Note: Descriptions are shown in the official language in which they were submitted.
~1~49~
BACKCROUND OF THE INVEMTION
Methylene chloride is a highly versatile and useful -
solvent for various industrial applications at both normal and
elevated temperatures. A particularly important industrial use
is the vapor degreasing of metals. Methylene chloride is known
to be more stable than other chlorinated hydrocarbons solvent~
such as perchloroethylene, trichloroethylene and methyl chloro-
form when the solvents are used in unstabilized condition. For
example, methylene chloride is more resistant to oxidation, ;
10 hydrolysis and pyrolysis than other chlorinated solvents and ;
: ..
does not substantially react with aluminum in the aluminum scratch ~
test commonly used to indicate unstabilized or minimally stabil- -
ized methyl chloroform. In addition, methylene chloride may be
used to greater advantage ln vapor degreasing of metals than `~
other known degreasing solvents since it may be used effectively ~
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~49S68
at lower temperatures due to its lower boiling point and ex-
cellent stability. Methylene chloride is particularly desirable
for such degreasing operations since it is substantially
resistant to photochemical activity and therefore does not con-
tribute to air pollution by smog formation. Methylene chloride
disadvantageously suffers degradation by reaction of aliphatic
organic compounds such as trans-dichloroethylene l,l,l-tri-
chloroethane and carbon tetrachloride with said metals, metal
halides and combinations thereof. The reaction products are
colored tar-like masses which render the methylene chloride un-
suitable for use as a solvent, particularly in vapor degreasing -
of metals. Aliphatic organic compounds of this nature and
metals such as aluminum, iron and zinc, their halides and com-
~ . ' ,.
binations are generally introduced into the methylene chloride
from various cutting oils and lubricants used in metal fabri-
cating operations which are carried over into the methylene
chloride solvent during vapor degreasing or other cleaning of the
fabricated metal parts. Solvent manufacturing, handling and
stora~e equipment is another source for introduction of such
impurities. To prevent degradation and other types of deteriora-
tion such as oxidation, hydrolysis and pyrolysis which may occurin some instances, it has been the practice to incorporate minor
quantities of various organic compounds into methylene chloride,
which compounds act as stabilizers to substantially prevent such
degradation. It is desirable to provide methylene chloride
~ ,
stabilized to effectively prevent degradation in various appli-
cations, and the demand still exists for a low cost stabilized
methylene chloride composition that can be easily prepared and
which provides optimum stabilization under many different opera~
ting conditions
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~0~956~
SUMM~RY OF THE INVEMlION
An ob;ect of this invention is to prevent deterioration
or degradation of methylene chloride in association with metals,
metal halides and combinations including aluminum, iron and zinc,
halides of said metals and an aliphatic organic compound capable
of reacting with these metals, metal halides and combinations
thereof in the presence of methylene chloride.
A further ob~ect of this invention is to provide a
stabilized methylene chloride composition in which the stabilizerc ~ -
are low in cost and capable of being incorporated with ease into
the methylene chloride.
A still further ob~ect of this invention is to provide
a process for the degreasing of metals by contacting the metals
with methylene chloride stabilized to prevent degradation of the
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methylene chloride in the presence of metals, metal halides and
combinations thereof including aluminum iron and zinc, halides of ;
said metals and combinations and aliphatic organic compounds
Which react with the metals, metal halides and combinations
thereof.
These and additional objects of the present invention
will become apparent to those skilled in the art from the des~
cription and claims which follow. ` --
- ,. ~. -.
DESCRIPTION OF THE PREFERRED EMBODIMENTS ~
. . - ,
The ob~ects set forth above have been found to be ~ ;
attained by providing a composition consisting essentially of ~ ~
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methylene chloride containing stabilizing amounts of from about
0.001 to about 2.0 percent by weight of the methylene chloride
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of each of diisopropylamine, N-methyl pyrolle, butylene oxide,
propylene oxide, methyl acetate; acetone, tertiary amylene and
optionally methyl alcohol.
