Patent Application
20140010963
None
This invention relates to novel silicone based release coating compositions and silicone based release coating compositions that contain release modifier compositions, both of which contain branched siloxanes.
Silicone based release coatings are useful in applications where relatively non-adhesive surfaces are required. Single sided liners, for example, backing papers for pressure sensitive adhesive labels, are usually adapted to temporarily retain the labels without affecting the adhesive properties of the labels. Double sided liners for example, interleaving papers for double sided and transfer tapes, are utilized to ensure the protection and desired unwind characteristics of a double sided self-adhesive tape or adhesive film.
Improvements in the performance of release coatings are continuously being sought with respect to, for example, ease of cure, i.e. the decrease in cure times at relatively low temperatures, anchorage of coatings to a substrate and release performance. One factor which particularly necessitates continued development of release coatings is the use of an ever increasing number of substrates, for example, polypropylene, polyethylene and polyester onto which release coating compositions are applied and cured and how to improve anchorage of silicone based release coating compositions to the substrates.
In one embodiment, the present invention relates to a silicone release coating composition, comprising;
In another embodiment, the invention is directed to a method of preparing a coated substrate comprising;
The branched siloxane comprises
(a) at least one Q unit of the formula (SiO4/2), and
(b) from 15 to 995 D units of the formula Rb2SiO2/2 which units (a) and (b) may be inter-linked in any appropriate combination, and
(c) M units of the formula RaRb2SiO1/2, wherein each Ra substituent is independently selected from an alkyl group having from 1 to 6 carbon atoms, an alkenyl group having from 1 to 6 carbon atoms or an alkynyl group having from 1 to 6 carbon atoms, at least three Ra substituents in the branched siloxane being alkenyl or alkynyl units, and each Rb substituent is independently selected from an alkyl group having from 1 to 6 carbon atoms, an alkenyl group having 2 to 6 carbon atoms, an aryl group, an alkoxy group, an acrylate group or a methacrylate group;
Alternatively, the branched siloxane contains from 20-500 D units. In another alternative, the branched siloxane contains from 50-350 D units.
Generally at least 50% of Ra substituents are alkenyl groups. Alternatively each Ra substituent is an alkenyl group. Each alkenyl group may be selected from vinyl, allyl, butenyl, pentenyl and hexenyl groups but is preferably selected from a vinyl (vi) and a hexenyl (hex) group.
Alternatively the branched siloxane comprises at least one Q unit bonded to four (Rb2SiO2/2)n chains and for example can have the formula
where each n is independently from 1 to 100.
Each Rb substituent is an alkyl group, for example, a methyl, ethyl, propyl, isopropyl, butyl, pentyl or hexyl group. Alternatively the Rb substituent is a methyl or ethyl group. Alternatively the Rb substituent is a methyl group.
Hence, in the case when there is only a single unit of the formula SiO4/2 present in the branched siloxane according to the first aspect of the present invention, the branched siloxane may have substantially the following formula wherein each n is independently from 1 to 100 when each Ra substituent is a vinyl group and each Rb group is a methyl group.
It is to be appreciated that in view of the size of the branched siloxane, it is possible that a very small number of the siloxane units present in the branched siloxane (preferably less than 1% siloxane units) may be units of the formula RbSiO3/2, where Rb as previously defined, may occur.
Henceforth the total number of siloxane units in the branched siloxane will be referred to as the degree of polymerization (DP).
The DP of the branched siloxane may be from 20 to 1000. Alternatively this range is from 20 to 500. In another alternative, the range is from 20 to 400.
