Patent Application
20120009414
1. Field of the Invention
This invention relates to polyurethane and polyisocyanurate foams. More particularly, it relates to such foams prepared from aromatic polyester polyols that show improved processability over a range of thicknesses, and also improved fire behavior. 2. Background of the Art
Polyurethane and polyisocyanurate foams are widely used as insulating materials in the construction industry. Typically these foams are closed-cell, rigid foams containing within the cells a low-conductivity gas, such as a hydrocarbon (HC). The foaming compositions, being liquids, may be used in pour-in-place applications; sprayed applications; and to form rigid foam boards or panels. The panels, which may be produced via continuous or discontinuous process technology, may include a facing, such as a metal foil, to which the foam adheres. These panels may be referred to as sandwich panels.
Unfortunately, these foams, which are frequently formed from polyester polyols and methylene diphenyl diisocyanate (MDI) at an MDI/polyol ratio over 150, may suffer from drawbacks. One frequent problem is that the foams may exhibit poor curing performance, resulting in defects such as shrinkage and deformation. Another problem may relate to fire behavior, as official testing requirements become ever more stringent. One example of a more stringent requirement are new Euroclasses regulations, such as EN 13823.
For many polyurethane and polyisocyanurate foams, the polyester polyol employed is an aromatic-based structure. While such foams have many uses, it has been found that inclusion of at least some aliphatic polyester polyol may offer benefits. For example, US 2006/0047011 A1 discloses that polyisocyanurate foams prepared from aliphatic polyester polyols may exhibit improved flame resistance, lower thermal conductivity, reduced brittleness and improved surface adhesion. Low viscosity enables potential use in spray foams. The aliphatic polyols used therein are based on a combination of adipic, glutaric, succinic and nitric acids with water, esterified with ethylene glycol. These polyols have hydroxyl (OH) numbers of greater than 200 and viscosities in the range of 2,000 mPa*s.
In another example, a combination of aliphatic and aromatic polyester polyols is described in US 2001/0003758 as useful for preparing rigid isocyanurate-modified polyurethane foams. The foams have an isocyanate index ranging from 80 to 380.
Notwithstanding the above-described art, there is still a need for polyurethane and polyisocyanurate foams exhibiting improvements in curing and fire behavior performance. These and other features may be found in the present invention.
In one aspect the invention provides polyurethane or polyisocyanurate foam formulation comprising (a) a formulated polyol comprising (i) from about 20 to about 60 percent by weight of an aromatic polyester polyol having a hydroxyl number greater than about 50 mg KOH/g and a functionality equal to or greater than about 2; (ii) from about 10 to about 30 percent by weight of a Novolac-type polyether polyol; and (iii) from about 5 to about 40 percent by weight of a sucrose- or sorbitol-initiated polyol having a hydroxyl number greater than about 200 mg KOH/g and a functionality of at least about 4; all percentages being based upon the formulated polyol as a whole; (b) a polyisocyanate; and (c) a blowing agent; such that the stoichiometric index of the isocyanate to the formulated polyol is from about 100 to about 250; and wherein the foam formulation is suitable for preparing a polyurethane or polyisocyanurate foam showing processability and fire behavior that are improved in comparison with polyurethane or polyisocyanurate foams prepared from foam formulations that are the same except for the formulated polyol. The invention includes the formulated polyol and a foam made from the given formulation.
In another aspect the invention provides a method of preparing a polyurethane or polyisocyanurate foam comprising contacting under foam-forming conditions (a) a formulated polyol comprising (i) from about 20 to about 60 percent by weight of an aromatic polyester polyol having a hydroxyl number greater than about 50 mg KOH/g and a functionality equal to or greater than about 2; (ii) from about 10 to about 30 percent by weight of a Novolac-type polyether polyol; (iii) from about 5 to about 40 percent by weight of a sucrose- or sorbitol-initiated polyol having a hydroxyl number greater than about 200 mg KOH/g and a functionality of at least about 4; all percentages being based upon the formulated polyol as a whole; (b) a polyisocyanate; and (c) a blowing agent; at an isocyanate index ranging from about 100 to about 250; to form a rigid polyurethane or polyisocyanurate foam. The invention also includes a foam prepared by this method.