The quantity of the stabilizing agents useful in the
practice of this invention will vary depending upon the conditions
of use, the identity and quantity of other stabilizers incor- ;
porated into the methylene chloride and other practical operating
considerations. Each stabilizing agent or compound may generally ~-
be used within the range of from about .001 to about 2.0 percent
and preferably from about 0.002 to about 1.0 percent by weight
of the methylene chloride. Although higher concentrations may
be used, if desired, no additional benefit is obtained and the -
cost is unnecessarily increased. While the above composition
containing stabilizing agents provides optimum prevention of
degradation of the methylene chloride under a variety of operating -
conditions it is also possible to stabilize methylene chloride
by deleting the propylene oxide depending on the stabilization
required for the particular operating condition.
- ~ The stabilized composition may be used for the de~
greasing of metals by contacting the metals with the stabilized
composition. Thus, the process for vapor degreasing metals com-
prises contacting the metals to be degreased with the above
described stabilized methylene chloride compositions wherein the
'~; methylene chloride contains an admixture of stabilizing amounts
f 25 of diisopropylamine, N-methyl pyrolle, butylene oxide, propylene
oxide, methyl acetate, acetone, te~tiary amylene and optionally
methyl alcohol. In degreasing metals with the above described
preferred stabilized methylene chloride in the presence of an
aliphatic organic compound which reacts with metals, metal ~ -
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~0495~8
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halides and combinations thereo~ including aluminum, iron, zinc,
halides of said metals and combinations, there exists upon con-
tact of the metal with the stabilized methylene chloride a com-
position comprising me~hylene chloride, a stabilizing amount of
from aboutO.OOl to about 2.0 weight percent of the methylene
chloride of each of diisopropylamine, N-methyl pyrolle, butylene
oxide, propylene oxide, methyl acetate, acetone, tertiary amylene
and optionally methyl alcohol and an aliphatic organic compound
. ~
which reacts with said metals, metal halides and combinations.
The metals,metal halides and combinations may be present from
any source such as chloride ~ormed by drilling or other machining
o~ aluminum or aluminum-containing materials with various working
fluids such as cuttin~ oils, lubricants and the like, or aluminum
c~loride may be present ~rom the reaction of methylene chloride
1~ with aluminum. The degradation of methylene chloride in the -~
presence of aliphatic organic compounds such as trans-dichloro-
ethylene, carbon tetrachloride and l,l,l-trichloroethane, metals, -
metal halides and combinations may be inhibited by admixingme~-Y~
' chloride with the above noted quantities of diisopropylamine,
N-methyl pyrolle, butylene oxide, propylene oxide, methyl acetate,
acetone 9 tertiary amylenes and optionally methyl alcohol.
In order that those skilled in the art ma~ readily understand the
present invention and certain specific embodiments by which it may be carried
into e~ect the foll~ing illustrative examples are presented.
In Examples 1 to 4, inclusive, an aluminum reflux stability test was
- carried out by placing 190 ml o~ substantially water free methylene chloride ~ -~
containing 5 Vol. % of a commercially a~ailable l,l,l-trichloroethane and the
same solvent system containing the stabilizin~ coDosition of this in~ention.
In Examples 3 and 4, respectively, anhydrous aluminum chloride and anhydrous
3 ferric chloride were added to the solvent system in a flat bottom 300 ml
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~1~4956~
boiling flask fitted with a condenser. About 1.0 gram of 20 mesh granular
aluminum ~as placed in the liquid in the ~lask and an all~inum coupon about
1- x 6 cm was suspended in the condenser. During the extended period o~ rerlu~
the sol~ent vapor surrounded, condensed, and dripped ~rom the suspended strip.
- In all cases the pH and alkalinity content, as ~aOH, trere determined after the
system was refluxed for varying time periods noted, The results of the various
tests are sh~ m in Table I bel~w. ~ - ~
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In Exa~ple l deterioration of the solvent system occurred due to the
reaction of aluminum with the contained l,l,l-trichloroethane. In F~ample 2 the
addition of the stabilizing compos-ition of this invention to this solvent system
prevented such deterioration and in Example 3 even after about O.O~ grams
anhydrous aluminum chloride was added and the system refluxed an additional day,
In E~ample ~ even with the further addition of about 0.04 grams anhydrous ferric
chloride and an additional seven days of refluxing no corrosion of the aluminum
in the flask or the condenser was observed.
