of bulk rosin, including thermally degraded rosin. In
this sump, the organic solvent is in contact with a heat source for a prolonged time.
After passage through the first sump, the circuit board is passed through a sump which
contains freshly distilled solvent and finally through solvent vapor over a boiling
sump, which provides a final rinse with a clean solvent which condenses on the circuit
board. Thus, in use, the organic solvent is subjected to constant heating either in
maintaining boiling sumps or in vaporizing the solvent to provide freshly distilled
solvent or vapor to condense on the circuit board for the final rinse. It is, therefore,
highly desirable to minimize any change in the solvent system which can adversely
affect the cleaning process or degrade the integrity of the solvent. As mentioned
earlier, such changes may be due to oxidation, polymerization or interaction between
the solvent system components.
[0019] For example, one such interaction which should be minimized is the interaction between
the hydrochlorofluorocarbons and metals, at elevated temperatures, which may generate
acidic by-products and chloride ions. Reactive metals such as zinc and aluminum as
well as certain aluminum alloys, which are often used as materials of circuit board
construction, are particularly susceptible to such interaction. It has been found
that nitromethane may be incorporated in the present solvent system in concentrations
of about 0.1 to 0.8 weight percent and effectively retard this type of attack and,
in addition, prevent the formation of gel.
[0020] The stabilizer package comprising diisopropylamine, in a concentration of about 0.025
to 0.2 weight percent, 4-methoxyphenol, in a concentration of about 0.002 to 0.016
weight percent, 1,2-propylene oxide, in a concentration of about 0.05 to 0.4 weight
percent, and nitromethane, in a concentration of about 0.05 to 0.8 weight percent,
enhances the stability of the present solvent system. All weight percentages are based
on the weight of the of the 1,1-dichloro-2,2,2-trifluoroethane and 1,1-dichloro-1-fluoroethane
azeotrope-like composition.
[0021] As shown in the examples, the stabilizers when used together in the present solvent
system (4-methoxyphenol, 1,2-propylene oxide, diisopropylamine and nitromethane) appear
to enhance the stability of the solvent system. The ranges of acceptable performance
for stabilizer concentrations when used together is the same as disclosed herein for
when they are used separately. It should be noted that stabilizer concentrations higher
than those specified can be employed; under normal circumstances, however, higher
stabilizer concentrations do not generally provide additional inhibition advantage.
[0022] Other acceptable inhibitor-stabilizer systems, which provide storage and use stability
to the aforedescribed azeotrope-like compositions are:
Inhibitor(s) |
Weight Percentage(s) |
Nitromethane |
0.2 |
Diisopropylamine |
0.05 |
1,2-Butylene oxide |
0.05 |
4-Methoxyphenol |
0.004 |
Nitromethane + 1,2-propylene oxide |
0.2 + 0.05 |
Nitromethane + 1,2-butylene oxide |
0.2 + 0.05 |
Nitromethane + 1,2-propylene oxide + diisopropylamine |
0.2 + 0.05 + 0.05 |
Nitromethane + 1,2-butylene oxide + diisopropylamine |
0.2 + 0.05 + 0.05 |
Nitromethane + 1,2-propylene oxide + 1,2-butylene oxide |
0.2 + 0.05 + 0.05 |
Nitromethane + 1,2-propylene oxide + 4-methoxyphenol |
0.2 + 0.05 + 0.004 |
[0023] The preferred stabilized, constant-boiling, azeotrope-like composition of the present
invention contains about 65 weight percent of 1,1-dichloro-2,2,2-trifluoroethane,
about 35 weight percent 1,1-dichloro-1-fluoroethane, about 0.1 to 0.8 weight percent
of nitromethane, about 0.05 to 0.4 weight percent 1,2-propylene oxide, and about 0.025
to 0.2 weight percent percent diisopropylamine and about 0.002 to 0.016 weight percent
4-methoxyphenol.
