Patent Application
20060122338
The present invention relates to moisture-curable polyether urethanes containing terminal cyclic urea/reactive silane groups and prepared from polyether polyols having a low degree of unsaturation and to the use of these polyether urethanes as sealants, adhesives and coatings.
Polyether urethanes containing reactive silane groups, also referred to as silane-terminated polyurethanes (STPs), and their use as sealants and adhesives are known and described, e.g., in U.S. Pat. Nos. 5,554,709; 4,857,623; 5,227,434 and 6,197,912; and WO 02/06367. The silane-terminated polyurethanes may be prepared by various methods. In one method the silane-terminated polyurethanes are prepared by reacting diisocyanates with polyether polyols to form isocyanate-terminated prepolymers, which are then reacted with aminosilanes to form the silane-terminated polyurethanes. The sealants may also be prepared by reacting unsaturated monools with diisocyanates to form intermediates containing unsaturated end groups and then converting these unsaturated groups to alkoxysilane groups by hydrosilylation. In another method the sealants are prepared in one step by the reaction of polyether diols with isocyanatosilanes
To be useful as sealants the silane-terminated polyurethanes should have a number average molecular weight of 6000 to 20,000. One method of obtaining this molecular weight is to use polyether diols prepared by the KOH process and having a molecular weight of 2000 to prepare the isocyanate-terminated prepolymers. The presence of urethane groups causes the products to have a high viscosity. To achieve suitable application viscosities, the high viscosity is reduced by the addition of higher amounts of plasticizer and lesser amounts of fillers, resulting in more expensive sealant products.
Another method of obtaining high molecular weight sealants is by using high molecular weight polyether diols having a low degree of unsaturation and prepared using special catalysts as described in EP-A 0,546,310, EP-A 0,372,561 and DE-A 19,908,562. When these polyether diols are used, the resulting sealants have excellent tensile strength, but the sealants are too brittle for many applications because the elongation is too low and the 100% modulus is too high.
The preparation of sealants from mixtures of polyfunctional and monofunctional silane-terminated polyurethanes is known and disclosed in U.S. Pat. Nos. 5,554,709 and 4,857,623 and WO 02/06367. However, these references do not disclose the use of polyether polyols having a low degree of unsaturation and aspartate-functional silanes to prepare the sealants.
The preparation of silane-terminated polyether urethanes from aspartate-functional silanes is disclosed in U.S. Pat. No. 5,364,955 and WO 98/18843. In both of these references the polyethers used to prepare polyether urethanes do not have a low degree of unsaturation. In addition, mixtures of polyfunctional and monofunctional silane-terminated polyurethanes are not disclosed. Finally, in the latter reference the polyethers must contain 15 to 40% by weight of ethylene oxide units.
WO 00/26271 discloses the preparation of silane-terminated polyether urethanes from polyether polyols having a low degree of unsaturation and aspartate-functional silanes. The products are prepared by reacting diisocyanates with high molecular weight polyether diols to form NCO prepolymers, which are then capped with aspartate-functional silanes to form silane-terminated polyether urethanes. This application does not disclose mixtures of disilane-terminated polyether urethanes with polyether urethanes containing one reactive silane group.
U.S. Pat. No. 6,265,517 describes a similar process for preparing silane-terminated polyether urethanes from polyether polyols having a low degree of unsaturation and aspartate-functional silanes. The patent requires the starting polyol to have a monool content of less than 31 mole %, and teaches that a relatively high monool content is highly undesirable because monools react with isocyanates thereby reducing crosslinking and curing of the prepolymer. The patent also requires the aspartate silanes to be prepared from dialkyl maleates in which the alkyl groups each contain more than four carbon atoms.
EP 0,372,561 discloses polyether urethanes containing reactive silane groups and prepared from polyether polyols having a low degree of unsaturation. In addition, polyether urethanes containing one reactive silane group are disclosed. This application fails to disclose the use of aspartate-functional silanes to incorporate the reactive silane groups.
Copending applications, Ser. Nos. 10/690,953, 10/690,954, 10/690,956 and 10/690,955, disclose alkoxysilane-functional polyether urethanes containing a mixture of polyether urethanes containing two or more reactive silane groups with polyether urethanes containing one reactive silane group. The polyether urethanes containing two or more reactive silane groups are prepared from high molecular weight polyether polyols having a low degree of unsaturation.
The deficiencies of the preceding sealants were overcome in copending applications, U.S. Ser. Nos. 10/690,751,10/690,955, 10/690,953, 10/690,956, 10/690,954 and 10/690,931, which describe moisture-curable, alkoxysilane-functional polyether urethanes containing both polyether urethanes having two or more reactive silane groups and polyether urethanes having one reactive silane group. The moisture-curable polyether urethanes are suitable for use as sealants, adhesives and coatings which possess high tensile strengths and elongations and have a reduced 100% modulus when compared with existing products.
