Octamethyltrisiloxane containing azeotropes

Abstract: Binary azeotropes of octamethyltrisiloxane (MDM) with certain alcohols and an ester and the use of the binary azeotropes as environmentally friendly cleaning agents are disclosed. The alcohol and ester components of the binary azeotrope are 2-methyl-1-pentanol, 1-hexanol, 1-butoxy-2-propanol and ethyl lactate.

Description: This invention is directed to an environmentally friendly cleaning agent which is a siloxane containing binary azeotrope. Because of regulations aimed at restricting the use of certain chemicals, the search for suitable replacements is an ever increasing dilemma faced by the chemical and industrial sectors. In the 1970s for instance, the US Environmental Protection Agency (EPA) named as "hazardous pollutants" sulfur dioxide SO 2 ; carbon monoxide CO; nitrogen dioxide NO 2 ; ozone O 3 ; suspended particulate with a diameter of ten micrometers or less PM 10 ; lead Pb; and nonmethane hydrocarbons (NMHC) now known as "volatile organic compounds" (VOC). The most abundant species of photochemical smog is ozone. Ozone precursors are VOC, nitric oxide NO and NO 2 . To reduce ozone in a polluted atmosphere, reductions in VOC and nitrogen oxide NO x (NO and NO 2 ) precursors has been required. Solar energy is absorbed by the surface of the earth and re-emitted as radiation. Certain gases in the atmosphere are capable of absorbing the re-emitted radiation and translating it into heat (THE GREENHOUSE EFFECT). The result is a higher atmospheric temperature (GLOBAL WARMING) than would be obtained in the absence of these "GREENHOUSE GASES". Accordingly, reductions in the emission of such gases has also been required, including carbon dioxide CO 2 , methane CH 4 , nitrous oxide N 2 O, ozone and a variety of chloro, fluoro and chlorofluorocarbons (CFC) such as methylchloroform CH 3 CCl 3 (MCF), carbon tetrachloride CCl 4 , C 2 HF 5 (HCFC-125), C 2 H 2 F 4 (HFC-134a) and chlorofluorocarbons such as CFCl 3 (CFC 11), CF 2 Cl 2 (CFC-12), C 2 ClF 5 (CFC-115), CHClF 2 (HCFC-22), C 2 HCl 2 F 3 (HCFC-123), C 2 HClF 4 (HCFC-124) and C 2 Cl 3 F 3 (CFC-113). Stratospheric ozone is a natural shield against the penetration of uv-light in the rays of the sun. There has been concern that any process which depletes stratospheric ozone will increase the amount of uv-B radiation (293-320 nanometers/2930-3200 angstroms) reaching the surface of the earth. Increased uv-B radiation may lead to the increased incidence of skin cancer. CFC's diffuse through the troposphere (up to 10 miles/16 kilometers) and into the mid-stratosphere (up to 30 miles/48 kilometers), where they are photolyzed by uv radiation and destroy ozone molecules. Because of STRATOSPHERIC OZONE DEPLETION, mandates such as the 1990 Clean Air Act Amendments contain a phaseout schedule for CFC's, halons (bromochlorofluorocarbons and bromofluorocarbons), carbon tetrachloride and methylchloroform. These are only a few of the problems faced by the chemical and industrial sectors in finding suitable replacements for such chemicals. Of particular interest however, is the VOC aspect of the problem and the provision of a suitable substitute material. The solution to this problem is an object of the present invention. Thus, "volatile organic compounds" (VOC) and "volatile organic material" (VOM) are defined in the United States by Federal statute and Title 40 CFR 51.100(s) to be any compound of carbon, excluding carbon monoxide, carbon dioxide, carbonic acid, metallic carbides or carbonates and ammonium carbonate, which participates in atmospheric photochemical reactions. The definition excludes certain compounds and classes of compounds as VOC or VOM. Scientifically, VOC has been defined as any compound of carbon that has a vapor pressure greater than 0.1 millimeters of mercury (13.3 Pa) at a temperature of twenty degrees Centigrade and a pressure of 760 millimeters mercury (101.3 kPa); or if the vapor pressure is unknown, a compound with less than twelve carbon atoms. "Volatile organic content" is the amount of volatile organic compounds (VOC) as determined according to EPA Test Method 24 or 24A, the procedures of which are set forth in detail in Title 40 CFR Part 60, Appendix A. Reduction of VOC has already been mandated in several states and regulations in California, for example, require less than 180 grams of volatile