A method for the preparation of the branched siloxane comprises the steps of:
(a) mixing a compound having the general formula (SiO4/2)(RaRb2SiO1/2)4 with a cyclic polydiorganosiloxane, and/or a substantially linear hydroxy terminated polydiorganosiloxane, and/or a substantially linear trimethylsiloxy terminated polydiorganosiloxane wherein each Ra substituent is selected from an alkyl group having from 1 to 6 carbon atoms, an alkenyl group having from 1 to 6 carbon atoms or an alkynyl group having from 1 to 6 carbon atoms and each Rb substituent is selected from an alkyl group having from 1 to 6 carbon atoms, an aryl group, an alkoxy group, an acrylate group or a methacrylate group;
(b) causing the mixture to react in the presence of an acid or phosphazene base catalyst at a temperature of up to 180° C.; and
(c) neutralizing the reaction mixture.
Generally each cyclic polydiorganosiloxane contains from 3 to 10 Rb2SiO2/2 units although in the alternative, the cyclic polydiorganosiloxanes are polydialkylsiloxane rings consisting of from 3 to 6 repeating Rb2SiO2/2 units in which each Rb substituent is a methyl group.
The type of reaction which takes place is either an acid or a base catalyzed equilibration reaction dependent on the chosen catalyst.
In the case of acid catalyzed equilibration reactions, the acid catalyst used may be any catalyst suitable the catalysis of an acid based equilibration reaction for example trifluoromethane sulfonic acid, acid clays, and supported acid catalyst, for example, amberlyst catalyst. A preferred catalyst is a trifluoromethane sulfonic acid.
In the case of basic catalyzed equilibration preparations the catalyst may be any suitable phosphazene base catalyst, for example phosphazene bases of the following general formulae:
((R12N)3P═N—)k(R12N)3-kP═NR2
[((R12N)3P═N—)k(R12N)3-kP—N(H)R2]+[A−] or
[((R12N)3P═N—)l(R12N)4-lP]+[A−]
in which R1, which may be the same or different in each position, is hydrogen or an optionally substituted hydrocarbon group, preferably a C1-C4 alkyl group, or in which two R1 groups bonded to the same N atom may be linked to complete a heterocyclic ring, preferably a 5- or 6-membered ring; R2 is hydrogen or an optionally substituted hydrocarbon group, preferably a C1-C20 alkyl group, more preferably a C1-C10 alkyl group; k is 1, 2 or 3, preferably 2 or 3; 1 is 1, 2, 3 or 4, preferably 2, 3 or 4; and A is an anion, preferably fluoride, hydroxide, silanolate, alkoxide, carbonate or bicarbonate. In an alternative, A is an aminophosphazenium hydroxide. Suitable catalysts and their preparation are described, for example, in EP)-A-1008598.
In the case of the acid catalyzed equilibration reaction the reaction mixture is preferably maintained at a temperature of from 75° C. to 120° C., most preferably the reaction mixture is maintained at a temperature of from 80° C. to 90° C. in the presence of a water co-catalyst. In the case of the base catalyzed equilibration reaction the reaction mixture is preferably maintained at a temperature of from 120° C. and 160° C., most preferably the reaction mixture is maintained at a temperature of from 130° C. to 150° C.
Any appropriate neutralizing agent may be utilized, the choice clearly being dependent on the acidic or basic nature of the catalyst, examples include the use of silylated phosphate or silylated alkylphosphonates, for example bis(trimethylsilyl)hydrogen phosphate or bis(trimethylsilyl)vinyl phosphonate for base catalyzed equilibrium reactions and calcium carbonate for acid catalyzed equilibration reactions.
The amount of each constituent used is dependent on two factors, the required degree of polymerization of the branched siloxane and the number of alkenyl groups required in the branched siloxane. Generally there is from 1.1 to 22.1% by weight of (SiO4/2)(RaRb2SiO1/2)4 in the mixture of step (a), alternatively from 2.21 to 11.04% by weight of (SiO4/2)(RaRb2SiO1/2)4 present and in another alternative from 3.45 to 6.9% by weight. The remainder is made up to 100% by weight with the cyclic polydiorganosiloxane and/or the substantially linear hydroxy terminated polydiorganosiloxane and/or the substantially linear trimethylsiloxy terminated polydiorganosiloxane.