The invention offers both process and property improvements that are advantageous in the polyurethane and polyisocyanurate industry. As used herein, the term “polyisocyanurate” includes both polyisocyanurate foams and urethane-modified polyisocyanurate (PU-PIR) foams.
The first component is an aromatic polyester polyol. As used herein, “aromatic” refers to organic compounds having at least one conjugated ring of alternate single and double bonds, which imparts an overall stability to the compounds. The term “polyester polyol” as used herein includes any minor amounts of unreacted polyol remaining after the preparation of the polyester polyol and/or unesterified polyol (for example, glycol) added after the preparation of the polyester polyol. While the aromatic polyester polyol may be prepared from substantially pure reactant materials, more complex starting materials, such as polyethylene terephthalate, may be advantageous. Other residues are dimethyl terephthalate (DMT) process residues, which are waste or scrap residues from the manufacture of DMT.
The aromatic polyester polyol may optionally contain, for example, halogen atoms and/or may be unsaturated, and may generally be prepared from the same selection of starting materials as described hereinabove, but at least one of the polyol or the polycarboxylic acid, preferably the acid, is an aromatic compound having an aromatic ring content (expressed as weight percent of groups containing at least one aromatic ring per molecule) that is at least about 50 percent by weight, based on the total compound weight, and preferably greater than about 50 percent by weight, i.e., it is predominantly aromatic in nature. Polyester polyols having an acid component that advantageously comprises at least about 30 percent by weight of phthalic acid residues, or residues of isomers thereof, are particularly useful. Preferably the aromatic ring content of the aromatic polyester polyol is from about 70 to about 90 percent by weight, based on the total compound weight. Preferred aromatic polyester polyols are the crude polyester polyols obtained by the transesterification of crude reaction residues or scrap polyester resins.
The aromatic polyester polyol is also characterized in that it has a hydroxyl number of greater than about 50 mg KOH/g, and in certain embodiments a functionality that is equal to or greater than about 2. In preferred embodiments, the hydroxyl number ranges from greater than about 50 to about 400 mg KOH/g, and in more preferred embodiments the hydroxyl number ranges from about 150 to about 300 mg KOH/g. The functionality may range from about 1.5 to about 8, but in certain non-limiting embodiments may range from about 2 to about 8, and in still other non-limiting embodiments may range from about 2 to about 6.
The second component is a Novolac-type polyether polyol. Novolac-type polyether polyols are the alkoxylation products of a phenol-formaldehyde resin, which is formed by the elimination reaction of phenol with formaldehyde in the presence of an acid catalyst, such as glacial acetic acid, followed by concentrated hydrochloric acid. Usually a small amount of the acid catalyst or catalysts is/are added to a miscible phenol, such as p-toluenesulfonic acid, followed by formaldehyde. The formaldehyde will react between two phenols to form a methylene bridge, creating a dimer by electrophilic aromatic substitution between the ortho and para positions of phenol and the protonated formaldehyde. This dimer is bisphenol F. Another example is bisphenol A, which is the condensation product of acetone with two phenols. As concentration of dimers increase, trimers, tetramers and higher oligomers may also form. However, because the molar ratio of formaldehyde to phenol is controlled at somewhat less than 1, polymerization is not completed. Thus, the Novolac may then be alkoxylated to build molecular weight to a desired level, desirably from about 300 to about 1500, and in certain non-limiting embodiments, from about 400 to about 1000.
Phenols which may be used to prepare the Novolac initiator include: o-, m-, or p-cresols, ethylphenol, nonylphenol, p-phenylphenol, 2,2-bis(4-hydroxyphenol) propane, beta-naphthol, beta-hydroxyanthracene, p-chlorophenol, o-bromophenol, 2,6-dichloro-phenol, p-nitrophenol, 4-nitro-6-phenylphenol, 2-nitro-4-methylphenol, 3,5-dimethylphenol, p-isopropylphenol, 2-bromo-4-cyclohexylphenol, 4-t-butylphenol, 2-methyl-4-bromophenol, 2-(2-hydroxypropyl)phenol, 2-(4-hydroxyphenol)ethanol, 2-carbethoxyphenol, 4-chloro-methylphenol, and mixtures thereof. It is especially preferred that the phenols used to prepare the Novolac-type polyether polyols be unsubstituted.