In the copending applications the polyether urethane component containing two or more reactive silane groups is prepared from high molecular weight polyether polyols having a low degree of unsaturation. In addition, at least a portion of the reactive silane groups present in at least one of the two components are incorporated by the use of silanes containing secondary amino groups.
Copending application, U.S. Ser. No. 10/690,955 describes moisture-curable polyether urethanes in which the silane groups are incorporated into the polyether urethanes having two or more reactive silane groups by the use of certain aspartate-functional silanes. A disadvantage of these moisture-curable polyether urethanes is that they are not storage stable at moderately elevated temperatures of 50 to 90° C., which may be present in a drum stored in a hot climate.
Accordingly, it is an object of the present invention to provide moisture-curable polyether urethanes that may be cured to provide products which are storage stable at elevated temperatures and also retain all of the valuable properties of the polyether urethanes disclosed in the preceding copending applications, i.e., the products are suitable for use as sealants, adhesives and coatings which possess high tensile strengths and elongations and have a reduced 100% modulus.
This object may be achieved with the moisture-curable polyether urethanes according to the present invention that contain terminal cyclic urea/reactive silane groups.
The present invention is based on the surprising discovery that the non-cyclic urea groups formed by the reaction of isocyanate groups and aspartate silane groups decompose back into the starting components when stored at moderately elevated temperatures. In accordance with the present invention this decomposition is prevented by converting the non-cyclic urea groups into cyclic urea groups, which are thermally stable.
It is surprising that the polyether urethanes obtained according to the present invention can be used to prepare cured resins that possess the same properties as those obtained in accordance with the copending applications because the presence of cyclic urea groups would be expected to result in less flexible cured resins that would not have the same elongation and 100% modulus as cured resins prepared from polyether urethanes containing non-cyclic urea groups.
The present invention relates to moisture-curable, polyether urethanes having terminal cyclic urea/reactive silane groups and containing
wherein
The present invention also relates to sealant, adhesive and coating compositions containing these polyether urethanes.
In the moisture-curable, polyether urethanes according to the present invention polyether urethanes a) are present in a minimum amount of at least 20% by weight, preferably 30% by weight and more preferably 40% by weight. The maximum amount of polymers a) is 100% by weight, preferably 90% by weight, more preferably 80% by weight and most preferably 70% by weight. Polyether urethanes b) are present in a minimum amount of 0% by weight, preferably 10% by weight, more preferably 20% by weight and most preferably 30% by weight. The maximum amount of polymers b) is 80% by weight, preferably 70% by weight and more preferably 60% by weight. The preceding percentages are based on the total weight of polyether urethanes a) and b).
Suitable polymers for use as component a) include polyether urethanes containing one or more, preferably one, polyether segment having a number average molecular weight of 3000 to 20,000, preferably 6000 to 15,000 and more preferably 8000 to 12,000. When the polyether segments have a number average molecular weight of 3000, for example, then two or more of these segments must be present so that the number average molecular weights of all of the polyether segments per molecule averages 6000 to 20,000. Polymers a) also contain two or more, preferably two, terminal cyclic urea/reactive silane groups. The reactive silane groups are incorporated by the reaction of an isocyanate group with an aspartate silane corresponding to formula I to form a non-cyclic urea/reactive silane group and then converting the non-cyclic urea into a cyclic urea in presence of a catalyst and heat.
In accordance with the present invention the term “reactive silane group” means a silane group containing at least two alkoxy or acyloxy groups as defined by substituent “X”. A silane group containing two or three alkoxy and/or acyloxy groups is considered to be one reactive silane group. Also, a urethane is a compound containing one or more urethane and/or urea groups. These compounds preferably contain one or more urethane groups and may optionally contain urea groups. More preferably, these compounds contain both urethane and urea groups.
Polymers a) may be prepared by several methods. For example, they may be prepared by reacting a high molecular weight polyether containing at least two isocyanate-reactive groups, preferably hydroxyl groups, with an excess of a polyisocyanate, preferably a diisocyanate, to form an NCO prepolymer. The resulting NCO prepolymer is reacted with an aspartate silane corresponding to formula I to form a polyether urethane intermediate containing terminal non-cyclic urea/reactive silane groups, which is then reacted in the presence of a catalyst and heat to form polymers a). Polymers a) may also be prepared by reacting an excess of a polyisocyanate with an aspartate silane to form a monoisocyanate, then reacting the monoisocyanate with a high molecular weight polyether to form a polyether urethane intermediate containing terminal non-cyclic urea/reactive silane groups, which is then reacted in the presence of a catalyst and heat to form polymers a).