[0024] A more preferred, stabilized, azeotrope-like composition of the present invention
contains about 65 weight percent 1,1-dichloro-2,2,2-trifluoroethane, and about 35
weight percent 1,1-dichloro-1-fluoroethane, about 0.2 weight percent nitromethane,
about 0.05 weight percent 1,2-propylene oxide, about 0.05 weight percent diisopropylamine
and about 0.004 weight percent 4-methoxyphenol.
[0025] The present invention thus provides stabilized, azeotrope-like compositions of 1,1-dichloro-2,2,2-trifluoroethane
and 1,1-dichlorolfluoroethane, which can be stored for long periods periods of time,
which will undergo little or no change during either prolonged storage or commercial
use and which minimize both aluminum corrosion and gel formation.
[0026] The methods of combining the inhibitors with the azeotrope-like compositions of this
invention are well-known in the art. They can be prepared by any convenient method
including mixing or combining the desired component amounts in suitable containers.
A preferred method is to weigh the desired component amounts and thereafter combine
them in an appropriate container.
[0027] The aforestated stabilized, azeotrope-like compositions have low ozone depletion
potentials and are expected to decompose almost completely prior to reaching the stratosphere.
[0028] The stabilized, azeotrope-like compositions of the present invention permit easy
recovery and reuse of the solvent from vapor defluxing and degreasing operations because
of their azeotrope-like natures. As an example, the azeotrope-like mixture of this
invention can be used in cleaning processes such as described in U.S. Patent No. 3,881,949,
which is incorporated herein by deference.
EXAMPLES
[0029] Comparative seven day stability tests of solvent system combinations of about 65
weight percent 1,1-dichloro-2,2,2-trifluoroethane and about 35 weight percent 1,1-dichloro-1-fluoroethane
with various inhibitor combinations were carried out by refluxing 150 ml of the solvent
combination in a series of 500 ml Pyrex® flasks using 90 percent, at 25°C, water-saturated
solvents. The flasks were connected to water-cooled condensers, on top of which were
affixed Drierite® desiccant tubes to exclude atmospheric moisture from the test systems.
Additionally, stainless steel (SS-304) specimens were located at the refluxing solvent
vapor/air interfaces in the condensers and coupled stainless steel (SS-304)/aluminum
alloy (AL-7075) specimens were located in the boiling liquids.
[0030] The 1,1-dichloro-1-fluoroethane used in these tests contained about 500 parts per
million by weight of vinylidene chloride, an impurity normally found in the crude
product; however, no vinylidene chloride was used in test number 1 below. The solvent
inhibitor systems tested are described in the Table.
[0031] The following tests were performed on each individual test system subsequent to test
exposures:
1. Chloride ion concentration was measured at the end of the test by extracting the
solvent with an equal volume of deionized water and analyzing the water for chloride
ion concentration. The original, uninhibited, solvent contained less than 0.2 ppm
chloride ion. Chloride ion increase generally represents loss of solvent system component
stability. Stability loss is generally accompanied by increased acidity.
2. The pH changes of the solvent (final minus original) were determined by extracting
the acid from the solvents with equal volumes of pH neutral (pH = 7), deionized water
and checking the pH of the water.
3. Corrosion rates were measured by rubbing the metal surfaces with ink and pencil
erasers, brushing the surfaces, rinsing the specimens sequentially with 1,1,2-trichlorotrifluoroethane,
deionized water and acetone, drying for 24 hours over Drierite® desiccant and weighing
the sample to 0.0001 gram, Metal specimen weight loss is expressed in mils/year. An
aluminum (Al-7075) corrosion rate of 4 mils/year is considered acceptable.