Suitable Novolac-type polyether polyols may be produced, for example, by reacting a condensate adduct of phenol and formaldehyde with one or more alkylene oxides including ethylene oxide, propylene oxide, and butylene oxide. Such polyols, sometimes referred to as Novolac-initiated polyols, are known to those skilled in the art, and may be obtained by methods such as are disclosed in, for example, U.S. Pat. Nos. 2,838,473; 2,938,884; 3,470,118; 3,686,101; and 4,046,721; the disclosures of which are incorporated herein by reference in their entireties. Typically, Novolac starting materials are prepared by reacting a phenol (for example, a cresol) with from about 0.8 to about 1.5 moles of formaldehyde per mole of the phenol in the presence of an acidic catalyst to form a polynuclear condensation product containing from 2.1 to 12, preferably from 2.2 to 6, and more preferably from 3 to 5 phenol units per molecule. The Novolac resin is then reacted with an alkylene oxide such as ethylene oxide, propylene oxide, butylene oxide, or isobutylene oxide to form an oxyalkylated product containing a plurality of hydroxyl groups. For the purpose of the present invention, preferred Novolac polyols are those having an average of from 3 to 6 hydroxyl moieties per molecule and an average hydroxyl number of from about 100 to about 500 mg KOH/g, preferably from about 100 to about 300 mg KOH/g.
A third required component of the formulated polyol is a sucrose- or sorbitol-initiated polyol. This polyol is a polyether polyol, and may have a hydroxyl number of greater than about 200 mg KOH/g and a functionality of at least about 4. Even higher functionality, ranging from about 4.5 to about 6.0, may be particularly desirable in some embodiments.
Sucrose may be obtained from sugar cane or sugar beets, honey, sorghum, sugar maple, fruit, and the like. Means of extraction, separation, and preparation of the sucrose component vary depending upon the source, but are widely known and practiced on a commercial scale by those skilled in the art.
Sorbitol may be obtained via the hydrogenation of D-glucose over a suitable hydrogenation catalyst. Fixed beds and similar types of equipment are especially useful for this reaction. Suitable catalysts may include, for example, Raney™ (Grace-Davison) catalysts, such as employed in Wen, Jian-Ping, et. al., “Preparation of sorbitol from D-glucose hydrogenation in gas-liquid-solid three-phase flow airlift loop reactor,” The Journal of Chemical Technology and Biotechnology, vol. 4, pp. 403-406 (Wiley Interscience, 2004), incorporated herein by reference in its entirety. Nickel-aluminum and ruthenium-carbon catalysts are just two of the many possible catalysts.
In an alternative embodiment, preparation of sorbitol may begin with a starch hydrolysate which has been hydrogenated. The starch is a natural material derived from corn, wheat and other starch-producing plants. To form the hydrolysate, the starch polymer molecule may be broken into smaller oligomers at the ether bond between glucose rings, to produce glucose, maltose and higher molecular weight oligo- and poly-saccharides. The resulting molecules, having hemiacetal glucose rings as end units, may then be hydrogenated to form sorbitol, maltitol and hydrogenated oligo- and poly-saccharides. Hydrogenated starch hydrolysates are commercially available and inexpensive, often in the form of syrups, and provide the added benefit of being a renewable resource. This method may further require a separation of either the glucose, prior to hydrogenation, or of the sorbitol after hydrogenation, in order to prepare a suitable sorbitol-initiated polyol therefrom. In general, the hydrogenation reduces or eliminates the end units' tendency to form the hydroxyaldehyde form of glucose. Therefore, fewer side reactions of the sorbitol, such as Aldol condensation and Cannizzaro reactions, may be encountered. Furthermore, the final polyol will comprise reduced amounts of by-products.
The sucrose- or sorbitol-initiated polyol may be made by polymerizing alkylene oxides onto the specified initiator in the presence of a suitable catalyst. In one embodiment, each of the initiators may be individually alkoxylated in separate reactions and the resulting polyols blended to achieve the desired component of the formulated polyol. In another embodiment, the initiators may be mixed together prior to alkoxylation, thereby serving as co-initiators, prior to preparing the polyol component having a target hydroxyl number and functionality.