The conversion of the non-cyclic urea groups into cyclic urea groups takes place according the following reaction
The reaction is carried out in the presence of a catalyst and heat. Suitable catalysts are Brønsted acids, such as mineral acids, carboxylic acids, sulfonic acids and phenols. Preferred catalysts are carboxylic acids, such as formic acid, acetic acid, propionic acid, 2-ethyl hexanoic acid, malonic acid, phthalic acid, and 1,2,3-tricarboxylic propane. Especially preferred 10 are acetic acid and 2-ethyl hexanoic acid.
Higher temperatures accelerate the conversion of the non-cyclic urea groups into cyclic urea groups. Suitable reaction temperatures are from 50 to 200° C. Very low temperatures require long reaction times and result in a very yellow product. Very high temperatures require only short reaction times, but also result in yellow products. The preferred range for minimizing the development of the yellow color is from 70 to 130° C., more preferably from 90 to 120° C. and most preferably from 100 to 120° C.
The conversion of non-cyclic urea groups into cyclic urea groups is accompanied by the release of a mole of alcohol from the succinyl ester. The generated alcohol and the catalyst can be removed from the reaction mixture, for example, by vacuum distillation, or they can be left in the product. If left in the product the released alcohols may undergo a transetherication reaction with the alkoxy groups on the silane. Whether the released alcohols are removed or not is of no consequence, since the products formed with or without vacuum purification, when formulated into a sealant or adhesive, undergo moisture cure to give cured compositions of equivalent performance.
The transetherification reaction can be used to alter the reactivity of the polyether urethanes according to the invention. For example, if a methoxysilane group is converted to an ethoxysilane group or a butoxysilane group, the reactivity of the resulting alkoxysilane groups will be substantially reduced. To the contrary if an ethoxysilane group or a butoxysilane group is converted to a methoxysilane group, the reactivity of the resulting alkoxysilane groups will be substantially increased.
Suitable aspartate silanes for prepareing polymers a) are those corresponding to formula I
wherein
Especially preferred are compounds in which X represents methoxy, ethoxy groups or propoxy groups, more preferably methoxy or ethoxy groups, and Y is a linear group containing 3 carbon atoms.
The compounds of formula I are prepared by reacting aminosilanes corresponding to formula II
H2N—Y—Si—(X)3 (II)
with maleic or fumaric acid esters corresponding to formula III
R5OOC—CR3═CR4—COOR2 (III)
Examples of suitable aminoalkyl alkoxysilanes and aminoalkyl acyloxysilanes corresponding to formula II include 3-aminopropyl-triacyloxysilane, 3-aminopropyl-methyldimethoxysilane; 6-aminohexyl-tributoxysilane; 3-aminopropyl-trimethoxysilane; 3-aminopropyl-triethoxysilane; 3-aminopropyl-methyldiethoxysilane; 5-aminopentyl-trimethoxysilane; 5-aminopentyl-triethoxysilane; 4-amino-3,3-dimethylbutyl-trimethoxysilane; and 3-aminopropyl-triisopropoxysilane. 3-aminopropyl-trimethoxysilane and 3-aminopropyl-triethoxysilane are particularly preferred.
Examples of optionally substituted maleic or fumaric acid esters suitable for preparing the aspartate silanes include the dimethyl, diethyl, dibutyl (e.g., di-n-butyl), diamyl, di-2-ethylhexyl esters and mixed esters based on mixture of these and/or other alkyl groups of maleic acid and fumaric acid; and the corresponding maleic and fumaric acid esters substituted by methyl in the 2- and/or 3-position. The dimethyl, diethyl and dibutyl esters of maleic acid are preferred, while the diethyl esters are especially preferred.
The reaction of primary amines with maleic or fumaric acid esters to form the aspartate silanes of formula III is known and described, e.g., in U.S. Pat. No. 5,364,955, which is herein incorporated by reference.
Suitable polyisocyanates which may be used to prepare polymers a) are known and include monomeric organic diisocyanates represented by the formula, R(NCO)2, in which R represents an organic group obtained by removing the isocyanate groups from an organic diisocyanate having a molecular weight of 112 to 1,000, preferably 140 to 400. Preferred diisocyanates are those represented by the above formula in which R represents a divalent aliphatic hydrocarbon group having from 4 to 18 carbon atoms, a divalent cycloaliphatic hydrocarbon group having from 5 to 15 carbon atoms, a divalent araliphatic hydrocarbon group having from 7 to 15 carbon atoms or a divalent aromatic hydrocarbon group having 6 to 15 carbon atoms.
