CA2159770A1 - Azeotropes of octamethyltrisiloxane and aliphatic or alicyclic alcohols - Google Patents
Azeotropes of octamethyltrisiloxane and aliphatic or alicyclic alcoholsInfo
- Publication number
- CA2159770A1 CA2159770A1 CA002159770A CA2159770A CA2159770A1 CA 2159770 A1 CA2159770 A1 CA 2159770A1 CA 002159770 A CA002159770 A CA 002159770A CA 2159770 A CA2159770 A CA 2159770A CA 2159770 A1 CA2159770 A1 CA 2159770A1
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- Canada
- Prior art keywords
- weight
- composition
- azeotrope
- octamethyltrisiloxane
- compositions
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Abandoned
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Classifications
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11D—DETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
- C11D7/00—Compositions of detergents based essentially on non-surface-active compounds
- C11D7/50—Solvents
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- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23G—CLEANING OR DE-GREASING OF METALLIC MATERIAL BY CHEMICAL METHODS OTHER THAN ELECTROLYSIS
- C23G5/00—Cleaning or de-greasing metallic material by other methods; Apparatus for cleaning or de-greasing metallic material with organic solvents
- C23G5/02—Cleaning or de-greasing metallic material by other methods; Apparatus for cleaning or de-greasing metallic material with organic solvents using organic solvents
- C23G5/032—Cleaning or de-greasing metallic material by other methods; Apparatus for cleaning or de-greasing metallic material with organic solvents using organic solvents containing oxygen-containing compounds
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- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11D—DETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
- C11D7/00—Compositions of detergents based essentially on non-surface-active compounds
- C11D7/50—Solvents
- C11D7/5031—Azeotropic mixtures of non-halogenated solvents
Abstract
Binary azeotropic and azeotrope-like compositions contain 1-heptanol, cyclohexanol or 4-methylcyclohexanol, with octamethyltrisiloxane and the compositions are useful for cleaning, rinsing or drying.
Description
AZEOTROPES OF OCTAMETHYLTRISILOXANE AND ALIPHATIC OR
ALICYCLIC ALCOHOLS
This invention is directed to environmentally friendly solvents, and particularly to cleaning, rinsing and drying agents which are binary azeotropic or azeotrope-like compositions cont~;n;ng a volatile methyl siloxane (VMS).
Since local, federal and international regulations have restricted the use of some chemicals, a search is on for replacement solvents. VMS have been found to be one suitable substitute. The Environmental Protection Agency (EPA) has determined that VMS such as octamethylcyclo-tetrasiloxane, decamethylcyclopentasiloxane, dodecamethyl-cyclohexasiloxane, hexamethyldisiloxane, octamethyltri-siloxane and decamethyltetrasiloxane are acceptable substitutes for CFC-113, the chlorofluorocarbon (C2Cl3F3) and methylchloroform (MCF). This is limited to closed systems for metal cleaning, electronic cleaning and precision cleaning applications, under their Significant New Alternatives Policy (SNAP).
In addition, EPA has exempted VMS as a volatile organic compound ~VOC) [40 CFR 51.100(s)] on the basis that VMS have negligible contribution to tropospheric ozone formation. The exemption of VMS from regulation as ozone precursors contributes to the achievement of several important environmental goals and allows their use as a substitute for several compounds previously listed as hazardous air pollutants (HAP). This meets the need to develop substitutes for ozone depleting substances (ODS) and also attains National Ambient Air Quality Standards for ozone under Title I of the Clean Air Act.
Compounds designated VMS by EPA exemption are cyclic, branched or linear, "completely methylated"
siloxanes. The term "completely methylated" means that methyl groups, and no other functional groups, are attached to the central backbone of the siloxane.
VMS have an atmospheric lifetime of 10-30 days and do not contribute significantly to global warming. Due to these short atmospheric lifetimes, they do not rise and accumulate in the stratosphere. VMS contain no chlorine or bromine atoms; they do not attack the ozone layer; they do not contribute to tropospheric ozone formation (smog); and they have m; n; r-l global warming potential. VMS are unique in simultaneously possessing these attributes and they provide one positive solution to the problem of finding new solvent replacements.
The invention relates to new binary azeotropic compositions contAining a volatile methyl siloxane and an aliphatic or alicyclic alcohol. Azeotrope-like compositions were also discovered. These azeotropic or azeotrope-like compositions have utility as environmentally friendly cleaning, rinsing and drying agents.
As cleaning agents, our compositions are used to remove contaminants from any surface, but especially in defluxing and precision cleaning, low-pressure vapor degreasing and vapor phase cleaning. These compositions exhibit unexpected advantages in their enhanced solvency power, and the maintenance of a constant solvency power following evaporation, which occur during applications involving vapor phase cleaning, distillation regeneration and wipe cleaning.
Because our cleaning agent is an azeotropic or azeotrope-like composition, it has another advantage in being easily recovered and recirculated. Thus, our composition is separated as a single substance from a contaminated cleaning bath after its use in the cleaning 21~9770 process. By simple distillation, its regeneration is facilitated so that it is freshly recirculated.
In addition, these compositions provide the unexpected benefit of being higher in siloxane fluid content, and correspondingly lower in alcohol content, than azeotropes of siloxane fluids and low molecular weight alcohols such as ethanol. The surprising result is that our compositions are less inclined to generate tropospheric ozone and smog. Another surprising result is that these compositions possess an enhanced solvency power compared to VMS itself. Yet, the compositions exhibit a mild solvency power making them useful for cleaning delicate surfaces without harm.
An azeotrope is a mixture of two or more liquids, the composition of which does not change upon distillation.
Thus, a mixture of 95% ethanol and 5% water boils at a lower temperature (78.15C.) than pure ethanol (78.3C.) or pure water (100C.). Such liquid mixtures behave like a single substance in that the vapor produced by partial evaporation of liquid has the same composition as the liquid. Thus, the mixtures distill at a constant temperature without change in composition and cannot be separated by normal distillation.
Azeotropes exist in systems containing two liquids (A and B) as binary azeotropes, three liquids (A, B and C) as ternary azeotropes and four liquids (A, B, C and D) as quaternary azeotropes. However, azeotropism is an unpredictable phenomenon and each azeotropic or azeotrope-like composition must be discovered. The unpredictability of azeotrope formation is well documented in US Patents 3085065, 4155865, 4157976, 4994202 and 5064560. One of ordinary skill in the art cannot predict or expect azeotrope formation, even among positional or constitutional isomers (i.e. butyl, isobutyl, sec-butyl and tert-butyl).
For purposes of our invention, a mixture of two or more components is azeotropic if it vaporizes with no change in the composition of the vapor from the liquid.
Specifically, an azeotropic composition includes mixtures that boil without changing composition and mixtures that evaporate at a temperature below their boiling point without changing composition. Accordingly, an azeotropic composition may include mixtures of two components over a range of proportions where each specific proportion of the two components is azeotropic at a certain temperature but not necessarily at other temperatures.