4. Appearance of the solvent and the aluminum specimens (Al-7075) were rated visually
using the following rating criteria:
APPEARANCES |
RATINGS |
ACCEPTABLE |
LIQUID |
ALUMINUM-7075 (*) |
0 |
Yes |
NO CHANGE OR TRACE CHANGE |
|
|
Clear, colorless No gel drops. |
Bright and shiny. |
1 |
Yes |
VERY, VERY SLIGHT BUT ACCEPTABLE CHANGES |
|
|
Very slight, clear, colorless gel drops formed. |
Very, very slight corrosion on ca. 1% of surface. |
2 |
Borderline |
VERY SLIGHT BORDERLINE CHANGES NOTED, MAY OR MAY NOT BE ACCEPTABLE FOR INTENDED END
USE. |
|
|
Clear. Slight gel drops formed |
Very slight corrosion or black spot deposits on ca. 10-20% of surface. |
3 |
No |
SLIGHT, UNACCEPTABLE CHANGES NOTED |
|
|
Moderate amount of gel drops in the liquid. |
Slight spotting and corrosion on ca. 50% of surface. |
4 |
No |
Severe amount of gel in the liquid. |
- |
(*) All reactivity occurred on the Al-7075 surface which interfaced with the SS-304
in the liquid. The SS-304 specimens were essentially unchanged throughout the tests
except in test 13. |
TABLE
TEST NO. |
STABILIZERS |
SOLVENT |
Al-7075 CORROS. RATE, MILS/YR |
APPEARANCE RATINGS |
|
|
WT. % |
Δ pH |
Cl- |
|
LIQUID(X) |
Al-7075(Y) |
1 |
NONE |
0 |
0.0 |
0.8 |
0.9 |
0 |
1 |
2 |
NONE |
0 |
0.5 |
0.9 |
0.9 |
4 |
0⁺ |
3 |
NM |
0.2 |
0.1 |
0.7 |
0.3 |
0 |
0⁺ |
4 |
DIPA |
0.05 |
0.1 |
1.1 |
1.0 |
0 |
1 |
5 |
1,2-PO |
0.05 |
-0.4 |
0.5 |
0.8 |
4 |
1 |
6 |
1,2-BO |
0.05 |
0.1 |
0.4 |
1.1 |
0 |
0 |
7 |
4-MP |
0.004 |
0.2 |
0.4 |
0.8 |
0 |
0⁺ |
8 |
NM |
0.2 |
0.2 |
0.4 |
0.9 |
0 |
0⁺ |
|
1,2-PO |
0.05 |
|
|
|
|
|
9 |
NM |
0.2 |
0.0 |
0.3 |
1.2 |
0 |
1 |
|
1,2-BO |
0.05 |
|
|
|
|
|
10 |
NM |
0.2 |
0.0 |
0.8 |
0.9 |
0 |
1 |
|
1,2-PO |
0.05 |
|
|
|
|
|
|
DIPA |
0.05 |
|
|
|
|
|
11 |
NM |
0.2 |
-0.1 |
0.7 |
1.1 |
0 |
0⁺ |
|
1,2-BO |
0.05 |
|
|
|
|
|
|
DIPA |
0.05 |
|
|
|
|
|
12 |
NM |
0.2 |
0.0 |
0.8 |
0.9 |
0 |
0 |
|
1,2-PO |
0.05 |
|
|
|
|
|
|
DIPA |
0.05 |
|
|
|
|
|
|
4-MP |
0.004 |
|
|
|
|
|
13 |
DIPA |
0.05 |
0.0 |
2.5 |
2.5 |
0 |
0 |
|
1,2-PO |
0.05 |
|
|
|
|
(1)* |
*On SS-304 surface in air space above condensing vapor. |
(X) All ratings are based on gel formation in the liquid phase. |
(Y) Relation of metal ratings to appearance changes. All ratings are based on the
appearance of the Al-7075 surface in the liquid phase except as noted. |
AL-7075 = 1 = very, very, slight corrosion on about 1% of surface |
SS-304 = 1 = very, very slight haze on about 20% of the metal surface. |
The abbreviations used in the Table are:
1,2-BO = 1,2-butylene oxide
1,2-PO = 1,2-propylene oxide
NM = nitromethane
4-M = 4-methoxyphenol
DIPA = diisopropylamine
1. A stabilized azeotrope-like composition comprising an azeotrope-like composition
consisting of about 80-20 weight percent of 1,1-dichloro-2,2,2-trifluoroethane and
about 20-80 weight percent of 1,1-dichloro-1-fluoroethane, said azeotrope-like composition
having a boiling point of about 31°C at substantially atmospheric pressure, said azeotrope-like
composition in admixture with effective stabilizing amounts of one or more of nitromethane,
diisopropylamine, 1,2-butylene oxide and 4-methoxyphenol.