The inhibition of the degradation of methylene chloride by the
reaction between 1,1,1-trichloroethane and aluNin~lm and metal salts by the
stabilizing composition of this invention is especially surprising and
unexpected when it is realized that the stabilizers included in the commercial
vapor degreasing grade l,l,l-trichloroethane to prevent reaction of the l,l,l-
trichloroethane with metals and/or metal salts in the presence of chlorinated
15 solvents failed to inhibit the degradation of the methylene chloride. Only ~-
when the stabilizing composition of this invention was admixed ~7ith the methylene
chloride containin~ the stabilized l,l,l-trichloroethane was degradation of the ;
methylene chloride prevented.
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~04956~ .
In Table II hydrolytic stability tests were made by
placing 150 ml. of methylene chloride in Example 5 and 150 ml.
of methylene chloride containing the stabilizing composition
specified in Example 6 into a 300 ml. boiling flask. The
flask was fitted with a Soxhlet extractor equipped with a
syphon break and a condenser vented to room air. Fifty
milliliters of the solvent of each Example were first intro- -
duced into the Soxhlet and -50 ml. of water was then added.
One gram of 20 mesh granular aluminum, about one gram of 30
mesh granular zinc and about 0.1 g of iron powder were placed
in the flask. A 2 x 7 cm. zinc coupon of known weight was
positioned in the Soxhlet and a 2 x 7 cm. weighed steel
,.. . .
coupon was mounted in the condenser. The contents of the
flask were refluxed for the period of time specified by ~;
heating the boiling flask with an electric heater. At the
end of the reflux period the pH and alkalinity, as NaOH, of
the solvent contents of the Soxhlet and of the flask were
determined from a portion of the aqueous phase obtained by
extraction of the solvent with an equal volume of neutral
distilled water after the solvent system had been refluxed
for the time specified. The zinc and iron coupons were
cIeaned of any accumulated corrosion products, weighed and
the difference in initial and final weight recorded as weight
loss.
The results are shown below in Table II.
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The superiority of the stabilizing composition of this
invention is evident from a comparison of the results of
Example 6, the composition of the present invention, and
Example 5, a stabilizing composition of known good stabilizing
characteristics formulated by the applicant herein. Much less
corrosion of the zinc coupon in the Soxhlet and the iron
coupon located in the condenser occurred in the use of the
composition of this invention during the 15 day reflux period.
In Examples 7 and 8 of Table III reflux stability tests
were conducted by following Federal Specification O-T-236b
modified by the use of 200 ml. of the solvent system in place
of 100 ml. and by positioning a 6-watt untraviolet lamp about
one inch from the vapor tube of the Soxhlet extractor. A
300 ml. boiling flash was fitted with a Soxhlet extractor, a
condenser connected to the extractor, about 1.0 gram of
granular zinc and about 0.5 ml. of water was added to the
flask and a 2 x 7 cm. zinc coupon was inserted in the extractor
and the condenser. The condenser was vented to a wat~r
scrubber.
The results of the tests are presented in Table III.
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~49568
Storage stability tests of stabilized methylene
chloride carried out in Examples 9 to 11 of Table 4. About
250 ml each of three stabilized methylene ~hloride compositions
specified in the Examples was placed in a pint bottle contain~
ing three 1/16" diameter x 5" rusty steel rods and two 1/2" x
6" x 0.003" gauge rusty steel coupons. About 1.32 ml. (0.4 wt.~)
of distilled water was added and the entire contents of the
bottle thoroughly agitated at the start of the test period.
In Example 9 an additional 0.4 wt.~ was added to the bottle
after one dayO The capped bottles were permitted to stand
for five days after which visual observations of the steel
coupons, the solvent and the surface of the solvent were
made and recorded. The bottles were then uncapped and any
detectable objectionable odor noted.
The results of the tests are included in Table IV.
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The superiority of the composition of th.is invention
in stabilizing methylene chloride on exposure to water and
rusty steel storage conditions is evidenced by the results
of Example ll as compared to the results of the tests in
Examples 9 and lO in which two different stabilizing compo-
sitions known in the art were used. In Example ll no uncharac-
teristic odor was detected but both Examples 9 and lO had an
objectionable putrid odor.
Although the present invention has been described with
detailed reference to specific embodiments thereof, it is
not intended to be so limited since modifications and alter-
ations may be made therein which are with1n the complete
intended scope of this invention as defined by the appended
claims.
-17-
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