Azeotropes vaporize with no change in composition.
If the applied pressure is above the vapor pressure of the azeotrope, it evaporates without change. If the applied pressure is below the vapor pressure of the azeotrope, it boils or distills without change. The vapor pressure of low boiling azeotropes is higher and the boiling point is lower, than the individual components. In fact, the azeotropic composition has the lowest boiling point of any composition of its components. Thus, an azeotrope is obtained by distillation of a mixture whose composition initially departs from that of the azeotrope.
Since only certain combinations of components form azeotropes, the formation of an azeotrope cannot be found without experimental vapor-liquid-equilibria (VLE) data, that i6 vapor and liquid composition6 at constant total pressure or temperature, for various mixtures of the components. The composition of some azeotropes is invariant to temperature, but in many cases the azeotropic compo~ition shifts with temperature. As a function of temperature, the azeotropic composition is determined from high quality VLE
data at a given temperature. Commercial software such as the ASPENPLUS~ program of Aspen Technology, Inc., Cambridge, Massachusetts, is available to make such determinations.
Given experimental data, programs such as ASPENPLUS~ can calculate parameters from which complete tables of composition and vapor pressure may be generated. This allows one to determine where an azeotropic composition is located.
The art also recognizes the existence of azeotrope-like compositions. For purposes of our invention, "azeotrope-like" means a composition that behaves like an azeotrope. Thus, azeotrope-like compositions have constant boiling characteristics or have a tendency not to fractionate upon boiling or evaporation. In an azeotrope-like mixture, the composition of the vapor formed during boiling or evaporation is identical or substantially identical to the composition of the original liquid. During boiling or evaporation, the liquid changes only m;n;m~lly or to a negligible extent if it changes at all. In other words, it has about the same composition in vapor phase as in liquid phase when employed at reflux. In contrast, the liquid composition of non-azeotrope-like mixtures change to a substantial degree during boiling or evaporation.
Azeotrope-like compositions include all ratios of the azeotropic components boiling within one C. of the r;n;rum boiling point at 760 Torr (101.1 kPa).
One component of our azeotropic and azeotrope-like composition is octamethyltrisiloxane ~CH3)3Sio(CH3)2SioSi(CH3)3. It has a viscosity of one centistoke (mm2/s) at 25C. and i8 often referred to as "MDM" because it contains one difunctional "D" unit (CH3 )2SiO2/2 and two monofunctional "M" units ( CH3)3SiOl/2 shown below.
CH3 - Si - O - Si - - Si - CH3 MDM is a clear fluid, essentially odorless, nontoxic, nongreasy, nonstinging and nonirritating to skin.
It leaves no residue after 30 minutes at room temperature (20-25C./68-77F.) when one gram is placed at the center of No. 1 circular filter paper (diameter 185 mm supported at its perimeter in open room atmosphere).
The other component of our azeotropic and azeotrope-like composition is an aliphatic or alicyclic alcohol. The aliphatic alcohol is l-heptanol CH3 (CH2)5CH2OH. One alicyclic alcohol is cyclohexanol, C6HllOH. The other alicyclic alcohol is 4-methylcyclo-hexanol, CH3C6HloOHI as a mixture of its "cis" and "trans"
forms. The boiling points of these liquids in C measured at standard barometric pressure (101. 3 kPa/760 mm Hg) are 152.6 for MDM; 176.6 for l-heptanol; 161 for cyclo-hexanol and 171 for 4-methylcyclohexanol.
New binary azeotropic compositions were discovered contA;n;ng (i) 2-9% by weight of l-heptanol and 91-98% by weight of octamethyltrisiloxane; (ii) 2-26% by weight of cyclohexanol and 74-98% by weight of octamethyltrisiloxane;
and (iii) 1-12% by weight of 4-methylcyclohexanol and 88-99%
by weight of octamethyltrisiloxane. These compositions were homogeneous and had a single liquid phase at the azeotropic temperature or at room temperature. Homogeneous azeotropes are more de6irable than heterogeneous azeotropes r especially - 21~9 770 for cleaning, because homogeneous azeotropes exist as one liquid phase instead of two. In contrast, each phase of a heterogeneous azeotrope differs in cleaning power.
Therefore, cleaning performance of a heterogeneous azeotrope is difficult to reproduce because it depends on consistent mixing of the phases. Single phase (homogeneous) azeotropes are also more useful than multi-phase (heterogeneous) azeotropes since they can be transferred between locations with facility.
Each homogeneous azeotrope we discovered existed over a particular temperature range. Within that range, the azeotropic composition shifted with temperature.
Compositions containing the three alcohols were azeotropic within the range of 75-162.4C. inclusive.
Example I
We used a single-plate distillation apparatus for measuring vapor-liquid equilibria. The liquid mixture was boiled and the vapor was condensed in a small receiver. The receiver had an overflow path for recirculation to the boiling liquid. When equilibrium was established, samples of boiling liquid and condensed vapor were separately removed and quantitatively analyzed by gas chromatography (GC). The temperature, ambient pressure and liquid-vapor compositions, were measured at several different initial composition points. This data was used to determine if an azeotropic or azeotrope-like composition existed. The composition at different temperatures was determined using the data with the ASPENPLUS~ software program which performed the quantitative determinations. Our new azeotropic compositions are shown in Tables I-III. In the tables, "MDM" is weight percent of octamethyltrisiloxane in the azeotrope. Vapor pressure (VP) is Torr pressure units - 21~9770 where one Torr is 0.133 kPa (1 mm Hg). Accuracy in determining these compositions was + 2% by weight.
TABLE I
ALCOHOL TEMPERATURE C VP (Torr) WEIGHT % MDM
1-heptanol 162.4 1000 91 152.1 760 93 135 360.2 98 TABLE II
ALCOHOL TEMPERATURE C VP (Torr) WEIGHT % MDM
cyclohexanol 156.6 1000 74 125 380.6 81 100 154.6 89 54.9 98 TABLE III
ALCOHOL TEMPERATURE C VP (Torr) WEIGHT % MDM
4-methylcyclohexanol 161.9 1000 88 151.9 760 91 125 345.8 99 These tables show that at different temperatures, the composition of a given azeotrope varies. Thus, an azeotrope represents a variable composition which depends on temperature.
We also discovered azeotrope-like compositions contA;n;ng octamethyltrisiloxane and 1-heptanol, cyclohexanol or 4-methyl-cyclohexanol. Azeotrope-like compositions of octamethyltrisiloxane and 1-heptanol were found at 760 Torr (101.1 kPa) vapor pressure for all ratios of the components, where the weight percent of 1-heptanol varied between 1-22% and the weight percent of octamethyl-trisiloxane varied between 78-99%. These azeotrope-like compositions had a normal boiling point (at 760 Torr) that was within one C. of 152.1C., which is the normal boiling point of the azeotrope itself.