The organohydrogenpolysiloxane cross linking agent generally contains on average at least three Si—H groups and may have the general formula:
Rt3SiO1/2((CH3)2!SiO2/2)d(Rt2SiO2/2)e)SiO1/2Rt3
where each Rt independently is an alkyl group having 1 to 4 carbon atoms or hydrogen, d is 0 or an integer, e is an integer such that d+e is from 8 to 400, alternatively from 10 to 300, and alternatively from 20 to 250. Alternatively the cross-linking agent may be an MQ resin consisting of units of the general formula SiO4/2 and Rq3SiO1/2 wherein at least one Rq substituent is a hydrogen atom and the remainder are alkyl groups.
Generally, the ratio of the total amount of Si—H groups of component (II) to aliphatically unsaturated hydrocarbon groups of Component (I) in the release coating composition is in the range of from 0.9:1 to 3:1, alternatively in the range of from 1.1:1 to 2.8:1, alternatively in the range is from 1.2:1 to 2:5.
Component (III) comprises any catalyst typically employed for hydrosilylation reactions. It is preferred to use platinum group metal-containing catalysts. By platinum group it is meant ruthenium, rhodium, palladium, osmium, iridium and platinum and complexes thereof. Platinum group metal-containing catalysts useful in preparing the compositions of the present invention are the platinum complexes prepared as described by Willing, U.S. Pat. No. 3,419,593, and Brown et al, U.S. Pat. No. 5,175,325, each of which is hereby incorporated by reference to show such complexes and their preparation. Other examples of useful platinum group metal-containing catalysts can be found in Lee et al., U.S. Pat. No. 3,989,668; Chang et al., U.S. Pat. No. 5,036,117; Ashby, U.S. Pat. No. 3,159,601; Lamoreaux, U.S. Pat. No. 3,220,972; Chalk et al., U.S. Pat. No. 3,296,291; Modic, U.S. Pat. No. 3,516,946; Karstedt, U.S. Pat. No. 3,814,730; and Chandra et al., U.S. Pat. No. 3,928,629 all of which are hereby incorporated by reference to show useful platinum group metal-containing catalysts and methods for their preparation. The platinum-containing catalyst can be platinum metal, platinum metal deposited on a carrier such as silica gel or powdered charcoal, or a compound or complex of a platinum group metal. Preferred platinum-containing catalysts include chloroplatinic acid, either in hexahydrate form or anhydrous form, and or a platinum-containing catalyst which is obtained by a method comprising reacting chloroplatinic acid with an aliphatically unsaturated organosilicon compound such as divinyltetramethyldisiloxane, or alkene-platinum-silyl complexes as described in U.S. Pat. No. 6,605,734 (August 12, 2003), such as (COD)Pt(SiMeCl2)2, where COD is 1,5-cyclooctadiene and Me is methyl. These alkene-platinum-silyl complexes may be prepared, for example by mixing 0.015 mole (COD)PtCl2 with 0.045 mole COD and 0.0612 moles HMeSiCl2.
The appropriate amount of the catalyst will depend upon the particular catalyst used.
The platinum catalyst should be present in an amount sufficient to provide at least 2 parts per million (ppm), alternatively, 4 to 200 ppm of platinum based on total weight percent solids (all non-solvent ingredients) in the composition. In another alternative, the platinum is present in an amount sufficient to provide 4 to 150 weight ppm of platinum on the same basis. The catalyst may be added as a single species or as a mixture of two or more different species.