material per liter of any product which enters the atmosphere. This amount can be determined by baking ten grams of a product in an oven at 110°C. for one hour. The amount of solids which remain is subtracted from the total of the ten grams which was tested. Calculations are based on the weight of the volatile that have evaporated, and the amount is reported as grams per liter. The EPA has identified many volatile organic compounds (VOC) present in consumer products among which are such common solvents as ethanol, isopropyl alcohol, kerosene and propylene glycol; and common hydrocarbon solvents such as isobutane, butane, and propane, which are often employed as propellants in various aerosol sprays. The California Air Regulation Board (CARB) has proposed standards which would limit and reduce the amount of volatile organic compounds (VOC) permitted in various chemically formulated products used by household and institutional consumers. These regulations cover products such as detergents; cleaning compounds; polishes; floor products; cosmetics; personal care products; home, lawn and garden products; disinfectants; sanitizers; and automotive specialty products. These CARB standards would effect such widely used common consumer products as shaving lather, hair spray, shampoos, colognes, perfumes, aftershave lotions, deodorants, antiperspirants, suntan preparations, breath fresheners and room deodorants. Replacement of "outlawed" chemicals with certain volatile methyl siloxanes (VMS) as a solvent substitute is a viable approach. In fact, the EPA in Volume 59, No. 53, of the Federal Register , 13044-13161, (March 18, 1994), has indicated at Page 13091 that "Cyclic and linear volatile methyl siloxanes (VMSs) are currently undergoing investigation for use as substitutes for Class I compounds in metals, electronic and precision cleaning applications. Because of their chemical properties, these compounds show promise as substitutes for cleaning of precision guidance equipment in the defense and aerospace industries. In addition, the volatile methyl siloxanes have high purity and are therefore relatively easy to recover and recycle. In the cleaning system using VMSs, the fluids are used to clean parts in a closed header system using a totally enclosed process. The parts are drained and then dried using vacuum baking". At Pages 13093-13094, the EPA goes on to state that the "volatile methyl siloxanes dodecamethylcyclohexasiloxane, hexamethyldisiloxane, octamethyltrisiloxane and decamethyltetrasiloxane are acceptable substitutes for CFC-113 and MCF" for cleaning in closed systems, in the metals cleaning sector, the electronics cleaning sector and the precision cleaning sector; under the EPA Significant New Alternatives Policy (SNAP). At Page 13137, the EPA notes that with regard to the two volatile methyl siloxanes octamethylcyclotetrasiloxane and decamethylcyclopentasiloxane, the "Agency has completed review of data, and intends under separate rule-making to propose these chemicals as acceptable with the use condition that the company-set exposure limits must be met". In addition, a petition to the EPA filed in late 1992 is pending seeking exemption of these volatile methyl siloxanes (VMS) from regulation as VOC. The basis for the petition is that the volatile methyl siloxanes do not contribute to, and in some cases actually inhibit, the formation of tropospheric ozone. Thus, the volatile methyl siloxanes have a lower ozone formation potential than ethane, which is the most reactive compound on a list of "exempt" VOC. Furthermore, these volatile methyl siloxanes (VMS) have an atmospheric lifetime of between 10 to 30 days. Consequently, VMS compounds do not contribute significantly to global warming. Volatile methyl siloxanes have no potential to deplete stratospheric ozone due to their short atmospheric lifetimes so they will not rise and accumulate in the stratosphere. VMS compounds also contain no chlorine or bromine atoms. Volatile methyl siloxane compounds (VMS) neither attack the ozone layer nor do they contribute to tropospheric ozone formation (smog), and they have minimum GLOBAL WARMING potential. Volatile methyl siloxane compounds are hence unique in simultaneously possessing these three attributes. Thus, volatile methyl siloxanes may provide a viable solution to the problem of finding a suitable replacement