To accomplish the alkoxylation, the alkylene oxide or mixture of alkylene oxides may be added to the initiator(s) in any order, and can be added in any number of increments or added continuously. Adding more than one alkylene oxide to the reactor at a time results in a block having a random distribution of the alkylene oxide molecules, a so-called heteric block. To make a block polyoxy-alkylene of a selected alkylene oxide, a first charge of alkylene oxide is added to an initiator molecule in a reaction vessel. After the first charge, a second charge can be added and the reaction can go to completion. Where the first charge and the second charge have different relative compositions of alkylene oxides, the result is a block polyoxyalkylene. It is preferred to make block polyols in this fashion where the blocks thus formed are either all ethylene oxide, or all propylene oxide, or all butylene oxide, but intermediate compositions are also possible. The blocks can be added in any order, and there may be any number of blocks. For example, it is possible to add a first block of ethylene oxide, followed by a second block of propylene oxide. Alternatively, a first block of propylene oxide may be added, followed by a block of ethylene oxide. Third and subsequent blocks may also be added. The composition of all the blocks is to be chosen so as to give the final material the properties required for its intended application.
Also included in the polyol composition is a chemical blowing agent, which may be selected based in part upon the desired density of the final foam. In certain non-limiting embodiments hydrocarbon blowing agents may be selected. For example, hydrocarbon or fluorine-containing hydrohalocarbon blowing agents may be used, and in some instances may serve to reduce, or further reduce, viscosity, and thereby to enhance sprayability. Among these are, for example, butane, isobutane, 2,3-dimethylbutane, n- and i-pentane isomers, hexane isomers, heptane isomers, cycloalkanes including cyclopentane, cyclohexane, cycloheptane, and combinations thereof, HFC-245fa (1,1,1,3,3-pentafluoropropane), HFC-365mfc (1,1,1,3,3-penta-fluorobutane), HFC-227ea (1,1,1,2,3,3,3-heptafluoropropane), HFC-134a (1,1,1,2-tetrafluoroethane), combinations of two or more of the above, and the like. These hydrocarbons and/or non-fluorine-containing hydrohalocarbons are preferably used in an amount such that the total blowing agent, including the hydrofluorocarbon, is no more than about 15 parts, more desirably no more than about 10 parts, based on 100 parts of the total polyol composition.
An optional chemical blowing agent that may be selected is formic acid or another carboxylic acid. The formic acid may be used in an amount of from about 0.5 to about 8 parts per 100 parts by weight of the polyol composition. In certain non-limiting embodiments, the formic acid is present in an amount from about 0.5 parts and more preferably from about 1 part, up to about 6 parts and more preferably to about 3.5 parts by weight. While formic acid is the carboxylic acid of preference, it is also contemplated that minor amounts of other aliphatic mono- and polycarboxylic acids may be employed, such as those disclosed in U.S. Pat. No. 5,143,945, which is incorporated herein by reference in its entirety, and including isobutyric acid, ethylbutyric acid, ethylhexanoic acid, and combinations thereof.
In addition to, or in lieu of, the formic acid or other carboxylic acid blowing agent, water may also be optionally selected as a chemical blowing agent. The water is, in some non-limiting embodiments, present in an amount of from about 0.5 to about 10 parts, and preferably from about 1 to about 6 parts, per 100 parts by weight of the formulated polyol. When preparing a polyurethane or polyisocyanurate foam, in order to facilitate and give desirable processing characteristics, it is advantageous not to exceed 4 parts of water, preferably not more than 2.5 parts of water, and more preferably not more than 1.5 parts of water, per 100 parts of polyol composition. Omission of water is desirable in some non-limiting embodiments.
Finally, carbamates, which release carbon dioxide during the foaming process, and their adducts may also be used advantageously as an optional, additional chemical blowing agent. Such are discussed in greater detail in, for example, U.S. Pat. Nos. 5,789,451 and 6,316,662, and EP 1 097 954, which are incorporated herein by reference in their entireties.
The three minimum required components of the formulated polyol (not including blowing agent(s)) are, in certain non-limiting embodiments, present in specific proportion ranges in order to improve their storage stability after they are combined. While the aromatic polyester polyol may range from about 20 to about 60 percent by weight, based on the weight of the formulated polyol as a whole, the Novolac-type polyether polyol may range from about 10 to about 30 weight percent by weight, preferably from about 20 to about 30 percent by weight. It is desirable in some embodiments that the aromatic polyester polyol be limited to a range from about 20 to about 40 percent by weight. The sucrose- or sorbitol-initiated polyol is desirably present in an amount ranging from about 5 to about 40 percent by weight, on the same basis. Combinations of more than one of each type of polyol may also be selected, provided their combined percentages in the formulated polyol as a whole comply with the stated ranges. The hydrocarbon or hydrohalocarbon blowing agent, whether included in the formulated polyol or introduced separately during the foam preparation, is desirably present in an amount from about 2 to about 15 parts, based on 100 parts of the formulated polyol, and more desirably in an amount from about 4 to about 10 parts on the same basis.