Styrene/olefin latexes useful in the practice of the present invention include, for example, styrene-butadiene latex, styrene-acrylate latex, styrene-acrylate-acrylonitrile latex, styrene-butadiene-acrylate-acrylonitrile latex, styrene-butadiene-acrylonitrile latex, styrene-maleic anhydride latex, and styrene-acrylate-maleic anhydride latex, as well as carboxylated styrene-butadiene latex, carboxylated styrene-acrylate latex, carboxylated styrene-acrylate-acrylonitrile latex, carboxylated styrene-butadiene-acrylate-acrylonitrile latex, carboxylated styrene-butadiene-acrylonitrile latex, carboxylated styrene-maleic anhydride latex, carboxylated styrene-acrylate-maleic anhydride latex, and mixtures thereof. Alternatively, the styrene/olefin latexes are styrene-butadiene latex, styrene-acrylate latex, styrene-acrylate-acrylonitrile latex, styrene-butadiene-acrylate-acrylonitrile latex, styrene-butadiene-acrylonitrile latex, styrene-maleic anhydride latex, styrene-acrylate-maleic anhydride latex, and mixtures thereof. Alternatively, the styrene/olefin latex is styrene-butadiene latex.
The preparation of the styrene/olefin latex is effected by emulsion polymerization, and the result is therefore an emulsion polymer. The preparation can, however, also be effected by solution polymerization and subsequent dispersing in water to form an emulsion.
In a representative procedure of emulsion polymerization, ionic and/or nonionic emulsifiers and/or protective colloids or stabilizers are used as surface-active compounds.
The surface-active substance is usually used in amounts of from 0.1 to 10% by weight, based on the monomers to be polymerized. Water-soluble initiators for the emulsion polymerization are two ammonium and alkali metal salts of peroxodisulfuric acid, e.g. sodium peroxodisulfate hydrogen peroxide or organic peroxides e.g. tert-butyl hydroperoxide. Reduction oxidation (redox) initiator systems are also suitable.
In the representative procedure, the amount of the initiators is in general from 0.1 to 10, alternatively from 0.5 to 5, % by weight, based on the monomers to be polymerized. It is also possible to use a plurality of different initiators in the emulsion polymerization.
In the representative procedure of the polymerization, it is possible to use regulators, for example in amounts of from 0 to 0.8 parts by weight, based on 100 parts by weight of the monomers to be polymerized, by means of which the molar mass is reduced. For example, compounds having a thiol group, such as tert-butyl mercaptan, thioglycolic acid ethyl acrylic ester, mercaptoethynol, mercaptopropyltrimethoxylan or tert-dodecyl mercaptan, are suitable.
In the representative procedure, the emulsion polymerization is effected as a rule at from 30° C. to 130° C., alternatively from 50° C. to 90° C. The polymerization medium may consist either only of water or of mixtures of water and liquids miscible therewith such as methanol. Typically, however, only water is used. The emulsion polymerization can be carried out both as a batch process and in the form of a feed process, including a step or gradient procedure. However, the feed process in which a part of the polymerization batch is initially taken, heated to the polymerization temperature and partly polymerized and then the remainder of the polymerization batch is fed to the polymerization zone, usually via a plurality of spatially separated feeds, one or more of which contain the monomers or in emulsified form, continuously, stepwise or with superposition of a concentration gradient, while maintaining the polymerization, is preferred.
In the representative procedure, the manner in which the initiator is added to the polymerization vessel in the course of the free radical aqueous emulsion polymerization is known. It may be either completely initially taken in the polymerization vessel or used continuously or stepwise at the rate of its consumption in the course of the free radical aqueous emulsion polymerization. Specifically, this depends on the chemical nature of the initiator system and on the polymerization temperature. Usually, a part is initially taken and the remainder is fed in at the rate of consumption in the polymerization zone.
For removing the residual monomers in the representative procedure, an initiator is usually also added after the end of the actual emulsion polymerization, i.e. after a conversion of the monomers of at least 95%. The individual components may be added to the reactor in the feed process from above, from the side or from below through the reactor bottom. In the emulsion polymerization, aqueous dispersions of the polymer, as a rule having solids contents of from 15 to 75, preferably from 40 to 75, % by weight, are obtained.
Typically, the styrene/olefin latex (IV) is present in the silicone release coating composition at from 0.5 to 19.5 weight % on a dry basis of all the components, alternatively at from 0.75 to 15, and alternatively at from 1-8.