Azeotrope-like compositions of octamethyltri-siloxane and cyclohexanol were found at 760 Torr (101.1 kPa) vapor pressure for all ratios of the components, where the weight percent of cyclohexanol varied between 11-46% and the weight percent of octamethyltrisiloxane varied between 54-89%. These azeotrope-like compositions had a normal boiling point that was within one C. of 147C., which is the normal boiling point of the azeotrope itself.
Azeotrope-like compositions of octamethyltri-siloxane and 4-methylcyclohexanol were found at 760 Torr (101.1 kPa) vapor pressure for all ratios of the components, where the weight percent of 4-methylcyclohexanol varied between 1-26% and the weight percent of octamethyltri-siloxane varied between 74-99%. These azeotrope-like compositions had a normal boiling point that was within one C. of 151.9C., which is the normal boiling point of the azeotrope itself.
The procedure for determining these azeotrope-like compositions was the same as for the azeotropic compositions of Example I. The azeotrope-like compositions were homogeneous and have the same utility as their azeotropic compositions.
An especially useful application of our azeotropic or azeotrope-like compositions is cleaning and removing fluxes used in mounting and soldering electronic parts on printed circuit boards. Solder i8 often used in making mechanical, electro-mechanical or electronic connections.
In making electronic connections, components are attached to 21~9770 conductor paths of printed wiring assemblies by wave, reflow or manual soldering. The solder is usually a tin-lead alloy used with a rosin-baæed flux. Rosin is a complex mixture of isomeric acids, principally abietic acid and rosin fluxes often contain activators such as amine hydro-halides and organic acids. The flux (i) reacts with and removes surface compounds such as oxides, (ii) reduces the surface tension of the molten solder alloy, and (iii) prevents oxidation during the heating cycle by providing a surface blanket to the base metal and solder alloy. After the soldering operation, it is u6ually necessary to clean the assembly.
The compositions of our invention are also useful as cleaners. They remove corrosive flux residues formed on areas unprotected by the flux during soldering, or residues which could cause malfunctioning and short circuiting of electronic assemblies. In this application, our compositions are used as cold cleaners, vapor degreasers or ultrasonically. The compositions can also be used to remove carbonaceous materials from the surface of these and other industrial articles. By "carbonaceous material", it is meant any carbon containing compound, or mixture of carbon containing compounds, soluble in common organic solvents such as hexane, toluene or 1,1,1-trichloroethane.
We used four azeotropic compositions for cleaning a rosin-based solder flux as soil. Cleaning tests were conducted at 22C in an open bath with no distillation recycle of the composition. The four composition6 contained 7% of 1-heptanol, 9% of 4-methylcyclohexanol, 11% of cyclohexanol and 26% of cyclohexanol. The compositions removed flux although they were not equally effective. This is further illustrated in the following example.
Example II
We used an activated rosin-based solder flux commonly used for electrical and electronic assemblies. It was RESTER~ No. 1544, a product of Kester Solder Division-Litton Industries, Des Plaines, Illinois. Its approximate composition is 50% by weight of modified rosin, 25% by weight of ethanol, 25% by weight of 2-butanol and 1% by weight of proprietary activator. The rosin flux was mixed with 0.05% by weight of nonreactive, low viscosity silicone-glycol flow-out additive. A uniform thin layer of the mixture was applied to a 2" x 3" (5.1 X 7.6 cm) area of an Aluminum Q panel and spread out evenly with the edge of a spatula. The coating was allowed to dry at room temperature and cured at 100C for 10 minutes in an air oven. The panel was placed in a large, magnetically-stirred beaker filled one-third with azeotrope. Cleaning was conducted while rapidly stirring at room temperature even when cleaning with higher temperature azeotropes. The panel was removed at timed intervals, dried at room temperature, weighed and re-immersed for additional cleaning. The initial coating weight and weight loss were measured as functions of cumulative cleaning time and shown in Table IV.
In Table IV, l-heptanol is "HEPTANOL"; cyclohexanol is "CYCLOHEX"; and 4-methylcyclohexanol is "4-METHYL".
"WT%" is weight percent of alcohol. "TEMP" is azeotropic temperature in C. "WT" is initial weight of the coating in grams. "Time" is cumulative time after 1, 5, 10 and 30 minutes. Composition No. 5 is a CONTROL of 100% by weight octamethyltrisiloxane used for comparison. Table IV shows that our azeotropic compositions 1-4 were more effective cleaners than CONTROL No. 5.
` - 2159770 TABLE IV
CLEANING EXTENT AT ROOM TEMPERATURE (22C.) No. WT% LIOUIDS TEMP _ % REMOVED ( Time-min) 1 7% HEPTANOL 152.1 0.3104-2.1 77.7 87.0 94.4 211% CYCLOHEX 100.0 0.313213.186.4 90.7 94.1 326% CYCLOHEX 156.6 0.324619.895.9 99.3 100.0 4 9% 4-METHYL 151.8 0.3258-1.1 40.7 80.7 90.7 5 0% 100% MDM ----- 0.32600.0 2.8 7.0 21.0 Our azeotropic and azeotrope-like compositions have several advantages for cleaning, rinsing or drying. They are regenerated by distillation so performance of the cleaning mixture is restored after periods of use. Other performance factors affected by the compositions are bath life, cleaning speed, lack of flammability when one component is non-flammable and lack of damage to sensitive parts. In vapor phase degreasing, our compositions are restored by continuous distillation at atmospheric or reduced pressure and continually recycled. In such applications, cleaning or rinsing are conducted at the boiling point by plunging the part into the boiling liquid or allowing the refluxing vapor to condense on the cold part. Alternatively, the part is immersed in a cooler bath continually fed with fresh condensate, while dirty overflow liquid is returned to a sump. In the later case, the part is cleaned in a continually renewed liquid with mA~;mum cleaning power.
When used in open systems, our compositions and their performance remain constant even though evaporative losses occur. Such systems are typically operated at room temperature as ambient cleaning baths or wipe-on-by-hand cleaners. Cleaning baths are also operated at elevated temperatures but below their boiling point; since cleaning, rinsing or drying often occur faster at elevated temperature and are desirable when the part being cleaned and equipment permit.
Our compositions are beneficial when used to rinse water displacement fluids from (i) mechanical and electrical parts such as gear boxes or electric motors and (ii) other articles made of metal, ceramic, glass and plastic, such as electronic and semiconductor parts; precision parts such as ball bearings; optical parts such as lenses, photographic or camera parts; and military or space hardware such as precision guidance equipment used in defense and aerospace industries. Our compositions are effective as a rinsing fluid, even though most water displacement fluids contain small amounts of one or more surfactants, and our compositions (i) more thoroughly remove residual surfactant on the part; (ii) reduce carry-over loss of rinse fluid; and (iii) increase the extent of water displacement.