Examples of suitable organic diisocyanates include 1,4-tetra-methylene diisocyanate, 1,6-hexamethylene diisocyanate, 2,2,4-trimethyl-1,6-hexamethylene diisocyanate, 1,12-dodecamethylene diisocyanate, cyclohexane-1,3- and -1,4-diisocyanate, 1-isocyanato-2-isocyanatomethyl cyclopentane, 1-isocyanato-3-isocyanatomethyl-3,5,5-trimethyl-cyclo-hexane (isophorone diisocyanate or IPDI), bis-(4-isocyanato-cyclohexyl)-methane, 1,3- and 1,4-bis-(isocyanatomethyl)-cyclohexane, bis-(4-iso-cyanatocyclo-hexyl)-methane, 2,4′-diisocyanato-dicyclohexyl methane, bis-(4-isocyanato-3-methyl-cyclohexyl)-methane, α,α,α′,α′-tetramethyl-1,3-and/or -1,4-xylylene diisocyanate, 1-isocyanato-1-methyl-4(3)-iso-cyanatomethyl cyclohexane, 2,4- and/or 2,6-hexahydro-toluylene diisocyanate, 1,3- and/or 1,4-phenylene diisocyanate, 2,4- and/or 2,6-toluylene diisocyanate, 2,4- and/or 4,4′-diphenylmethane diisocyanate and 1,5-diisocyanato naphthalene and mixtures thereof.
Monomeric polyisocyanates containing 3 or more isocyanate groups such as 4-isocyanatomethyl-1,8-octamethylene diisocyanate and aromatic polyisocyanates such as 4,4′,4″-triphenylmethane triisocyanate and polyphenyl polymethylene polyisocyanates obtained by phosgenating aniline/formaldehyde condensates may also be used. Also suitable, although less preferred, are polyisocyanate adducts prepared from the preceding monomeric polyisocyanates and containing isocyanurate, uretdione, biuret, urethane, allophanate, iminooxadiazine dione, carbodiimide and/or oxadiazinetrione groups.
Preferred diisocyanates include bis-(4-isocyanatocyclohexyl)-methane, 1,6-hexamethylene diisocyanate, isophorone diisocyanate, α,α,α′,α′-tetramethyl-1,3- and/or -1,4-xylylene diisocyanate, 2,4- and/or 2,6-toluylene diisocyanate, and 2,4- and/or 4,4′-diphenylmethane diisocyanate. Especially preferred are isophorone diisocyanate, 2,4-toluylene diisocyanate and mixtures of 2,4- and 2,6-toluylene diisocyanate.
Suitable polyols for preparing polymers a) are polyether polyols, in some cases polyoxypropylene polyols, in many instances diols, having a number average molecular weight of 3000 to 20,000, preferably 6000 to 15,000, and more preferably 8000 to 12,000. The polyethers can have a maximum total degree of unsaturation of less than 0.04 milliequivalents/g, in some cases less than 0.02 meq/g (meq/g), in other cases less than 0.01 meq/g and in some situations 0.007 meq/g or less. The amount of unsaturation will vary depending on the method used to prepare the polyether as well as the molecular weight of the polyerther. Such polyether diols are known and can be produced, as a non-limiting example, by the propoxylation of suitable starter molecules. As another non-limiting example, minor amounts (up to 20% by weight, based on the weight of the polyol) of ethylene oxide can be used. If ethylene oxide is used, it can be used as the initiator for or to cap the polypropylene oxide groups. Non-limiting examples of suitable starter molecules include diols such as ethylene glycol, propylene glycol, 1,3-butanediol, 1,4-butanediol, 1,6 hexanediol and 2-ethylhexanediol-1,3. Also suitable are polyethylene glycols and polypropylene glycols.
Suitable methods for preparing polyether polyols are known and are described, for example, in EP-A 283 148, U.S. Pat. No. 3,278,457, U.S. Pat. No. 3,427,256, U.S. Pat. No. 3,829,505, U.S. Pat. No. 4,472,560. U.S. Pat. No. 3,278,458, U.S. Pat. No. 3,427,334, U.S. Pat. No. 3,941,849, U.S. Pat. No. 4,721,818, U.S. Pat. No. 3,278,459, U.S. Pat. No. 3,427,335 and U.S. Pat. No. 4,355,188. They are preferably prepared using double metal cyanides as catalysts.
In addition to the polyether polyols, minor amounts (up to 20% by weight, based on the weight of the polyol) of low molecular weight dihydric and trihydric alcohols having a molecular weight 32 to 500 can also be used. Suitable examples include ethylene glycol, 1,3-butandiol, 1,4-butandiol, 1,6-hexandiol, glycerine or trimethylolpropane. However, the use of low molecular weight alcohols is less preferred.
It is also possible in accordance with the present invention to use aminopolyethers instead of the polyether polyols. The aminopolyethers may be prepared by aminating the corresponding polyether polyols in known manner.