A styrene/olefin latex (IV) having utility in this invention is Styrofan® DS 3492, an aqueous dispersion of a styrene/olefin latex (IV), specifically a styrene butadiene latex from BASF.
The composition and the method for preparing the composition may additionally comprise one or more inhibitors (V) adapted to prevent the cure of the coating composition from occurring below a predetermined temperature. While an inhibitor is not essential to the functioning of the coating composition itself it is to be understood that in the absence of an inhibitor the catalyst may initiate/catalyze the cure of the silicone based release coating composition at ambient temperature, once the three essential constituents have been mixed together.
Examples of suitable inhibitors (V) include ethylenically or aromatically unsaturated amides, acetylenic compounds, ethylenically unsaturated isocyanates, olefinic siloxanes, unsaturated hydrocarbon diesters, conjugated ene-ynes, hydroperoxides, nitriles and diaziridines, specific examples include methyl butynol, dimethyl hexynol or ethynyl cyclohexanol, trimethyl(3,5-dimethyl-1-hexyn-3-oxy)silane, a maleate for example, Bis(2-methoxy-1-methylethyl)maleate, diallylmaleate, a fumarate e.g. diethylfumarate or a fumarate/alcohol mixture wherein the alcohol is, for example, benzyl alcohol or 1-octanol and ethenyl cyclohexyl-1-ol.
The release coating composition may optionally comprise a dialkyl alkenyl silyl terminated polydiorganosiloxane having a viscosity at 25° C. of at least 50 mm2/s of which a dimethyl vinyl silyl terminated or dimethyl hexenyl silyl terminated polydimethylsiloxane is preferred.
Other optional constituents which may also be added to the release coating compositions of the present invention include, for example, silicone release modifiers, fillers, reactive diluents, adhesion promoters, solvents, fragrances, preservatives and fillers, for example, silica, quartz and chalk.
Useful silicone based release modifiers which may be added to the silicone release coating of the present invention may include a branched siloxane as described above and at least one additional component selected from the following components:
(i) an alkenylated silicone resin
(ii) an alkenylated polydiorganosiloxane, and
(iii) one or more primary alkenes containing from 14 to 30 carbon atoms,
(iv) one or more branched alkenes containing at least 10 carbon atoms, and
(v) a non-alkenylated resin.
The alkenylated silicone resin (i) is most preferably at least one alkenylated MQ resin wherein the M groups have the general formula R23SiO1/2 and are typically trialkyl siloxy and/or dialkyl alkenyl siloxy groups. The alkenyl group may be selected from the group consisting of cyclohexenyl, vinyl, propenyl, butenyl, pentenyl and hexenyl. Most preferably the alkenyl group is a vinyl or hexenyl group. The alkyl groups may be any suitable alkyl groups, but are most preferably methyl groups. The Q groups are groups of the formula SiO4/2 and these M and Q groups may be present in any appropriate ratio.
The alkenylated polydiorganosiloxane, is preferably an alkenyldialkyl silyl terminated polydiorganosiloxane comprising units of the formula R2SiO2/2 wherein each R group is an alkyl group having from 1 to 6 carbon atoms or one R group is an alkyl group as defined and one is an alkenyl group having from 1 to 6 carbon atoms, preferably a vinyl or hexenyl group.
Each primary alkene (iii) may be any primary alkene containing from 10 to 30 carbon atoms such as, for example, tetradecene and octadecene.
Each branched alkene (iv) may be any one or more suitable branched alkenes, for example, one or more branched alkenes of the general formula
wherein the n number of methylene groups and m number of branched alkyl groups are randomly distributed in the chain, n and m are independently 0 or an integer of from 1 to 20, x, z and each y is independently an integer of from 1 to 12. Preferably the total number of carbon atoms in each alkene is at least 20. It is to be noted that release modifiers containing substantially linear alkenes such as for example component (iii) above tend to cause smoking during the curing process of a coating. It has been found that replacement of component (iii) with a branched alkene as exemplified by component (iv) significantly reduces this problem.