Cleaning is conducted by using a given azeotropic or azeotrope-like composition at or near its azeotropic temperature or at some other temperature. It can be used alone,or combined with small amounts of one or more organic liquid additives capable of enhancing oxidative stability, corrosion inhibition or solvency. Oxidative stabilizers in amounts of 0.05-5% by weight inhibit slow oxidation of organic compounds such as alcohols. Corrosion inhibitors in amounts of 0.1-5% by weight prevent metal corrosion by traces of acids that may be present or slowly form in alcohols. Solvency enhancers in amounts of 1-10% by weight increase solvency power by adding a more powerful solvent.
These additives mitigate undesired effects of alcohol components of the azeotropic or azeotrope-like composition, since the alcohol is not as resistant to oxidative degradation as VMS. Numerous additives are suitable as the VMS is miscible with small amounts of many additives. The additive, however, must be one in which the resulting liquid mixture is homogeneous and single phased and one that does not significantly affect the azeotropic or azeotrope-like character of our composition.
Useful oxidative stabilizers are phenols such as trimethylphenol, cyclohexylphenol, thymol, 2,6-di-t-butyl-4-methylphenol, butylhydroxyanisole and isoeugenol; amines such as hexylamine, pentylamine, dipropylamine, diisopropyl-amine, diisobutylamine, triethylamine, tributylamine, pyridine, N-methylmorpholine, cyclohexylamine, 2,2,6,6-tetramethyl-piperidine and N,N'-diallyl-p-phenylenediamine;
and triazoles such as benzotriazole, 2-(2'-hydroxy-5'-methylphenyl)benzo-triazole and chlorobenzotriazole.
Useful corrosion inhibitors are acetylenic alcohols such as 3-methyl-1-butyn-3-ol or 3-methyl-1-pentyn-3-ol;
epoxides such as glycidol, methyl glycidyl ether, allyl glycidyl ether, phenyl glycidyl ether, 1,2-butylene oxide, cyclohexene oxide and epichlorohydrin; ethers such as dimethoxymethane, 1,2-dimethoxyethane, 1,4-dioxane and 1,3,5-trioxane; unsaturated hydrocarbons such as hexene, heptene, octene, 2,4,4-trimethyl-1-pentene, pentadiene, octadiene, cyclohexene and cyclopentene; olefin based alcohols such as allyl alcohol or l-butene-3-ol; and acrylic acid esters such as methyl acrylate, ethyl acrylate and butyl acrylate.
Useful solvency enhancers are hydrocarbons such as pentane, isopentane, hexane, isohexane and heptane;
-- 21$9770 nitroalkanes such as nitromethane, nitroethane and nitropropane; amines such as diethylamine, triethylamine, isopropylamine, butylamine and isobutylamine; alcohols such as methanol, ethanol, n-propyl alcohol, isopropyl alcohol, n-butanol and isobutanol; ethers such as methyl Cellosolve~, tetrahydrofuran and 1,4-dioxane; ketones such as acetone, methyl ethyl ketone and methyl butyl ketone; and esters such as ethyl acetate, propyl acetate and butyl acetate.
ALICYCLIC ALCOHOLS
This invention is directed to environmentally friendly solvents, and particularly to cleaning, rinsing and drying agents which are binary azeotropic or azeotrope-like compositions cont~;n;ng a volatile methyl siloxane (VMS).
Since local, federal and international regulations have restricted the use of some chemicals, a search is on for replacement solvents. VMS have been found to be one suitable substitute. The Environmental Protection Agency (EPA) has determined that VMS such as octamethylcyclo-tetrasiloxane, decamethylcyclopentasiloxane, dodecamethyl-cyclohexasiloxane, hexamethyldisiloxane, octamethyltri-siloxane and decamethyltetrasiloxane are acceptable substitutes for CFC-113, the chlorofluorocarbon (C2Cl3F3) and methylchloroform (MCF). This is limited to closed systems for metal cleaning, electronic cleaning and precision cleaning applications, under their Significant New Alternatives Policy (SNAP).
In addition, EPA has exempted VMS as a volatile organic compound ~VOC) [40 CFR 51.100(s)] on the basis that VMS have negligible contribution to tropospheric ozone formation. The exemption of VMS from regulation as ozone precursors contributes to the achievement of several important environmental goals and allows their use as a substitute for several compounds previously listed as hazardous air pollutants (HAP). This meets the need to develop substitutes for ozone depleting substances (ODS) and also attains National Ambient Air Quality Standards for ozone under Title I of the Clean Air Act.
Compounds designated VMS by EPA exemption are cyclic, branched or linear, "completely methylated"
siloxanes. The term "completely methylated" means that methyl groups, and no other functional groups, are attached to the central backbone of the siloxane.
VMS have an atmospheric lifetime of 10-30 days and do not contribute significantly to global warming. Due to these short atmospheric lifetimes, they do not rise and accumulate in the stratosphere. VMS contain no chlorine or bromine atoms; they do not attack the ozone layer; they do not contribute to tropospheric ozone formation (smog); and they have m; n; r-l global warming potential. VMS are unique in simultaneously possessing these attributes and they provide one positive solution to the problem of finding new solvent replacements.
The invention relates to new binary azeotropic compositions contAining a volatile methyl siloxane and an aliphatic or alicyclic alcohol. Azeotrope-like compositions were also discovered. These azeotropic or azeotrope-like compositions have utility as environmentally friendly cleaning, rinsing and drying agents.
As cleaning agents, our compositions are used to remove contaminants from any surface, but especially in defluxing and precision cleaning, low-pressure vapor degreasing and vapor phase cleaning. These compositions exhibit unexpected advantages in their enhanced solvency power, and the maintenance of a constant solvency power following evaporation, which occur during applications involving vapor phase cleaning, distillation regeneration and wipe cleaning.
Because our cleaning agent is an azeotropic or azeotrope-like composition, it has another advantage in being easily recovered and recirculated. Thus, our composition is separated as a single substance from a contaminated cleaning bath after its use in the cleaning 21~9770 process. By simple distillation, its regeneration is facilitated so that it is freshly recirculated.
In addition, these compositions provide the unexpected benefit of being higher in siloxane fluid content, and correspondingly lower in alcohol content, than azeotropes of siloxane fluids and low molecular weight alcohols such as ethanol. The surprising result is that our compositions are less inclined to generate tropospheric ozone and smog. Another surprising result is that these compositions possess an enhanced solvency power compared to VMS itself. Yet, the compositions exhibit a mild solvency power making them useful for cleaning delicate surfaces without harm.
An azeotrope is a mixture of two or more liquids, the composition of which does not change upon distillation.