When preparing polymers a) from a diisocyanate, a diol and an aspartate silane, the diisocyanate is reacted with the diol at an equivalent ratio of isocyanate groups to hydroxyl groups of approximately 2:1 to form an NCO prepolymer. In addition to the 2/1 adduct of the diisocyanate and diol, minor amounts of higher molecular weight oligomers are also formed, such as the 3/2 adduct, etc. When these oligomers are formed, the reaction mixture also contains a minor amount of unreacted diisocyanate, which can be removed, e.g., by distillation, or which can remain in the reaction mixture.
The NCO prepolymer is then reacted with the aspartate silane at an equivalent ratio of isocyanate groups to amino groups of approximately 1:1. The resulting polyether urethane intermediate a) contains the reaction products of the NCO prepolymers with the aspartate silanes and optionally polymers c), which are the reaction products of monomeric diisocyanates with the aspartate silanes. Polymers c) are preferably present in an amount of less then 2% by weight, more preferably less than 1% by weight, based on the weight of polyether urethane a). When polymers c) are present, they are preferably present in an amount of at least 0. 1% by weight, more preferably at least 0.5% by weight, based on the weight of polyether urethane a).
Similarly to polymers a), polymers b) also contain one or more polyether segments, but they only contain one reactive silane group. Polymers b) may be prepared by several methods. For example, they may be prepared by reacting a high molecular weight polyether containing one isocyanate-reactive group, preferably a hydroxyl group, with an excess of a polyisocyanate, preferably a diisocyanate. The amount of the isocyanate and polyether is chosen such that the resulting product contains one isocyanate group.
For example, when reacting a diisocyanate with a monool using equimolar mixtures of the reactants, the resulting product contains an average of one isocyanate group. In addition to the monoisocyanate intermediate, which is the 1/1 adduct of the monool and diisocyanate, the reaction mixture also contains minor amounts of non-functional polymers d), which are formed by the reaction of two molecules of the monool with one molecule of the diisocyanate. The reaction mixture may also contain a minor amount of unreacted diisocyanate, which can be removed, e.g., by distillation, or which can remain in the reaction mixture.
In accordance with the present invention it is also possible to react additional quantities of the monool with the diisocyanate. When the reaction is carried out in this manner, additional amounts of non-functional polymers d) are formed. These polymers remain in the reaction mixture and function as plasticizers during the subsequent use of the moisture-curable, polyether urethanes according to the invention.
The reaction mixture containing the monoisocyanate intermediate is reacted with a compound containing an isocyanate-reactive group, preferably an —NH group, and one or more, preferably one reactive silane group to form polyether urethane b). The reaction mixture also contains polymers e), which are the reaction products of any monomeric diisocyanates present in the reaction mixture with the isocyanate-reactive silanes. Polymers e) are considered a part of polyether urethane b), even though they contain two reactive silane groups.
Non-functional polymers d) are preferably present in an amount of less than 60% by weight, more preferably less than 30% by weight and most preferably less than 10% by weight, based on the weight of polyether urethane b). When polymers d) are present, they are preferably present in an amount of at least 0.1% by weight, more preferably at least 0.5% by weight.
Polymers e) are preferably present in an amount of less then 2% by weight, more preferably less than 1% by weight, based on the weight of polyether urethane b). When polymers e) are present, they are preferably present in an amount of at least 0.1% by weight and more preferably at least 0.5% by weight, based on the weight of polyether urethane a).
Polymers b) may also be prepared by reversing these steps and reacting an excess of a polyisocyanate with an isocyanate-reactive silane and then reacting the resulting intermediate with the high molecular weight polyether. Mixtures of polymers b), d) and e) will also be formed when the process steps are carried out in this order.
Suitable polyisocyanates for preparing the polymers b) are those previously set forth as suitable for preparing polymers a). Monomeric diisocyanates are preferred. Also suitable are the difunctional NCO prepolymers previously set forth for preparing polymers a). If the NCO prepolymer contains high molecular weight polyether segments, then low molecular weight monools can also be used to prepare the previously described monoisocyanate intermediates.
Suitable monools for preparing polymers b) are polyether monools having a number average molecular weight of 1000 to 15,000, preferably 3000 to 12,000 and more preferably 6000 to 12,000. The polyether monools are prepared by the alkoxylation of monofunctional starting compounds with alkylene oxides, preferably ethylene oxide, propylene oxide or butylene oxide, more preferably propylene oxide. If ethylene oxide is used, it is used in an amount of up to 40% by weight, based on the weight of the polyether. The polyethers are preferably prepared either by the KOH process or by mixed metal cyanide catalysis. The latter process results in products with low a degree of unsaturation.