for "outlawed" chemicals heretofore commonly used as cleaning agents. Our invention provides new binary azeotropes of a volatile methyl siloxane with certain alcohols and an ester. The invention also introduces the use of these new siloxane containing azeotropes as an environmentally friendly cleaning agent. As cleaning agents, the new azeotropes can be used to remove contaminants from any surface, but are particularly useful in applications related to defluxing and precision cleaning; low-pressure vapor degreasing and vapor phase cleaning. The unexpected advantages and benefits of these siloxane containing azeotropes as cleaning agents include enhanced solvency power, and the maintenance of a constant solvency power following evaporation, which may occur during applications involving vapor phase cleaning, distillative regeneration and wipe cleaning. Because our cleaning agent is an azeotrope, it possesses the added advantage and benefit of being more easily recovered and recirculated. Thus, the azeotrope can be separated from the contaminated cleaning bath effluent after its use in the cleaning process. By simple distillation, its regeneration is facilitated whereby it may be recirculated in the system as fresh cleaning agent influent. In addition, these azeotropes provide an unexpected advantage in being higher in siloxane fluid content and correspondingly lower in alcohol content, than azeotropes of siloxane fluids and lower molecular weight alcohols such as ethanol. The surprising result is that the azeotropes of the invention are less inclined to generate tropospheric ozone and smog. An azeotrope is a mixture of two or more liquids, the composition of which does not change upon distillation. For example, a mixture of 95% ethanol and 5% water boils at a lower temperature of 78.15°C., than either pure ethanol which boils at a temperature of 78.3°C., or pure water which boils at a temperature of 100°C. 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, these mixtures distill at a constant temperature without change in their composition and cannot be separated by normal distillation procedures. Azeotropes exist in systems containing two liquids (A and B) termed binary azeotropes, in systems containing three liquids (A, B, and C) termed ternary azeotropes and in systems containing four liquids (A, B, C, and D) termed quaternary azeotropes. The azeotropes of this invention are binary azeotropes. However, as is well known in the art, azeotropism is an "unpredictable phenomenon" and each azeotropic composition must be discovered. This phenomenon of "unpredictability" is documented in the prior art and U.S. Patent No. 4,157,976 (Column 1 lines 47-51) is one example. Reference may also be had to U.S. Patent 4,155,865 for further support. An azeotropic composition for use as a cleaning agent is described in JP-A-6093294, which composition comprises 35-36 wt% propylene glycol ethyl ether acetate and the balance of octamethyltrisiloxane. For this 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, azeotropic mixtures include both mixtures that boil without changing composition, and mixtures that evaporate at a temperature below the boiling point without changing composition. Accordingly, an azeotropic mixture 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 their composition. If the applied pressure is above the vapor pressure of the azeotrope, the azeotrope evaporates without change. If the applied pressure is below the vapor pressure of the azeotrope, the azeotrope boils or distills without change. The vapor pressure of low boiling azeotropes is higher and the boiling point is lower than that of the individual components. In fact, the azeotropic composition has the lowest boiling point of any composition of its components. Thus, the azeotrope can be obtained by distillation of a mixture whose composition initially departs from that of the azeotrope. Since only certain combinations of components can form azeotropes, the formation of an azeotrope cannot be reliably predicted without experimental vapor-liquid-equilibria (VLE) data, that is vapor and liquid compositions 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 composition shifts with temperature. The azeotropic composition as a function of temperature can be determined from high quality VLE data at a given temperature. Commercial software is available