In order to prepare a polyisocyanurate foam, it is necessary to react the polyol composition with a polyisocyanate component under appropriate foam-forming conditions. The polyisocyanate component is referred to in the United States as the “A-component” (in Europe, as the “B-component”). Selection of the A-component may be made from a wide variety of polyisocyanates, including but not limited to those that are well known to those skilled in the art. For example, organic polyisocyanates, modified polyisocyanates, isocyanate-based prepolymers, and mixtures thereof may be employed. These may further include aliphatic and cycloaliphatic isocyanates, and in particular aromatic and, more particularly, multifunctional aromatic isocyanates. Also particularly preferred are polyphenyl polymethylene polyisocyanates (PMDI).
Other polyisocyanates useful in the present invention include 2,4- and 2,6-toluenediisocyanate and the corresponding isomeric mixtures; 4,4′-, 2,4′- and 2,2′-diphenyl-methanediisocyanate and the corresponding isomeric mixtures; mixtures of 4,4′-, 2,4′- and 2,2′-diphenyl-methanediisocyanates and polyphenyl polymethylene polyisocyanates (PMDI); and mixtures of PMDI and toluene diisocyanates. Also useful herein are aliphatic and cycloaliphatic isocyanate compounds, such as 1,6-hexamethylenediisocyanate;1-isocyanato-3,5,5-trimethyl-1,3-isocyaantomethylcyclo-hexane; 2,4- and 2,6-hexahydrotoluene-diisocyanate and their corresponding isomeric mixtures; and 4,4′-, 2,2′- and 2,4′-dicyclohexyl-methanediisocyanate and their corresponding isomeric mixtures. Also useful in the present invention is 1,3-tetra-methylene xylene diisocyanate.
Also advantageously used for the A-component are the so-called modified multifunctional isocyanates, that is, products which are obtained through chemical reactions of the above diisocyanates and/or polyisocyanates. Exemplary are polyisocyanates containing esters, ureas, biurets, allophanates and, preferably, carbodiimides and/or uretonomine, and isocyanurate and/or urethane group-containing diisocyanates or polyisocyanates. Liquid polyisocyanates containing carbodiimide groups, uretonomine groups and/or isocyanurate rings, having isocyanate groups (NCO) contents of from 120 to 40 weight percent, more preferably from 20 to 35 weight percent, can also be used. These include, for example, polyisocyanates based on 4,4′- 2,4′- and/or 2,2′-diphenylmethane diisocyanate and the corresponding isomeric mixtures, 2,4- and/or 2,6-toluenediisocyanate and the corresponding isomeric mixtures; mixtures of diphenylmethane diisocyanates and PMDI; and mixtures of toluenediisocyanates and PMDI and/or diphenylmethane diisocyanates.
Suitable prepolymers for use as the polyisocyanate component of the formulations of the present invention are prepolymers having NCO contents of from 2 to 40 weight percent, more preferably from 4 to 30 weight percent. These prepolymers are prepared by reaction of the di- and/or poly-isocyanates with materials including lower molecular weight diols and triols, but also can be prepared with multivalent active hydrogen compounds such as di- and tri-amines and di- and tri-thiols. Individual examples include aromatic polyisocyanates containing urethane groups, preferably having NCO contents of from 5 to 40 weight percent, more preferably 20 to 35 weight percent, obtained by reaction of diisocyanates and/or polyisocyanates with, for example, polyols such as lower molecular weight diols, triols, oxyalkylene glycols, dioxyalkylene glycols, or polyoxyalkylene glycols having molecular weights up to about 800. These polyols can be employed individually or in mixtures as di- and/or polyoxyalkylene glycols. For example, diethylene glycols, dipropylene glycols, polyoxyethylene glycols, ethylene glycols, propylene glycols, butylene glycols, polyoxypropylene glycols and polyoxypropylene polyoxyethylene glycols can be used. Polyester polyols can also be used, as well as alkyl diols such as butane diol. Other diols also useful include bishydroxyethyl- or bishydroxypropyl-bisphenol A, cyclohexane dimethanol, and bishydroxyethyl hydroquinone.