2. The stabilized azeotrope-like composition of Claim 1 wherein about 65 weight percent
1,1-dichloro-2,2,2-trifluoroethane and about 35 weight percent 1,1-dichloro-1-fluoroethane
is present.
3. The stabilized azeotrope-like composition of Claim 1 wherein about 0.2 weight percent
nitromethane is present, said weight percent based on the weight of the azeotrope-like
composition.
4. The stabilized azeotrope-like composition of Claim 1 wherein about 0.05 weight
percent diisopropylamine is present, said weight percent based on the weight of the
azeotrope-like composition.
5. The stabilized azeotrope-like composition of Claim 1 wherein about 0.05 weight
percent 1,2-butylene oxide is present, said weight percent based on the weight of
the azeotrope-like composition.
6. The stabilized azeotrope-like composition of Claim 1 wherein about 0.004 weight
percent 4-methoxyphenol is present, said weight percent based on the weight of the
azeotrope-like composition.
7. A stabilized azeotrope-like composition comprising an azeotrope-like composition
consisting of about 80-20 weight percent of 1,1-dichloro-2,2,2-trifluoroethane and
about 20-80 weight percent of 1,1-dichloro-1-fluoroethane, said azeotrope-like composition
having a boiling point of about 31°C at substantially atmospheric pressure, said azeotrope-like
composition in admixture with effective stabilizing amounts of 1,2-propylene oxide
and nitromethane with or without one or more of diisopropylamine, 1,2-butylene oxide
and 4-methoxyphenol.
8. The stabilized, azeotrope-like composition of Claim 7 wherein about 0.05 to 0.8
weight percent nitromethane, about 0.05 to 0.4 weight percent 1,2-propylene oxide,
about 0.025 to 0.2 weight percent diisopropylamine and/or about 0.002 to 0.016 weight
percent 4-methoxyphenol is present, said weight percents based on the weight of the
azeotrope-like composition.
9. The stabilized, azeotrope-like composition of Claim 7 wherein about 0.2 weight
percent nitromethane, about 0.05 weight percent 1,2-propylene oxide, about 0.05 weight
percent diisopropylamine and about 0.004 weight percent 4-methoxyphenol is present
10. The stabilized azeotrope-like composition of Claim 7 wherein about 0.2 weight
percent nitromethane and about 0.05 weight percent 1,2-propylene oxide are present,
said weight percents based on the weight of the azeotrope-like composition.
11. The stabilized azeotrope-like composition of Claim 7 wherein about 0.2 weight
percent nitromethane, about 0.05 weight percent 1,2-propylene oxide and about 0.05
weight percent diisopropylamine are present, said weight percents based on the weight
of the azeotrope-like composition.
12. The stabilized azeotrope-like composition of Claim 7 wherein about 0.2 weight
percent nitromethane, about 0.05 weight percent 1,2-propylamine oxide and about 0.05
weight percent 1,2-butylene oxide are present, said weight percents based on the weight
of the azeotrope-like composition.
13. The stabilized azeotrope-like composition of Claim 7 wherein about 0.2 weight
percent nitromethane, about 0.05 weight percent 1,2-propylamine oxide and about 0.004
weight percent 4-methoxyphenol are present, said weight percents based on the weight
of the azeotrope-like composition.
14. A process for cleaning a solid surface comprising the use of the stabilized azeotrope-like
composition of Claim 1.
15. A process for cleaning a solid surface comprising the use of the stabilized azeotrope-like
composition of Claim 7.
16. A process for expanding a polymeric foam comprising the use of the stabilized
azeotrope-like composition of Claim 1 as a blowing agent.
17. A process for expanding a polymeric foam comprising the use of the stabilized
azeotrope-like composition of Claim 7 as a blowing agent.