to make such determinations. The ASPENPLUS® program of Aspen Technology, Inc., of Cambridge, Massachusetts, is an example of such a program. Given experimental data, such programs can calculate parameters from which complete tables of composition and vapor pressure may be generated. This allows a user of the system to determine where an azeotropic composition is located. According to the present invention there is provided a composition comprising octamethyltrisiloxane and an alcohol or ester selected from 8-40 wt% 2-methyl-1-pentanol, 5-28 wt% 1-hexanol, 2-13 wt% 1-butoxy-2-propanol and 36-46 wt% ethyl lactate, wherein the composition is homogeneous and azeotropic at a temperature within the range of zero to 162°C inclusive. The volatile methyl siloxane used to form the azeotropes of the present invention, is the linear short chain siloxane fluid octamethyltrisiloxane, which has the formula (CH 3 ) 3 SiO(CH 3 ) 2 SiOSi(CH 3 ) 3 . Octamethyltrisiloxane has a viscosity of 1.0 centistoke (mm 2 /s) measured at 25°C. Octamethyltrisiloxane is sometimes abbreviated in the literature as "MDM", which indicates the presence in the molecule of one difunctional "D" unit (CH 3 ) 2 SiO 2/2 and two monofunctional "M" units (CH 3 ) 3 SiO 1/2 , shown below. Octamethyltrisiloxane (MDM) is a clear fluid, essentially odorless, nontoxic, nongreasy, nonstinging and it is nonirritating to skin. It will leave substantially no residue after thirty minutes at room temperature, when one gram of the fluid is placed at the center of No. 1 circular filter paper, with a diameter of 185 millimeters and supported at its perimeter in open room atmosphere. In U.S. Patent No. 5,478,493, we described azeotropes of hexamethyldisiloxane with three alcohols, namely, 3-methyl-3-pentanol, 2-pentanol and 1-methoxy-2-propanol. The binary azeotropes according to this invention also includes an alcohol. In addition, we have unexpectedly found new alcohols and an ester, which form azeotropes with octamethyltrisiloxane, instead of hexamethyldisiloxane. The alcohol or ester used in the present invention is selected from 2-methyl-1-pentanol which has the formula C 3 H 7 CH(CH 3 )CH 2 OH in an amount of 8-40 wt%; 1-hexanol (amyl carbinol) which has the formula CH 3 (CH 2 ) 4 CH 2 OH in an amount of 5-28 wt%; the alkoxy containing aliphatic alcohol 1-butoxy-2-propanol which has the formula C 4 H 9 OCH 2 CH(CH 3 )OH in an amount of 2-13 wt%, and ethyl lactate (2-hydroxypropanoic acid ethyl ester) which has the formula CH 3 CH(OH)COOC 2 H 5 in an amount of 36-46 wt%. The boiling points of each of the liquids in degrees Centigrade measured at the standard barometric pressure of 760 millimeters of mercury (101.3 kPa) are 152.6° for octamethyltrisiloxane; 148° for 2-methyl-1-pentanol; 157.2° for 1-hexanol; 170° for 1-butoxy-2-propanol; and 154° for ethyl lactate. An especially significant, surprising and unexpected result flowing from the use of the azeotropes of the invention is that they possess an enhanced solvency power in comparison to the use of octamethyltrisiloxane alone. Yet at the same time, the azeotropes exhibit a mild solvency power making them useful for cleaning delicate surfaces without doing harm to the surface being cleaned. The following examples are set forth for the purpose of illustrating the invention in more detail. New homogeneous binary azeotropes of octamethyltrisiloxane were discovered with three different alcohols and an ester. These azeotropes contained 8 to 40 percent by weight of 2-methyl-1-pentanol; 5 to 28 percent by weight of 1-hexanol; 2 to 13 percent by weight of 1-butoxy-2-propanol; and 36 to 46 percent by weight of ethyl lactate; respectively with octamethyltrisiloxane. The azeotropes were homogeneous in that they had a single liquid phase at both the azeotropic temperature and also at room temperature. Homogeneous azeotropes are more desirable than heterogeneous azeotropes, especially for cleaning applications, because homogeneous azeotropes exist as one liquid phase instead of two phases as the heterogeneous azeotrope. Each phase of a heterogeneous azeotrope differs in its cleaning power. Therefore, the cleaning performance of a heterogeneous azeotrope will be difficult to reproduce because it is dependent upon 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 more facility. Each homogeneous azeotrope was found to exist