Useful as the polyisocyanate component of prepolymer formulations that may be employed in the present invention are: (i) polyisocyanates having an NCO content of from 8 to 40 weight percent containing carbodiimide groups and/or urethane groups, from 4,4′-diphenylmethane diisocyanate or a mixture of 4,4′- and 2,4′-diphenylmethane diisocyanates; (ii) prepolymers containing NCO groups, having an NCO content of from 2 to 35 weight percent, based on the weight of the prepolymer, prepared by the reaction of polyols having a functionality of preferably from 1.75 to 4 and a molecular weight of from 800 to 15,000 with either 4,4′-diphenylmethane diisocyanate, a mixture of 4,4′- and 2,4′-diphenylmethane diisocyanate, or a mixture of (i) and (ii); and (iii) 2,4′ and 2,6-toluene-diisocyanate and their corresponding isomeric mixtures.
PMDI in any of its forms is the most preferred polyisocyanate for use with the present invention. When used, it preferably has an equivalent weight between 125 and 300, more preferably from 130 to 175, and an average functionality of greater than about 1.5. More preferred is an average functionality of from 1.75 to 3.5. The viscosity of the polyisocyanate component is preferably from 25 to 5,000 centipoise (cP) (0.025 to about 5 Pa*s), but values from 100 to 1,000 cP at 25° C. (0.1 to 1 Pa*s) are preferred for ease of processing. Similar viscosities are preferred where alternative polyisocyanate components are selected. Still, preferably the polyisocyanate component of the formulations of the present invention is selected from the group consisting of MDI, PMDI, an MDI prepolymer, a PMDI prepolymer, a modified MDI, and mixtures thereof.
In proportion it is desirable that the ratio of the A-component to the B-component (polyisocyanate to formulated polyol) ranges from about 100 to about 250, that is to say, an isocyanate index of from about 1 to about 2.5; in some non-limiting embodiments, the isocyanate index is desirably from about 1.5 to about 1.8, that is, so-called “medium index” foams.
Other polyols may also be included in the formulated polyol and/or in the final formulation, in addition to the three denoted hereinabove as required, and, if included, are considered to be part of the formulation's B-component. While these additional materials are typically included as part of the B-component during the formulating process, such are treated here separately because they are considered to be optional. Such may include one or more other polyether or polyester polyols of the kind typically employed in processes to make polyurethane and/or polyisocyanurate foams. Other compounds having at least two isocyanate-reactive hydrogen atoms may also be present, for example, polythioether polyols, polyester amides and polyacetals containing hydroxyl groups, aliphatic polycarbonates containing hydroxyl groups, amine terminated polyoxyalkylene polyethers, and preferably, polyester polyols, polyoxyalkylene polyether polyols, and graft dispersion polyols. Mixtures of two or more of the aforesaid materials may also be employed. In many embodiments such polyols have from about 2 to about 8 hydroxyl groups per molecule, a molar average functionality of at least about 3 or more, and a hydroxyl number of greater than 100 mg KOH/g, and in certain embodiments, greater than 300 mg KOH/g.
In some non-limiting embodiments, the formulated polyol may also include one or more chain extenders and/or crosslinkers. Where selected, chain extenders may be bifunctional, low molecular weight alcohols, in particular those having a molecular weight of up to 400, for example ethylene glycol, propylene glycol, butanediol, hexanediol, and mixtures thereof. Crosslinkers, in many embodiments, are at least trifunctional, and may be selected from, for example, low molecular weight alcohols such as glycerol, trimethylolpropane, pentaerythritol, sucrose, sorbitol, or mixtures thereof.