Thus, a mixture of 95% ethanol and 5% water boils at a lower temperature (78.15C.) than pure ethanol (78.3C.) or pure water (100C.). Such liquid mixtures behave like a single substance in that the vapor produced by partial evaporation of liquid has the same composition as the liquid. Thus, the mixtures distill at a constant temperature without change in composition and cannot be separated by normal distillation.
Azeotropes exist in systems containing two liquids (A and B) as binary azeotropes, three liquids (A, B and C) as ternary azeotropes and four liquids (A, B, C and D) as quaternary azeotropes. However, azeotropism is an unpredictable phenomenon and each azeotropic or azeotrope-like composition must be discovered. The unpredictability of azeotrope formation is well documented in US Patents 3085065, 4155865, 4157976, 4994202 and 5064560. One of ordinary skill in the art cannot predict or expect azeotrope formation, even among positional or constitutional isomers (i.e. butyl, isobutyl, sec-butyl and tert-butyl).
For purposes of our invention, a mixture of two or more components is azeotropic if it vaporizes with no change in the composition of the vapor from the liquid.
Specifically, an azeotropic composition includes mixtures that boil without changing composition and mixtures that evaporate at a temperature below their boiling point without changing composition. Accordingly, an azeotropic composition may include mixtures of two components over a range of proportions where each specific proportion of the two components is azeotropic at a certain temperature but not necessarily at other temperatures.
Azeotropes vaporize with no change in composition.
If the applied pressure is above the vapor pressure of the azeotrope, it evaporates without change. If the applied pressure is below the vapor pressure of the azeotrope, it boils or distills without change. The vapor pressure of low boiling azeotropes is higher and the boiling point is lower, than the individual components. In fact, the azeotropic composition has the lowest boiling point of any composition of its components. Thus, an azeotrope is obtained by distillation of a mixture whose composition initially departs from that of the azeotrope.
Since only certain combinations of components form azeotropes, the formation of an azeotrope cannot be found without experimental vapor-liquid-equilibria (VLE) data, that i6 vapor and liquid composition6 at constant total pressure or temperature, for various mixtures of the components. The composition of some azeotropes is invariant to temperature, but in many cases the azeotropic compo~ition shifts with temperature. As a function of temperature, the azeotropic composition is determined from high quality VLE
data at a given temperature. Commercial software such as the ASPENPLUS~ program of Aspen Technology, Inc., Cambridge, Massachusetts, is available to make such determinations.
Given experimental data, programs such as ASPENPLUS~ can calculate parameters from which complete tables of composition and vapor pressure may be generated. This allows one to determine where an azeotropic composition is located.
The art also recognizes the existence of azeotrope-like compositions. For purposes of our invention, "azeotrope-like" means a composition that behaves like an azeotrope. Thus, azeotrope-like compositions have constant boiling characteristics or have a tendency not to fractionate upon boiling or evaporation. In an azeotrope-like mixture, the composition of the vapor formed during boiling or evaporation is identical or substantially identical to the composition of the original liquid. During boiling or evaporation, the liquid changes only m;n;m~lly or to a negligible extent if it changes at all. In other words, it has about the same composition in vapor phase as in liquid phase when employed at reflux. In contrast, the liquid composition of non-azeotrope-like mixtures change to a substantial degree during boiling or evaporation.
Azeotrope-like compositions include all ratios of the azeotropic components boiling within one C. of the r;n;rum boiling point at 760 Torr (101.1 kPa).
One component of our azeotropic and azeotrope-like composition is octamethyltrisiloxane ~CH3)3Sio(CH3)2SioSi(CH3)3. It has a viscosity of one centistoke (mm2/s) at 25C. and i8 often referred to as "MDM" because it contains one difunctional "D" unit (CH3 )2SiO2/2 and two monofunctional "M" units ( CH3)3SiOl/2 shown below.
CH3 - Si - O - Si - - Si - CH3 MDM is a clear fluid, essentially odorless, nontoxic, nongreasy, nonstinging and nonirritating to skin.
It leaves no residue after 30 minutes at room temperature (20-25C./68-77F.) when one gram is placed at the center of No. 1 circular filter paper (diameter 185 mm supported at its perimeter in open room atmosphere).
The other component of our azeotropic and azeotrope-like composition is an aliphatic or alicyclic alcohol. The aliphatic alcohol is l-heptanol CH3 (CH2)5CH2OH. One alicyclic alcohol is cyclohexanol, C6HllOH. The other alicyclic alcohol is 4-methylcyclo-hexanol, CH3C6HloOHI as a mixture of its "cis" and "trans"
forms. The boiling points of these liquids in C measured at standard barometric pressure (101. 3 kPa/760 mm Hg) are 152.6 for MDM; 176.6 for l-heptanol; 161 for cyclo-hexanol and 171 for 4-methylcyclohexanol.
New binary azeotropic compositions were discovered contA;n;ng (i) 2-9% by weight of l-heptanol and 91-98% by weight of octamethyltrisiloxane; (ii) 2-26% by weight of cyclohexanol and 74-98% by weight of octamethyltrisiloxane;
and (iii) 1-12% by weight of 4-methylcyclohexanol and 88-99%
by weight of octamethyltrisiloxane. These compositions were homogeneous and had a single liquid phase at the azeotropic temperature or at room temperature. Homogeneous azeotropes are more de6irable than heterogeneous azeotropes r especially - 21~9 770 for cleaning, because homogeneous azeotropes exist as one liquid phase instead of two. In contrast, each phase of a heterogeneous azeotrope differs in cleaning power.
Therefore, cleaning performance of a heterogeneous azeotrope is difficult to reproduce because it depends on consistent mixing of the phases. Single phase (homogeneous) azeotropes are also more useful than multi-phase (heterogeneous) azeotropes since they can be transferred between locations with facility.
Each homogeneous azeotrope we discovered existed over a particular temperature range. Within that range, the azeotropic composition shifted with temperature.
Compositions containing the three alcohols were azeotropic within the range of 75-162.4C. inclusive.
Example I
We used a single-plate distillation apparatus for measuring vapor-liquid equilibria. The liquid mixture was boiled and the vapor was condensed in a small receiver. The receiver had an overflow path for recirculation to the boiling liquid. When equilibrium was established, samples of boiling liquid and condensed vapor were separately removed and quantitatively analyzed by gas chromatography (GC). The temperature, ambient pressure and liquid-vapor compositions, were measured at several different initial composition points. This data was used to determine if an azeotropic or azeotrope-like composition existed. The composition at different temperatures was determined using the data with the ASPENPLUS~ software program which performed the quantitative determinations. Our new azeotropic compositions are shown in Tables I-III. In the tables, "MDM" is weight percent of octamethyltrisiloxane in the azeotrope. Vapor pressure (VP) is Torr pressure units - 21~9770 where one Torr is 0.133 kPa (1 mm Hg). Accuracy in determining these compositions was + 2% by weight.