over a particular temperature range. Within that range, the azeotropic composition shifted somewhat with temperature. The compositions were azeotropic within the range of zero to 162°C. inclusive. Example I There was employed a single-plate distillation apparatus for measuring vapor-liquid equilibria. The liquid mixture was boiled and the vapor condensed into a small receiver which had an overflow path to recirculate back to the boiling liquid. When equilibrium was established, samples of the boiling liquid and of the condensed vapor were separately removed and quantitatively analyzed by gas chromatography (GC). The measured temperature, ambient pressure and the liquid and vapor compositions were obtained at several different initial compositional points. These data were used to determine whether an azeotropic composition existed. The azeotropic composition at different temperatures was determined by using the same data with the assistance of the ASPENPLUS® software program to perform the quantitative determinations. The azeotropic compositions are shown in Table I. In Table I, "MDM" is used to designate the weight percent in the azeotropic composition of octamethyltrisiloxane. The vapor pressure VP in Table I is shown in Torr pressure units (1 Torr = 0.133 kPa/1 mm Hg). The accuracy in determining the azeotropic compositions is approximately plus or minus about two weight percent. ALCOHOL/ESTER TEMPERATURE° C VP (Torr) WEIGHT % MDM 2-methyl-1-pentanol 148.3 1000 60 139.4 760 61 125 473.9 65 100 189.3 70 75 65.1 75 50 18.6 81 25 4.1 87 0 0.7 92 1-hexanol 153.2 1000 72 143.9 760 75 125 415.9 78 100 167.7 83 75 58.2 89 50 16.8 95 1-butoxy-2-propanol 162.3 1000 87 151.8 760 89 125 347.7 94 100 148.8 98 ethyl lactate 148.7 1000 61 139.4 760 63 125 486.3 63 100 205.7 64 75 76.1 64 50 23.8 63 25 6.0 59 0 1.1 54 The azeotropic compositions of the invention are particularly useful for cleaning precision articles made- of metal, ceramic, glass and plastic. Examples of such articles are electronic and semiconductor parts, electric and precision machinery parts such as ball bearings, optical parts and components such as lenses, photographic and camera parts and equipment, and military and space hardware such as precision guidance equipment used in the defense and aerospace industries. One especially useful application of our azeotropic compositions is the cleaning and removal of fluxes used in mounting and soldering electronic parts on printed circuit boards. For example, a solder is often used in making a mechanical, electromechanical or electronic connection. Thus, in making electronic connections, the components are attached to the conductor paths of a printed wiring assembly by wave soldering. The solder used is usually a tin-lead alloy, with the aid of a flux which is rosin based. Rosin is a complex mixture of isomeric acids principally abietic acid. These rosin fluxes often also contain activators such as amine hydrohalides and organic acids. The function of the flux is to react with and remove surface compounds such as oxides. It also reduces the surface tension of the molten solder alloy and prevents oxidation during the heating cycle by providing a surface blanket to the base metal and solder alloy. After the soldering operation, however, it is usually necessary to perform a final cleaning of the assembly. The azeotropic compositions of the invention are useful as a final cleaner. They remove any flux residues and oxides formed on areas unprotected by the flux during soldering which are corrosive or would cause malfunctioning or short circuiting of electronic assemblies. In such applications, the azeotropic compositions can be used as cold cleaners, vapor degreasers or accompanied with ultrasonic energy. The azeotropic compositions of this invention can also be used to remove carbonaceous materials from the surface of the above types of articles, as well as from the surface of various other industrial articles. Exemplary of carbonaceous materials are any carbon containing compound or mixtures of carbon containing compounds which are soluble in one or more of the common organic solvents, such as hexane, toluene or 1,1,1-trichloroethane. For the purpose of further illustrating the invention, the use of the azeotropes for cleaning was tested using a rosin-based solder flux as the soil. The cleaning tests were at 