Such a release modifier preferably comprises from 25 to 85% by weight of the branched siloxane, the remainder being made up of one or more of components (i), (ii), (iii) or (iv).
One advantage in using a release modifier in accordance with the present invention is that by replacing at least a proportion of substantially linear alkene with the branched siloxane the smoking effect often seen during the cure process is significantly reduced. It has also been found that when a release modifier is used in a release coating composition, the level of extractables, i.e. the level of uncured siloxane, is maintained at the same level or is even reduced compared to the level of extractables obtained from a release coating composition not containing the release modifier.
While release coating compositions of the present invention may be prepared by merely mixing the branched siloxane (I), the organohydrogenpolysiloxane cross-linking agent (II), the hydrosilylation catalyst (III), and the styrene/olefin latex(IV) together with any optional ingredients, it may be more desirable to prepare a separate package of certain components such as components (I) and (II). Typically, this separate package of components (I) and (II) is an item of commerce and is available from Dow Corning Corporation, Midland, Mich. as aqueous emulsions, identified as Syl-Off® EM 7935 and Syl-Off® EM 7990 aqueous emulsion coatings.
The four components can each be aqueous emulsions. In putting together the inventive composition, the four components can be combined in any order, with or without additional water to form a coating bath. If no additional water is added and if it is determined that the viscosity of the bath is higher than 10000 mm2/s, additional water may be added to reduce the viscosity. The contents are stirred for about five minutes to effect dispersion and permitted to equilibrate for about one hour.
The bath containing the release coating composition has a viscosity of not less than 50 mm2/s and not more than 10000 mm2/s at 25° C., alternatively, the viscosity is from 50 to 1000 mm2/s so that the release coating composition is of a suitable viscosity for coating a substrate. If the viscosity is lower than 50 mm2/s problems may occur with the wetting of a substrate surface by the release coating composition. If the viscosity is higher than 10000 mm2/s then the release coating composition is too viscous for use in the present application.
Optional bath life extenders may be present in an amount sufficient to retard the curing reaction at room temperature. Examples may include compounds which contain one or more primary or secondary alcohol groups, for example, aliphatic and aromatic alcohols with fewer than 10 carbon atoms, such as methanol, ethanol, propanol, phenol and cyclohexanol, carboxylic acids and cyclic ethers.
In another embodiment, the invention is directed to a method of preparing a coated substrate comprising;
The present release coating composition may be utilized for release purposes on a variety of substrates including paper and films. The substrates may for example be polyethylene, polypropylene, polyester, polystyrene, oriented polypropylene, biaxially oriented polypropylene films, polyethylene coated Kraft paper, or polypropylene coated Kraft paper. An alternative substrate is polyester. An alternative polyester is polyethylene terephthalate.
Any conventional coating technique can be used to apply the release coating composition to the substrate such as brushing, spreading, rolling, wire or knife coating, roll coating, gravure coating, transfer roll coating, air knife or doctor blade coating. The coating can be successfully applied with direct gravure, reverse gravure, single or double Mayer rod, knife-over-roll, and inverted knife techniques. The technique is selected for the substrate to be coated. The coating viscosity is adjusted for the coating technique. The coating solids are adjusted to provide the requisite coating viscosity.
The coat weight of the coating will vary depending upon many factors including the nature of the substrate, for example, its absorbency, porosity, surface roughness, crepe, etc., whether the substrate is a film or paper and whether the paper is impregnated. Generally, the release coating is applied in an amount ranging from about 0.5 to 5 pounds dry weight per 2 5 3,000 square feet. Film, foil, and super calendared Kraft paper substrates are typically coated with 35% solids material by direct or reverse gravure techniques to a dry coating weight of 0.5 to 1.5 pounds per 3,000 square feet ream. Coarse paper substrates, such as crepe or flatback, are typically coated with 35 to 45% solids material by any of the aforementioned techniques to a dry coat weight of 2 to 6 pounds per 3,000 sq. ft. ream. While heavier coat weights may be used, this is generally economically undesirable.