The formulation of the present invention may include further additives or modifiers such as are well-known in the art. For example, surfactants, catalysts, flame retardants, and/or fillers may be employed. Of particular significance are one or more trimerization catalysts. The trimerization catalyst employed may be any known to those skilled in the art that will catalyze the trimerization of an organic isocyanate compound to form the isocyanurate moiety. For typical isocyanate trimerization catalysts, see The Journal of Cellular Plastics, November/December 1975, page 329: and U.S. Pat. Nos. 3,745,133; 3,896,052; 3,899,443; 3,903,018; 3,954,684 and 4,101,465; the disclosures of which are incorporated by reference herein in their entireties. Typical trimerization catalysts include the glycine salts, tertiary amine trimerization catalysts, alkali metal carboxylic acid salts, and mixtures of these classes of catalysts. Preferred species within the classes are sodium N-2-hydroxy-5-nonylphenyl-methyl-N-methylglycinate, N,N-dimethylcyclohexyl-amine, and mixtures thereof. Also included in the preferred catalyst components are the epoxides disclosed in U.S. Pat. No. 3,745,133, the disclosure of which is incorporated herein by reference in its entirety.
Another category of catalysts that may be included is the amine catalysts, including any organic compound which contains at least one tertiary nitrogen atom and is capable of catalyzing the hydroxyl/isocyanate reaction between the A-component and B-component. Typical classes of amines include the N-alkylmorpholines, N-alkyl-alkanolamines, N,N-dialkylcyclohexylamines, and alkylamines where the alkyl groups are methyl, ethyl, propyl, butyl and isomeric forms thereof, and heterocyclic amines. Typical but non-limiting thereof are triethylenediamine, tetramethylethylenediamine, bis(2-dimethylaminoethyl)ether, triethylamine, tripropylamine, tributylamine, triamylamine, pyridine, quinoline, dimethylpiperazine, piperazine, N,N-dimethylcyclohexylamine, N-ethyl-morpholine, 2-methylpropanediamine, methyltriethyl-enediamine, 2,4,6-tridimethylamino-methyl)phenol, N,N′,N″-tris(dimethylamino-propyl)sym-hexahydrotriazine, and mixtures thereof. A preferred group of tertiary amines from which selection may be made comprises bis(2-dimethylamino-ethyl)ether, dimethylcyclohexylamine, N,N-dimethyl-ethanolamine, triethylenediamine, triethylamine, 2,4,6-tri(dimethylaminomethyl)phenol, N,N′,N-ethylmorpholine, and mixtures thereof.
Non-amine catalyst may also be used in the present invention. Typical of such catalysts are organometallic compounds of bismuth, lead, tin, titanium, iron, antimony, uranium, cadmium, cobalt, thorium, aluminum, mercury, zinc, nickel, cerium, molybdenum, vanadium, copper, manganese, zirconium, and combinations thereof. Included for illustrative purposes only are bismuth nitrate, lead 2-ethylhexoate, lead benzoate, lead naphthenate, ferric chloride, antimony trichloride, antimony glycolate, combinations thereof, and the like. A preferred class includes the stannous salts of carboxylic acids, such as stannous acetate, stannous octoate, stannous 2-ethylhexoate, 1-methylimidazole, and stannous laurate, as well as the dialkyl tin salts of carboxylic acids, such as dibutyl tin diacetate, dibutyl tin dilaurate, dibutyl tin dimaleate, dioctyl tin diacetate, combinations thereof, and the like. Catalysts, such as NIAX™ A-1, POLYCAT™ 9 and/or POLYCAT™ 77, may be included in amounts from about 1 to about 8 parts, total, of B-component. (NIAX™ A-1 is available from General Electric. POLYCAT™ 9 and POLYCAT™ 77 are available from Air Products.) Additional catalysts, such as TOYOCAT™ DM 70 or other gelling catalysts, may be included in amounts ranging from 0 to about 2 parts. (TOYOCAT™ DM 70 is available from Tosoh Corporation.)
While the basic formulation enables preparation of foams having improved fire behavior, as defined hereinbelow, in some embodiments it may be desirable to further enhance fire performance by including, as additives, one or more brominated or non-brominated flame retardants, such as tris(2-chloroethyl)phosphate, tris(2-chloro-propyl)phosphate, tris(1,3-dichloropropyl)phosphate, diammonium phosphate, various halogenated aromatic compounds, antimony oxide, alumina trihydrate, polyvinyl chloride, and combinations thereof. Dispersing agents, cell stabilizers, and surfactants may also be incorporated into the formulations.