22°C. in an open bath with no distillative recycle of the azeotrope. All of the azeotropes were found to remove flux, although not each of the azeotropes was equally effective. For purposes of comparison, a CONTROL composition consisting of only octamethyltrisiloxane was included in these cleaning tests, and is shown in Table II as composition "No. 6". Example II Kester No. 1544 rosin flux was mixed with 0.05 weight percent of a nonreactive low viscosity silicone glycol flow-out additive. The mixture was applied as a uniform thin layer to a 2'' x 3'' (5.1 X 7.6 cm) area of an Aluminum Q panel with a No. 36 Industry Tech Inc., draw-down rod. An activated rosin-based solder flux commonly used for electrical and electronic assemblies was employed. It is a product manufactured and sold by Kester Solder Division, Litton Industries, Des Plaines, Illinois, USA. The approximate composition of the flux was fifty weight percent of a modified rosin, twenty-five weight percent of ethanol, twenty-five weight percent of 2-butanol and one weight percent of a proprietary activator. The coating was allowed to dry at room temperature and cured at 100°C. for ten minutes in an air oven. The Aluminum Q panel was placed in a large beaker which had a magnetic stirring bar at the bottom and one-third filled with the azeotropic composition. Cleaning was conducted while rapidly stirring at room temperature, even when cleaning with the higher temperature azeotropic compositions. The panel was removed at timed intervals, dried at 80°C. for ten minutes, weighed and reimmersed for additional cleaning. The initial coating weight and the weight loss were measured as a function of cumulative cleaning time, and this data is shown in Table II. In Table II, the alcohols and the ester are abbreviated as "2-M-1-P" for 2-methyl-1-pentanol; "HEXANOL" for 1-hexanol; "1-B-2-P" for 1-butoxy-2-propanol; and "ESTER" for ethyl lactate. The "WT%" shown in Table II refers to the weight percent of the alcohol or ester in the azeotrope. The "TEMP" is the azeotropic temperature in Centigrade degrees of the azeotrope. The "WT" is the initial weight of the coating in grams. The time shown in Table II is cumulative time measured after the elapse of one minute, five minutes, ten minutes and thirty minutes. As noted above, composition No. 6 in Table II was a CONTROL consisting of one hundred percent octamethyltrisiloxane (MDM). It should be apparent from Table II that all of the azeotropic compositions 1 to 5 in Table II were much more effective cleaners than composition No. 6. CLEANING EXTENT AT ROOM TEMPERATURE (22°C) No. WT% LIQUIDS TEMP WT % REMOVED (Time-min) 1 5 10 30 1 39% 2-M-1-P 139.4 0.3096 85.4 99.8 99.9 ---- 2 13% 2-M-1-P 25.0 0.3011 79.7 96.6 98.1 98.8 3 25% HEXANOL 143.9 0.2993 77.0 96.6 99.8 ---- 4 11% 1-B-2-P 151.8 0.3445 13.9 65.9 73.3 86.3 5 37% ESTER 139.4 0.3117 93.0 99.8 100.2 ---- 6 0% 100% MDM ---- 0.3460 0.7 1.5 1.9 3.2 Our azeotropes have several advantages for cleaning, rinsing or drying. Also, our azeotropic composition can easily be regenerated by distillation so that the performance of the cleaning mixture can be restored after a period of use. The performance factors which can be affected by the composition of azeotropic mixtures include bath life, cleaning speed, lack of flammability when only one component is non-flammable and lack of damage to sensitive parts. In vapor phase degreasing equipment, our azeotropic mixture can be continually restored by continuous distillation at atmospheric or at reduced pressure, and can be continually recycled in the cleaning equipment. In this type of equipment, cleaning or rinsing can be conducted at the boiling point by plunging the part to be cleaned or rinsed in the boiling liquid or by allowing the refluxing vapor to condense on the cold part. Alternatively, the part may be immersed in a cooler bath that is continually fed by fresh condensate and the dirty overflow liquid is returned to a boil sump. If the azeotrope is used in an open system, the composition and the performance of the azeotrope will remain constant even though evaporative losses occur. Such a system can be operated at room temperature when used in a ambient cleaning bath or when used as a wipe-on-by-hand cleaner. The cleaning bath can also be operated at elevated temperatures which are below the boiling point, although often