Cure time is dependent on several variables, typically on the amount of the organohydrogenpolysiloxane cross-linking agent (II) used, on the thickness of the coating onto the substrate, and on the temperature. When temperature is the variable, a higher temperature results in a faster cure time and a lower temperature results in a slower cure time. The temperature of paper coating machines can be adjusted such that when the paper is coated at a paper temperature as low as 80° C. and at a speed on 150 m/min, cure occurs at about 30 seconds. When the paper is coated at a paper temperature as high as 220° C. and at a speed on 1000 m/min, cure occurs at about 1 second.
The following test terms are used in the examples: cure by extractables and anchorage. The test “cure by extractables” provides a quantitative determination of the amount of silicone release coating that is not cured after the curing process (called extractables) and would transfer into a solvent. The degree of cure of a specified silicone release coating applied to a specified substrate is determined quantitatively after preparation under specified and controlled conditions. This is carried out by first determining the coat weight of a standard sized sample of a substrate with a cured coating. The coated sample is then placed in a solution of methyl isobutyl ketone solvent to extract any unreacted siloxane which has not been cross-linked into the coating matrix or adhered to the substrate. After a 20 minute period of time the sample is removed from the solvent, dried at room temperature for five minutes, and reweighed. The percentage extractables indicated in Table 1 are the percentage weight losses after the unreacted silicone had been removed from the coating. The quantity of extractable silicone may be determined by the change in the silicone coat weight on the substrate. The silicone coat weight on the substrate is determined by x-ray fluorescence (XRF) analysis, before and after contact with the methyl isobutyl ketone extraction solvent.
The Anchorage index results measure the anchorage or adhesive strength of a cured silicone coating composition over an extended period of time to a corona treated 50 micron monoaxially oriented polyester terephthalate substrate. For each result in Tables 1 and 2, an identically sized sample of the substrate coated with release coating composition was cut, and the “initial coat weight (g/m2)”, i.e. the amount of the release coating composition coated on to the surface of the substrate was determined by x-ray fluorescence.
The aforementioned sample was adhered to a flat plastic disc and fitted in to the base of a 3.2 Kg weight. The sample, with the weight applying downward pressure, is then placed on a felt bed with the release coating composition face of the sample in contact with the felt surface. The weighted sample was subsequently moved along a 30 cm length of the felt bed at a pre-set speed of 3 m/min on two occasions, utilizing different sections of the felt bed on each occasion and the sample coat weight was remeasured and is indicated as “subsequent coat weight (g/m2).”
The results provided in Tables 1 and 2 are determined by way of the following equation
The % Anchorage Index is therefore the percentage of the release coating composition remaining on the surface of the substrate and hence 100% Anchorage Index equates to no rub off.
The invention having been generally described above, may be better understood by reference to the examples described below. The following examples represent specific but non-limiting embodiments of the present invention.
Added to a vessel were 28.5 parts (40% on a dry basis) Syl-Off® EM 7935 aqueous emulsion coating from Dow Corning Corporation, Midland, Mich. that contains component (I) and component (II), present as 30-60 wt % dimethyl cyclics with tetrakis(vinyldimethylsiloxy)silane and 1-5 wt % dimethyl, methylhydrogen siloxane respectively, 1.5 parts (40% on a dry basis) Syl-Off® EM 7975 catalyst aqueous emulsion from Dow Corning Corporation, Midland, Mich. that contains component (III), present as 30-60 wt % of a Pt complex dispersed in dimethylvinyl-terminated dimethyl siloxane, and 70 parts water. The contents were stirred for five minutes to effect dispersion and then permitted to rest for one hour to establish equilibrium.
The procedure and reactants of Example 1 were repeated except that 0.5 parts (50% on a dry basis) Styrofan® DS 3492, an aqueous dispersion of a styrene/olefin latex (IV), specifically a styrene butadiene latex from BASF, was added to give a formulation containing 2% of component (IV) in the formulation, on a dry basis.