TABLE I
ALCOHOL TEMPERATURE C VP (Torr) WEIGHT % MDM
1-heptanol 162.4 1000 91 152.1 760 93 135 360.2 98 TABLE II
ALCOHOL TEMPERATURE C VP (Torr) WEIGHT % MDM
cyclohexanol 156.6 1000 74 125 380.6 81 100 154.6 89 54.9 98 TABLE III
ALCOHOL TEMPERATURE C VP (Torr) WEIGHT % MDM
4-methylcyclohexanol 161.9 1000 88 151.9 760 91 125 345.8 99 These tables show that at different temperatures, the composition of a given azeotrope varies. Thus, an azeotrope represents a variable composition which depends on temperature.
We also discovered azeotrope-like compositions contA;n;ng octamethyltrisiloxane and 1-heptanol, cyclohexanol or 4-methyl-cyclohexanol. Azeotrope-like compositions of octamethyltrisiloxane and 1-heptanol were found at 760 Torr (101.1 kPa) vapor pressure for all ratios of the components, where the weight percent of 1-heptanol varied between 1-22% and the weight percent of octamethyl-trisiloxane varied between 78-99%. These azeotrope-like compositions had a normal boiling point (at 760 Torr) that was within one C. of 152.1C., which is the normal boiling point of the azeotrope itself.
Azeotrope-like compositions of octamethyltri-siloxane and cyclohexanol were found at 760 Torr (101.1 kPa) vapor pressure for all ratios of the components, where the weight percent of cyclohexanol varied between 11-46% and the weight percent of octamethyltrisiloxane varied between 54-89%. These azeotrope-like compositions had a normal boiling point that was within one C. of 147C., which is the normal boiling point of the azeotrope itself.
Azeotrope-like compositions of octamethyltri-siloxane and 4-methylcyclohexanol were found at 760 Torr (101.1 kPa) vapor pressure for all ratios of the components, where the weight percent of 4-methylcyclohexanol varied between 1-26% and the weight percent of octamethyltri-siloxane varied between 74-99%. These azeotrope-like compositions had a normal boiling point that was within one C. of 151.9C., which is the normal boiling point of the azeotrope itself.
The procedure for determining these azeotrope-like compositions was the same as for the azeotropic compositions of Example I. The azeotrope-like compositions were homogeneous and have the same utility as their azeotropic compositions.
An especially useful application of our azeotropic or azeotrope-like compositions is cleaning and removing fluxes used in mounting and soldering electronic parts on printed circuit boards. Solder i8 often used in making mechanical, electro-mechanical or electronic connections.
In making electronic connections, components are attached to 21~9770 conductor paths of printed wiring assemblies by wave, reflow or manual soldering. The solder is usually a tin-lead alloy used with a rosin-baæed flux. Rosin is a complex mixture of isomeric acids, principally abietic acid and rosin fluxes often contain activators such as amine hydro-halides and organic acids. The flux (i) reacts with and removes surface compounds such as oxides, (ii) reduces the surface tension of the molten solder alloy, and (iii) prevents oxidation during the heating cycle by providing a surface blanket to the base metal and solder alloy. After the soldering operation, it is u6ually necessary to clean the assembly.
The compositions of our invention are also useful as cleaners. They remove corrosive flux residues formed on areas unprotected by the flux during soldering, or residues which could cause malfunctioning and short circuiting of electronic assemblies. In this application, our compositions are used as cold cleaners, vapor degreasers or ultrasonically. The compositions can also be used to remove carbonaceous materials from the surface of these and other industrial articles. By "carbonaceous material", it is meant any carbon containing compound, or mixture of carbon containing compounds, soluble in common organic solvents such as hexane, toluene or 1,1,1-trichloroethane.
We used four azeotropic compositions for cleaning a rosin-based solder flux as soil. Cleaning tests were conducted at 22C in an open bath with no distillation recycle of the composition. The four composition6 contained 7% of 1-heptanol, 9% of 4-methylcyclohexanol, 11% of cyclohexanol and 26% of cyclohexanol. The compositions removed flux although they were not equally effective. This is further illustrated in the following example.
Example II
We used an activated rosin-based solder flux commonly used for electrical and electronic assemblies. It was RESTER~ No. 1544, a product of Kester Solder Division-Litton Industries, Des Plaines, Illinois. Its approximate composition is 50% by weight of modified rosin, 25% by weight of ethanol, 25% by weight of 2-butanol and 1% by weight of proprietary activator. The rosin flux was mixed with 0.05% by weight of nonreactive, low viscosity silicone-glycol flow-out additive. A uniform thin layer of the mixture was applied to a 2" x 3" (5.1 X 7.6 cm) area of an Aluminum Q panel and spread out evenly with the edge of a spatula. The coating was allowed to dry at room temperature and cured at 100C for 10 minutes in an air oven. The panel was placed in a large, magnetically-stirred beaker filled one-third with azeotrope. Cleaning was conducted while rapidly stirring at room temperature even when cleaning with higher temperature azeotropes. The panel was removed at timed intervals, dried at room temperature, weighed and re-immersed for additional cleaning. The initial coating weight and weight loss were measured as functions of cumulative cleaning time and shown in Table IV.
In Table IV, l-heptanol is "HEPTANOL"; cyclohexanol is "CYCLOHEX"; and 4-methylcyclohexanol is "4-METHYL".
"WT%" is weight percent of alcohol. "TEMP" is azeotropic temperature in C. "WT" is initial weight of the coating in grams. "Time" is cumulative time after 1, 5, 10 and 30 minutes. Composition No. 5 is a CONTROL of 100% by weight octamethyltrisiloxane used for comparison. Table IV shows that our azeotropic compositions 1-4 were more effective cleaners than CONTROL No. 5.
` - 2159770 TABLE IV
CLEANING EXTENT AT ROOM TEMPERATURE (22C.) No. WT% LIOUIDS TEMP _ % REMOVED ( Time-min) 1 7% HEPTANOL 152.1 0.3104-2.1 77.7 87.0 94.4 211% CYCLOHEX 100.0 0.313213.186.4 90.7 94.1 326% CYCLOHEX 156.6 0.324619.895.9 99.3 100.0 4 9% 4-METHYL 151.8 0.3258-1.1 40.7 80.7 90.7 5 0% 100% MDM ----- 0.32600.0 2.8 7.0 21.0 Our azeotropic and azeotrope-like compositions have several advantages for cleaning, rinsing or drying. They are regenerated by distillation so performance of the cleaning mixture is restored after periods of use. Other performance factors affected by the compositions are bath life, cleaning speed, lack of flammability when one component is non-flammable and lack of damage to sensitive parts. In vapor phase degreasing, our compositions are restored by continuous distillation at atmospheric or reduced pressure and continually recycled. In such applications, cleaning or rinsing are conducted at the boiling point by plunging the part into the boiling liquid or allowing the refluxing vapor to condense on the cold part. Alternatively, the part is immersed in a cooler bath continually fed with fresh condensate, while dirty overflow liquid is returned to a sump. In the later case, the part is cleaned in a continually renewed liquid with mA~;mum cleaning power.