In many cases, the polyethers, which as a non-limiting example can be polypropylene oxide polyethers have a maximum total degree of unsaturation of less than 0.04 milliequivalents/g (meq/g) in some cases less than 0.02 meq/g, in other cases less than 0.01 meq/g and in some situations 0.007 meq/g or less. The amount of unsaturation will vary depending on the method used to prepare the polyether as well as the molecular weight of the polyerther. Such polyether monools are known and can be produced, as a non-limiting example by the methods set forth previously for preparing polyethers, a non-limiting example being the polyoxypropylene polyols by the propoxylation of suitable starter molecules. In another non-limiting example, minor amounts (up to 20% by weight, based on the weight of the polyol) of ethylene oxide can also be used. As with the polyethers a-i), if ethylene oxide is used, it can be used as the initiator for or to cap the polypropylene oxide groups.
Examples of suitable starter molecules include aliphatic, cycloaliphatic and araliphatic alcohols, phenol and substituted phenols, such as methanol, ethanol, the isomeric propanols, butanols, pentanols and hexanols, cyclohexanol and higher molecular weight compounds such as nonylphenol, 2-ethylhexanol and a mixture of C12 to C15, linear, primary alcohols (Neodol 25, available from Shell). Also suitable are unsaturated alcohols such as allyl alcohol; and hydroxy functional esters such as hydroxyethyl acetate and hydroxyethyl acrylate. Preferred are the higher molecular weight monohydroxy compounds, especially nonyl phenol and mixtures of C12 to C15, linear, primary alcohols.
It is also possible in accordance with the present invention to use monoaminopolyethers instead of the polyether monools. These aminopolyethers may be prepared by aminating the corresponding polyether monools in known manner.
Suitable isocyanate-reactive silanes for use in preparing polymers b) by the preceding processes include those corresponding to the formula
wherein
Examples of suitable aminoalkyl alkoxysilanes and aminoalkyl acyloxysilanes of formula IV, which contain primary amino groups, are the compounds of formula 11 that have previously been described as suitable for preparing the aspartate silanes of formula I.
Examples of suitable aminoalkyl alkoxysilanes and aminoalkyl acyloxysilanes of formula IV, which contain secondary amino groups, include the previously disclosed aspartate silanes corresponding to formula I and also N-phenylaminopropyl-trimethoxysilane (available as A-9669 from OSI Corporation), bis-(γ-trimethoxysilylpropyl)amine (available as A-1170 from OSI Corporation), N-cyclohexylaminopropyl-triethoxy-silane, N-methylaminopropyl-trimethoxysilane, N-butylamino-propyl-trimethoxysilane, N-butylaminopropyl-triacyloxysilane, 3-(N-ethyl)amino-2-methylpropyl-trimethoxysilane, 4-(N-ethyl)amino-3,3-dimethylbutyl-trimethoxysilane and the corresponding alkyl diethoxy, alkyl dimethoxy and alkyl diacyloxysilanes, such as 3-(N-ethyl)amino-2-methyl-propyl-methyldimethoxysilane.
It is also possible to prepare polymers b) by reacting the polyether in one step with a compound containing isocyanate and alkoxysilane groups corresponding to formula VI
OCN—Y—Si—(X)3 (VI)
wherein X and Y are as previously defined.
Examples of suitable isocyanatosilanes include 3-isocyanatopropyl-methyldimethoxysilane, 3-isocyanatopropyl-trimethoxysilane and 3-isocyanatopropyl-triethoxysilane. 3-isocyanatopropyl-trimethoxysilane (Silquest Y-5187, available from OSI Corporation) is especially preferred.
When the compounds of formula VI are reacted with a polyether monool to prepare polymers b), then polymers c) and d) are not formed.
Instead of using an aminosilane, it is also possible to prepare polyether urethanes b) by using the hydroxy compound obtained by reacting an aminosilane with a cyclic carbonate such as ethylene or propylene carbonate. The aminosilane may also be replaced with the corresponding thiosilane or the monofunctional adduct of an isocyanatosilane of formula VI with a diol or a diamine.
In accordance with another embodiment of the present invention it is possible to avoid the need for separately preparing a high molecular weight polyether monool by converting a high molecular weight polyether diol into a monool by reacting it with a monoisocyanate. A further alternative for preparing a polyether monool is to react one mole of a diol with a monoacid chloride. Another method for preparing a high molecular weight monool is to react one mole of a monool and one mole of a diol with one mole of a diisocyanate. Either or both of the monool and diol may contain high molecular weight polyether segments. The polyether monools obtained from these processes can then be used to prepare polymers b) using the previously described processes.
If two moles of a diisocyanate are used in the last process, then the resulting product is a monoisocyanate that can be reacted with an isocyanate-reactive compound containing an alkoxysilane group to form polymers b). Another method for forming this monoisocyanate is to react an NCO prepolymer, such as those previously described for preparing polymers a), with a monoalcohol.
The polyether monoamines, which have also been described as suitable for preparing polymers b), can be reacted in the same manner as the polyether monools. In addition, they can also be reacted with epoxy silanes to form polymers b).