The procedure and reactants of Example 1 were repeated except that 1 part (50% on a dry basis) Styrofan® DS 3492, was added to give a formulation containing 4% of component (IV) in the formulation, on a dry basis.
The procedure and reactants of Example 1 were repeated except that 2 parts (50% on a dry basis) Styrofan® DS 3492, was added to give a formulation containing 8% of component (IV) in the formulation, on a dry basis.
The procedure and reactants of Example 1 were repeated except that 5 parts (50% on a dry basis) Styrofan® DS 3492, was added to give a formulation containing 20% of component (IV) in the formulation, on a dry basis.
Added to a vessel were 28.5 parts (40% on a dry basis) Syl-Off® EM 7990 aqueous emulsion coating from Dow Corning Corporation, Midland, Mich. that contains components (I) and (II), present as 30-60 wt % dimethyl cyclics with tetrakis(vinyldimethylsiloxy)silane and 1-5 wt % dimethyl, methylhydrogen siloxane respectively, 1.5 parts (40% on a dry basis) Syl-Off® EM 7975 catalyst aqueous emulsion from Dow Corning Corporation, Midland, Mich. that contains component (III), present as 30-60 wt % of a Pt complex dispersed in dimethylvinyl-terminated dimethyl siloxane, and 70 parts water. The contents were stirred for five minutes to effect dispersion and then permitted to rest for one hour to establish equilibrium.
The procedure and reactants of Example 6 were repeated except that 0.5 parts (50% on a dry basis) Styrofan® DS 3492, was added to give a formulation containing 2% of component (IV) in the formulation, on a dry basis.
The procedure and reactants of Example 6 were repeated except that 1 part (50% on a dry basis) Styrofan® DS 3492, was added to give a formulation containing 4% of component (IV) in the formulation, on a dry basis.
The procedure and reactants of Example 6 were repeated except that 2 parts (50% on a dry basis) Styrofan® DS 3492, was added to give a formulation containing 8% of component (IV) in the formulation, on a dry basis.
The following Table 1 details a comparative study of the release performance of a corona treated oriented polyethylene terephthalate (PET), substrate coated with silicone based release coating compositions of Examples 1-5.
The composition of each Example was applied on to the PET substrate from Mitsubishi using a direct reverse gravure type TR15e coater at room temperature (20° C.) and then the resultant coating was cured at 180° C. for a period of 7.6 seconds.
As observed above, the addition of the styrene/olefin latex as styrene butadiene latex in Examples 2-4 shows an improvement in the anchorage index of the silicone release coating composition to the PET substrate, at one day without adversely affecting the cure.
The following Table 2 details a comparative study of the release performance of a corona treated oriented polyethylene terephthalate (PET), substrate coated with silicone release coating compositions of Examples 6-9.
The composition of each Example was applied on to the PET substrate from Mitsubishi using a direct reverse gravure type TR15e coater at room temperature (20° C.) and then the resultant coating was cured at 180° C. for a period of 7.6 seconds.
As observed above, the addition of the styrene/olefin latex as styrene butadiene latex in Examples 7-9 shows an improvement in the anchorage index of the silicone release coating composition to the PET substrate, at both one day and at three months without adversely affecting the cure. Further, after 3 months' aging of the coated film, the % decrease in the anchorage index of Examples 7-9 containing the styrene/olefin latex is not as severe as the % decrease in the anchorage index of the baseline composition Example 6.
While the invention has been explained in relation to its preferred embodiments, it is to be understood that various modifications thereof will become apparent to those skilled in the art upon reading the description. Therefore, it is to be understood that the invention disclosed herein is intended to cover such modifications as fall within the scope of the appended claims.
| Filing Document | Filing Date | Country | Kind | 371c Date |
|---|---|---|---|---|
| PCT/US12/27668 | 3/5/2012 | WO | 00 | 9/17/2013 |
| Number | Date | Country | |
|---|---|---|---|
| 61454064 | Mar 2011 | US |