When used in open systems, our compositions and their performance remain constant even though evaporative losses occur. Such systems are typically operated at room temperature as ambient cleaning baths or wipe-on-by-hand cleaners. Cleaning baths are also operated at elevated temperatures but below their boiling point; since cleaning, rinsing or drying often occur faster at elevated temperature and are desirable when the part being cleaned and equipment permit.
Our compositions are beneficial when used to rinse water displacement fluids from (i) mechanical and electrical parts such as gear boxes or electric motors and (ii) other articles made of metal, ceramic, glass and plastic, such as electronic and semiconductor parts; precision parts such as ball bearings; optical parts such as lenses, photographic or camera parts; and military or space hardware such as precision guidance equipment used in defense and aerospace industries. Our compositions are effective as a rinsing fluid, even though most water displacement fluids contain small amounts of one or more surfactants, and our compositions (i) more thoroughly remove residual surfactant on the part; (ii) reduce carry-over loss of rinse fluid; and (iii) increase the extent of water displacement.
Cleaning is conducted by using a given azeotropic or azeotrope-like composition at or near its azeotropic temperature or at some other temperature. It can be used alone,or combined with small amounts of one or more organic liquid additives capable of enhancing oxidative stability, corrosion inhibition or solvency. Oxidative stabilizers in amounts of 0.05-5% by weight inhibit slow oxidation of organic compounds such as alcohols. Corrosion inhibitors in amounts of 0.1-5% by weight prevent metal corrosion by traces of acids that may be present or slowly form in alcohols. Solvency enhancers in amounts of 1-10% by weight increase solvency power by adding a more powerful solvent.
These additives mitigate undesired effects of alcohol components of the azeotropic or azeotrope-like composition, since the alcohol is not as resistant to oxidative degradation as VMS. Numerous additives are suitable as the VMS is miscible with small amounts of many additives. The additive, however, must be one in which the resulting liquid mixture is homogeneous and single phased and one that does not significantly affect the azeotropic or azeotrope-like character of our composition.
Useful oxidative stabilizers are phenols such as trimethylphenol, cyclohexylphenol, thymol, 2,6-di-t-butyl-4-methylphenol, butylhydroxyanisole and isoeugenol; amines such as hexylamine, pentylamine, dipropylamine, diisopropyl-amine, diisobutylamine, triethylamine, tributylamine, pyridine, N-methylmorpholine, cyclohexylamine, 2,2,6,6-tetramethyl-piperidine and N,N'-diallyl-p-phenylenediamine;
and triazoles such as benzotriazole, 2-(2'-hydroxy-5'-methylphenyl)benzo-triazole and chlorobenzotriazole.
Useful corrosion inhibitors are acetylenic alcohols such as 3-methyl-1-butyn-3-ol or 3-methyl-1-pentyn-3-ol;
epoxides such as glycidol, methyl glycidyl ether, allyl glycidyl ether, phenyl glycidyl ether, 1,2-butylene oxide, cyclohexene oxide and epichlorohydrin; ethers such as dimethoxymethane, 1,2-dimethoxyethane, 1,4-dioxane and 1,3,5-trioxane; unsaturated hydrocarbons such as hexene, heptene, octene, 2,4,4-trimethyl-1-pentene, pentadiene, octadiene, cyclohexene and cyclopentene; olefin based alcohols such as allyl alcohol or l-butene-3-ol; and acrylic acid esters such as methyl acrylate, ethyl acrylate and butyl acrylate.
Useful solvency enhancers are hydrocarbons such as pentane, isopentane, hexane, isohexane and heptane;
-- 21$9770 nitroalkanes such as nitromethane, nitroethane and nitropropane; amines such as diethylamine, triethylamine, isopropylamine, butylamine and isobutylamine; alcohols such as methanol, ethanol, n-propyl alcohol, isopropyl alcohol, n-butanol and isobutanol; ethers such as methyl Cellosolve~, tetrahydrofuran and 1,4-dioxane; ketones such as acetone, methyl ethyl ketone and methyl butyl ketone; and esters such as ethyl acetate, propyl acetate and butyl acetate.
Claims (2)
1. A composition essentially consisting of (a) from 91-98% by weight of octamethyltrisiloxane and from 2-9%
by weight of 1-heptanol, wherein the composition is homogenous and azeotropic at a temperature within the range of 135-162.4°C. inclusive, wherein the composition has a vapor pressure of 47.9 kPa (360.2 Torr) at 135°C. when the composition consists essentially of 98% by weight of octamethyltrisiloxane and 2% by weight of 1-heptanol and wherein the composition has a vapor pressure of 133.3 kPa (1,000 Torr) at 162.4°C. when the composition essentially consists of 91% by weight of octamethyltrisiloxane and 9% by weight of 1-heptanol; or (b) from 78-99% by weight of octamethyl-trisiloxane and 1-22% by weight of 1-heptanol, wherein the composition is homogenous and azeotrope-like at a temperature within one degree of 152.1°C.; or (c) from 74-98% by weight of octamethyltrisiloxane and 2-26% by weight of cyclohexanol, wherein the composition is homogenous and azeotropic at a temperature within the range of 75-156.6°C.
inclusive, wherein the composition has a vapor pressure of 7.3 kPa (54.9 Torr) at 75°C. when the composition essentially consists of 98% by weight of octamethyltri-siloxane and 2% by weight of cyclohexanol and wherein the composition has a vapor pressure of 133.3 kPa (1,000 Torr) at 156.6°C. when the composition essentially consists of 74%
by weight of octamethyltrisiloxane and 26% by weight of cyclohexanol; or (d) from 54-89% by weight of octamethyltri-siloxane and 11-46% by weight of cyclohexanol, wherein the composition is homogenous and azeotrope-like at a temperature within one degree of 147°C.; or (e) from 88-99%
by weight of octamethyltrisiloxane and 1-12% by weight of 4-methylcyclohexanol, wherein the composition is homogenous and azeotropic at a temperature within the range of 125-161.9°C. inclusive, wherein the composition has a vapor pressure of 46.1 kPa (345.8 Torr) at 125°C. when the composition essentially consists of 99% by weight of octamethyltrisiloxane and 1% by weight of 4-methyl-cyclohexanol and wherein the composition has a vapor pressure of 133.3 kPa (1,000 Torr) at 161.9°C. when the composition essentiallly consists of 88% by weight of octamethyltrisiloxane and 12% by weight of 4-methylcyclohexanol; or (f) from 74-99% by weight of octamethyltrisiloxane and 1-26% by weight of 4-methylcyclo-hexanol, wherein the composition is homogenous and azeotrope-like at a temperature within one degree of 151.9°C.