cleaning, rinsing or drying, occurs faster at an elevated temperature, and hence is desirable when the part to be cleaned and the equipment permit. The azeotropes of the invention can be used for cleaning in a variety of ways beyond those shown by the foregoing examples. Thus, cleaning can be conducted by using a given azeotrope at or near its azeotropic temperature or at some other temperature. Other processes of use of the azeotropes of the invention include the distillative recycle of a spent azeotrope at atmospheric pressure or at a reduced pressure. In addition, cleaning may be conducted by immersing the part to be cleaned in quiescent or boiling liquid, as well as in the vapor condensation region above the boiling liquid. In the later case, the part is cleaned in a continually renewed liquid of maximum cleaning power. In cleaning applications according to our invention, only the azeotrope may be used, however, if desired, small amounts of one or more organic liquid additives can be combined with the azeotrope. Organic liquid additives contemplated according to the invention, are compounds capable of imparting an enhanced oxidative stability, corrosion inhibition, or solvency enhancement. Oxidative stabilizers inhibit the slow oxidation of organic compounds such as alcohols and esters. Corrosion inhibitors inhibit metal corrosion by traces of acids that may be present, or which slowly form in alcohols and esters. Solvency enhancers increase solvency power by adding more powerful solvents to a starting solvent. These additives can mitigate any undesired effects of the alcohol and ester components of the new azeotropes of the invention, since the alcohol and ester components are not as resistant to oxidative degradation as octamethyltrisiloxane. Numerous additives are suitable for combination with the azeotropes of the invention, and octamethyltrisiloxane is miscible with small amounts of many such additives. However, regardless of the additive, it must be one in which the resulting liquid mixture of the selected additive and the azeotrope, is homogeneous and single phased. Among the oxidative stabilizers that may be employed in amounts of 0.05 to 5 percent by weight are phenols such as trimethylphenol, cyclohexylphenol, thymol, 2,6-di-t-butyl-4-methylphenol, butylhydroxyanisole and isoeugenol; amines such as hexylamine, pentylamine, dipropylamine, diisopropylamine, diisobutylamine, triethylamine, tributylamine, pyridine, N-methylmorpholine, cyclohexylamine, 2,2,6,6-tetramethylpiperidine and N,N'-diallyl-p-phenylenediamine; and triazoles such as benzotriazole, 2-(2'-hydroxy-5'-methylphenyl)benzotriazole and chlorobenzotriazole. Among the corrosion inhibitors that may be employed in amounts of 0.1 to 5 percent by weight are aliphatic nitro compounds such as nitromethane, nitroethane and nitropropane; acetylene alcohols such as 3-methyl-1-butyn-3-ol, and 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 and 1-butene-3-ol; and acrylic acid esters such as methyl acrylate, ethyl acrylate and butyl acrylate. Among the solvency enhancers that may be employed in amounts of 0.1 to 10 percent by weight are hydrocarbons such as pentane, isopentane, hexane, isohexane and heptane; 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 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: A binary composition comprising octamethyltrisiloxane and an alcohol or ester selected from 8-40 wt% 2-methyl-1-pentanol, 5-28 wt% 1-hexanol, 2-13 wt% 1-butoxy-2-propanol and 36-46 wt% ethyl lactate, wherein the composition is homogeneous and azeotropic at a temperature within the range of zero to 162°C. inclusive. A method of cleaning material from the surface of an article comprising applying to the surface a cleaning agent which is a composition as defined in accordance with Claim 1. The method according to Claim 2 in which the article is an electronic circuit board or an article made of a material selected from metal, ceramic, glass and plastic. The method according to Claim 3 in which material cleaned from the surface is selected from carbonaceous materials and solder fluxes.

Inventors: FLANINGAM ORA LEY, WILLIAMS DWIGHT EDWARD, FLANINGAM, ORA LEY, WILLIAMS, DWIGHT EDWARD
Applicants: DOW CORNING, DOW CORNING CORPORATION
Application year: 1995
Main classification: C11D7
IPC codes: C07F7, C23G5, H05K3, H01L21, C07C69, C11D7, C07C31, B23K35