In another embodiment a polyether monool is prepared by the alkoxylation of a hydroxyalkyl (meth)acrylate. The resulting polyether monool is reacted with a monoisocyanate to form an unsaturated intermediate. This intermediate is then reacted with an aminosilane or a thiosilane to incorporate silane groups by a Michael addition.
In accordance with a final embodiment of the present invention it is possible to prepare polyether urethanes a) and b) in one step by reacting a mixture of polyether monools and polyether diols with the diisocyanates. Preferably, one mole of diisocyanate is present for each equivalent of hydroxyl groups. The resulting product contains a mixture of NCO prepolymers, monoisocyanate intermediates, non-functional polymers d) and unreacted diisocyanate. The reaction mixture is then reacted with the aspartate silane, which is required to prepare polyether urethanes a), to form a mixture of polyether urethane intermediates a) and b), non-functional polymers d) and polymers c) and e).
When aspartate silane groups are reacted with isocyanate groups to form polymers b), a polyether urethane intermediate is obtained which contains terminal non-cyclic urea/reactive silane groups. These terminal groups can be converted to cyclic urea/reactive silane groups in the same manner as previously described for polymers a). It is also possible in accordance with the present invention to mix the polyether urethane intermediates for polymers a) and b) and convert the non-cyclic urea groups to cyclic urea groups at the same time. The non-cyclic urea groups may also be converted to cyclic urea groups at the same time when the mixture of polyether urethane intermediates is prepared in one step as described in the preceding paragraph.
The compositions of the present invention may be cured in the presence of water or moisture to prepare coatings, adhesives or sealants. The compositions cure by “silane polycondensation” from the hydrolysis of alkoxysilane groups to form Si—OH groups and their subsequent reaction with either Si—OH or Si—OR groups to form siloxane groups (Si—O—Si).
Suitable acidic or basis catalysts may be used to promote the curing reaction. Examples include acids such as paratoluene sulfonic acid; metallic salts such as dibutyl tin dilaurate; tertiary amines such as triethylamine or triethylene diamine; and mixtures of these catalysts. The previously disclosed, low molecular weight, basic aminoalkyl trialkoxy-silanes, also accelerate hardening of the compounds according to the invention.
The one-component compositions generally may be either solvent-free or contain up to 70%, preferably up to 60% organic solvents, based on the weight of the one-component composition, depending upon the particular application. Suitable organic solvents include those which are known from either from polyurethane chemistry or from coatings chemistry.
The compositions may also contain known additives, such as leveling agents, wetting agents, flow control agents, antiskinning agents, antifoaming agents, fillers (such as chalk, lime, flour, precipated and/or pyrogenic silica, aluminum silicates and high-boiling waxes), viscosity regulators, plasticizers, pigments, dyes, UV absorbers and stabilizers against thermal and oxidative degradation.
The one-component compositions may be used with any desired substrates, such as wood, plastics, leather, paper, textiles, glass, ceramics, plaster, masonry, metals and concrete. They may be applied by standard methods, such as spraying, spreading, flooding, casting, dipping, rolling and extrusion.
The one-component compositions may be cured at ambient temperature or at elevated temperatures. Preferably, the moisture-curable compositions are cured at ambient temperatures.
The invention is further illustrated but is not intended to be limited by the following examples in which all pars and percentages are by weight unless otherwise specified.
An aspartate resin was prepared according to U.S. Pat. No. 4,364,955. To a 5 liter flask fitted with agitator, thermocouple, nitrogen inlet and addition funnel with condenser were added 1483 g (8.27 equivalents) of 3-amino-propyl-trimethoxysilane (Silquest A-1110, available from OSI Corporation). The addition funnel was used to admit 1423.2 g (8.27 equivalents) of diethyl maleate over a two hour period. The temperature of the reactor was maintained at 25° C. during the addition. The reactor was maintained at 25° C. for an additional five hours at which time the product was poured into glass containers and sealed under a blanket of nitrogen. After one week the unsaturation number was 0.6 indicating the reaction was ˜99% complete.
Polyether diol 1
A polyoxypropylene diol (Acclaim 12200, unsaturation=0.007 meq/g available from Bayer Corporation) having a functionality of 2 and an equivalent weight of 5783.
Polyether monool 2
203 g (1.00 eq) of Neodol 25 monool (available from Shell Chemical) were charged to a stainless-steel reactor. Zinc hexacyanocobaltate-tert-butyl alcohol complex (0.143 g, prepared as described in U.S. Pat. No. 5,482,908) was added and the mixture was heated with stirring under vacuum at 130° C. for one hour to remove traces of water from the monool starter. Propylene oxide (8547 g, 194.2 eq) was introduced into the reactor over 6 hours. After the epoxide addition was completed, the mixture was heated to 130° C. until no further pressure decrease occurred. The product was vacuum stripped and then drained from the reactor. The resulting polyether had an OH number of 6.4, an equivalent weight of 8750, a functionality of 1, and an unsaturation of less than meq/g.