by weight of 1-heptanol, wherein the composition is homogenous and azeotropic at a temperature within the range of 135-162.4°C. inclusive, wherein the composition has a vapor pressure of 47.9 kPa (360.2 Torr) at 135°C. when the composition consists essentially of 98% by weight of octamethyltrisiloxane and 2% by weight of 1-heptanol and wherein the composition has a vapor pressure of 133.3 kPa (1,000 Torr) at 162.4°C. when the composition essentially consists of 91% by weight of octamethyltrisiloxane and 9% by weight of 1-heptanol; or (b) from 78-99% by weight of octamethyl-trisiloxane and 1-22% by weight of 1-heptanol, wherein the composition is homogenous and azeotrope-like at a temperature within one degree of 152.1°C.; or (c) from 74-98% by weight of octamethyltrisiloxane and 2-26% by weight of cyclohexanol, wherein the composition is homogenous and azeotropic at a temperature within the range of 75-156.6°C.
inclusive, wherein the composition has a vapor pressure of 7.3 kPa (54.9 Torr) at 75°C. when the composition essentially consists of 98% by weight of octamethyltri-siloxane and 2% by weight of cyclohexanol and wherein the composition has a vapor pressure of 133.3 kPa (1,000 Torr) at 156.6°C. when the composition essentially consists of 74%
by weight of octamethyltrisiloxane and 26% by weight of cyclohexanol; or (d) from 54-89% by weight of octamethyltri-siloxane and 11-46% by weight of cyclohexanol, wherein the composition is homogenous and azeotrope-like at a temperature within one degree of 147°C.; or (e) from 88-99%
by weight of octamethyltrisiloxane and 1-12% by weight of 4-methylcyclohexanol, wherein the composition is homogenous and azeotropic at a temperature within the range of 125-161.9°C. inclusive, wherein the composition has a vapor pressure of 46.1 kPa (345.8 Torr) at 125°C. when the composition essentially consists of 99% by weight of octamethyltrisiloxane and 1% by weight of 4-methyl-cyclohexanol and wherein the composition has a vapor pressure of 133.3 kPa (1,000 Torr) at 161.9°C. when the composition essentiallly consists of 88% by weight of octamethyltrisiloxane and 12% by weight of 4-methylcyclohexanol; or (f) from 74-99% by weight of octamethyltrisiloxane and 1-26% by weight of 4-methylcyclo-hexanol, wherein the composition is homogenous and azeotrope-like at a temperature within one degree of 151.9°C.
2. A method of cleaning, rinsing or drying the surface of an article comprising applying to the surface of said article the azeotropic or azeotrope-like composition of claim 1.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US08/427,316 US5501811A (en) | 1995-04-24 | 1995-04-24 | Azeotropes of octamethyltrisiloxane and aliphatic or alicyclic alcohols |
| US08/427,316 | 1995-04-24 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CA2159770A1 true CA2159770A1 (en) | 1996-10-25 |
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ID=23694340
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CA002159770A Abandoned CA2159770A1 (en) | 1995-04-24 | 1995-10-03 | Azeotropes of octamethyltrisiloxane and aliphatic or alicyclic alcohols |
Country Status (7)
| Country | Link |
|---|---|
| US (2) | US5501811A (en) |
| EP (1) | EP0739998B1 (en) |
| JP (1) | JP3323713B2 (en) |
| KR (1) | KR19980025367A (en) |
| CA (1) | CA2159770A1 (en) |
| DE (1) | DE69514327T2 (en) |
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| JPH06248294A (en) * | 1992-12-29 | 1994-09-06 | Olympus Optical Co Ltd | Azeotropic and azeotrope-like composition and cleaning agent |
| JPH06202051A (en) * | 1992-12-29 | 1994-07-22 | Olympus Optical Co Ltd | Azeotropic and azeotropic-like composition and detergent |
| US5401429A (en) * | 1993-04-01 | 1995-03-28 | Minnesota Mining And Manufacturing Company | Azeotropic compositions containing perfluorinated cycloaminoether |
| US5494601A (en) * | 1993-04-01 | 1996-02-27 | Minnesota Mining And Manufacturing Company | Azeotropic compositions |
| JP3274737B2 (en) * | 1993-04-09 | 2002-04-15 | オリンパス光学工業株式会社 | Cleaning method and cleaning spray device |
| JPH06306390A (en) * | 1993-04-23 | 1994-11-01 | Olympus Optical Co Ltd | Azeotropic or azeotrope-like composition and detergent comprising same |
| JPH06306392A (en) * | 1993-04-23 | 1994-11-01 | Olympus Optical Co Ltd | Azeotropic or azeotrope-like composition and detergent comprising same |
| JPH06313196A (en) * | 1993-04-29 | 1994-11-08 | Olympus Optical Co Ltd | Azeotropic or azeotropelike composition and detergent |
| US5454970A (en) * | 1994-08-11 | 1995-10-03 | Dow Corning Corporation | Octamethyltrisiloxane containing azeotropes |
| US5454972A (en) * | 1994-09-15 | 1995-10-03 | Dow Corning Corporation | Azeotropes of octamethyltrisiloxane and n-propoxypropanol |
| US5456856A (en) * | 1995-01-18 | 1995-10-10 | Dow Corning Corporation | Azeotrope and azeotrope-like compositions of octamethyltrisiloxane |
-
1995
- 1995-04-24 US US08/427,316 patent/US5501811A/en not_active Expired - Fee Related
- 1995-08-10 US US08/513,466 patent/US5507878A/en not_active Expired - Fee Related
- 1995-09-23 TW TW084109936A patent/TW300917B/zh active
- 1995-10-03 CA CA002159770A patent/CA2159770A1/en not_active Abandoned
- 1995-10-13 KR KR1019950035249A patent/KR19980025367A/en not_active Application Discontinuation
- 1995-10-17 EP EP95307364A patent/EP0739998B1/en not_active Expired - Lifetime
- 1995-10-17 DE DE69514327T patent/DE69514327T2/en not_active Expired - Fee Related
- 1995-11-08 JP JP29013195A patent/JP3323713B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| EP0739998B1 (en) | 2000-01-05 |
| US5507878A (en) | 1996-04-16 |
| KR19980025367A (en) | 1998-07-06 |
| TW300917B (en) | 1997-03-21 |
| JPH08295899A (en) | 1996-11-12 |
| JP3323713B2 (en) | 2002-09-09 |
| DE69514327T2 (en) | 2000-05-18 |
| US5501811A (en) | 1996-03-26 |
| DE69514327D1 (en) | 2000-02-10 |
| MX9504324A (en) | 1998-07-31 |
| EP0739998A2 (en) | 1996-10-30 |
| EP0739998A3 (en) | 1997-03-05 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| EEER | Examination request | ||
| FZDE | Discontinued |