A 5 liter round bottom flask was fitted with agitator, nitrogen inlet, condenser, heater and addition funnel. Into the flask were charged 127.9 g (1.15 eq) of isophorone diisocyanate, 2691.6 g (0.47 eq) of polyether diol 1, 946.7 g (0.11 eq) of polyether monool 2 and 0.78 g of dibutyltin dilaurate. The reaction was heated to 60° C. for 8 hours until the NCO content was 0.58% (theoretical=0.63%). 202.2 g (0.55 eq) of silane functional aspartate 1 were added and the flask was heated at 60° C. for an additional 1 hour until no NCO remained as determined by an IR spectrum. 19.9 g of glacial acetic acid were added and the temperature was raised to 11 0° C. The reaction mixture was held at 110° C. for three hours until an IR spectrum showed the urea peak had disappeared and a cyclic urea peak had appeared. 19.8 g of vinyl trimethoxysilane were added as moisture scavenger; and 9.9 g of butylated hydroxy toluene and 6.1 g of Naugard 445 (available from Crompton) were added as antioxidants. The resulting product had a viscosity of 54,000 mPa.s at 25° C.
A 3 liter round bottom flask was fitted with agitator, nitrogen inlet, condenser, heater and addition funnel. Into the flask were charged 80.0 g (0.72 eq) of isophorone diisocyanate, 1680.4 g (0.31 eq) of polyether diol 1,591.7 g (0.07 eq) of polyether monool 2 and 0.53 g of dibutyltin dilaurate. The reaction was heated to 60° C. for 8 hours until the NCO content was 0.60% (theoretical=0.62%). 126.4 g (0.34 eq) of silane functional aspartate 1 were added and the flask was heated at 60° C. for an additional 1 hour until no NCO remained as determined by an IR spectrum. 5.5 g of vinyl trimethoxysilane were added as moisture scavenger; and 6.2 g of butylated hydroxy toluene and 3.7 g Naugard 445 (available from Crompton) were added as antioxidants. The resulting product had a viscosity of 34,700 mPa·s at 25° C.
Heat Aging of Silanes
Into unlined steel cans were placed 300 g of silane. Four cans of each resin were placed into a 90° C. oven. One can of each resin was removed each week and the viscosities were determined. The following table sets forth the change in viscosity over the testing period.
Formulation of Silane Sealants
The STP's were formulated into sealants using the following typical formulation and procedure. The difunctional STP's were formulated alone and in combination with the monofunctional STP's to demonstrate the effects of these combinations.
Procedure
The following is the standard sealant/adhesive formulation and procedure used to formulate all diol and diol/monool blends. Values given for each formula component are percent by weight of the total formula weight. A high-speed centrifugal mixer was used to mix the formulation components in the steps given below. Each mixing period was one minute in length at a speed of 2200 rpm.
To a clean dry mixing container were charged the following:
A portion of the filler was added to the mixing container.
The remaining filler was added to the mixing container.
Exxon Jayflex DIDP was used as the plasticizer. An aminosilane (Silquest A-1120, available from OSI Corporation) was used as the adhesion promoter. A vinyltrimethoxysilane (Silquest A-171, available from OSI Corporation) was used as the desiccant. The filler used was Specialty Minerals Ultra P Flex precipitated calcium carbonate (mean particle size of 0.07 microns). The catalyst used was dibutyltin dilaurate.
Cure and Testing of Silane Sealants
The sealant formulations were cast onto 0.25 inch thick polyethylene sheets and cured at standard conditions of 20° C., 50% relative humidity for at least two weeks before testing. Tensile strength, percent elongation and 100% modulus were determined according to ASTM D-412. Die “C” tear strengths were determined according to ASTM D-624. The results are set forth in the following table.
The sealant properties of the preceding examples demonstrate that the polyether urethanes containing terminal cyclic urea/reactive silane groups according to the invention are more heat stable than the comparitive polyether urethanes containing terminal non-cyclic urea/reactive silane groups.
Although the invention had been described in detail in the foregoing for the purpose of illustration, it was to be understood that such detail was solely for that purpose and that variations can be made therein by those skilled in the art without departing from the spirit and scope of the invention except as it may be limited by the claims.
| Number | Date | Country | Kind |
|---|---|---|---|
| 10325029 | Dec 2002 | US | national |
| Filing Document | Filing Date | Country | Kind | 371c Date |
|---|---|---|---|---|
| PCT/US03/38710 | 12/5/2003 | WO | 6/17/2005 |