Surfactants, including organic surfactants and silicone based surfactants, may be added to serve as cell stabilizers. Some representative materials are sold under the designations SF1109, L520, L521 and DC193, which are, generally, polysiloxane polyoxylalkylene block copolymers, such as those disclosed in U.S. Pat. Nos. 2,834,748; 2,917,480; and 2,846,458, the disclosures of which are incorporated herein by reference in their entireties. Also included are organic surfactants containing polyoxyethylene-polyoxybutylene block copolymers, as are described in U.S. Pat. No. 5,600,019, the disclosure of which is incorporated herein by reference in its entirety. It is particularly desirable to employ a minor amount of a surfactant to stabilize the foaming reaction mixture until it cures. Other surfactants include polyethylene glycol ethers of long-chain alcohols, tertiary amine or alkanolamine salts of long-chain allyl acid sulfate esters, alkylsulfonic esters, alkyl arylsulfonic acids, and combinations thereof.
Such surfactants are employed in amounts sufficient to stabilize the foaming reaction against collapse and the formation of large uneven cells. Typically, from about 0.2 to about 3 parts of the surfactant per 100 parts by weight of the formulated polyol are sufficient for this purpose. Surfactants, such as DABCO™ DC5598, may be included in any amount ranging from 0 to about 6 parts. (DABCO™ DC5598 is available from Air Products).
Other additives may include, but are not limited to, carbon black and colorants, fillers and pigments. Examples may include barium sulfate, calcium carbonate, graphite, carbon black, titanium dioxide, iron oxide, microspheres, alumina trihydrate, wollastonite, prepared glass fibers (dropped or continuous), and polyester fibers and other polymeric fibers, as well as various combinations thereof.
The polyurethane or polyisocyanurate polymer prepared according to the process of this invention is in certain non-limiting embodiments a rigid, foamed, closed-cell polymer. Such a polymer is typically prepared by intimately mixing the reaction components, i.e., a polyol/blowing agent component (consisting essentially of or comprising the formulated polyol and blowing agent defined hereinabove), along with an isocyanate component, i.e., at least two streams; or a polyol component (consisting essentially of or comprising the formulated polyol defined hereinabove), a blowing agent component, and an isocyanate component, i.e., at least three streams, wherein the formulated polyol and blowing agent component mix just prior to contact thereof with the isocyanate component) at room temperature or at a slightly elevated temperature for a short period. Additional streams may be included, as desired, for the introduction of various catalysts and other additives. Mixing of streams may be carried out either in a spray apparatus, a mixhead with or without a static mixer for combining the polyol component and blowing agent, or a vessel, and then spraying or otherwise depositing the reacting mixture onto a substrate. This substrate may be, for example, a rigid or flexible facing sheet made of foil or another material, including another layer of similar or dissimilar polyurethane or polyisocyanurate which is being conveyed, continuously or discontinuously, along a production line, or directly onto a conveyor belt.
In alternative embodiments the reacting mixture may be poured into an open mold or distributed via laydown equipment into an open mold or simply deposited at or into a location for which it is destined, i.e., a pour-in-place application, such as between the interior and exterior walls of a structure. In the case of deposition on a facing sheet, a second sheet may be applied on top of the deposited mixture. In other embodiments, the mixture may be injected into a closed mold, with or without vacuum assistance for cavity-filling. If a mold is employed, it is most typically heated.
In general, such applications may be accomplished using the known one-shot, prepolymer or semi-prepolymer techniques used together with conventional mixing methods. The mixture, on reacting, takes the shape of the mold or adheres to the substrate to produce a polyurethane or polyisocyanurate polymer of a more-or-less predefined structure, which is then allowed to cure in place or in the mold, either partially or fully. Suitable conditions for promoting the curing of the polymer include a temperature of typically from 20° C. to 150° C., preferably from 35° C. to 75° C., and more preferably from 45° C. to 55° C. Such temperatures will usually permit the sufficiently cured polymer to be removed from the mold, where such is used, typically within from about 1 to 10 minutes and more typically within from 1 to 5 minutes after mixing of the reactants. Optimum cure conditions will depend upon the particular components, including catalysts and quantities used in preparing the polymer and also the size and shape of the article manufactured.
The result may be a rigid foam in the form of slabstock, a molding, a filled cavity, including but not limited to a pipe or insulated wall or hull structure, a sprayed foam, a frothed foam, or a continuously- or discontinuously-manufactured laminate product, including but not limited to a laminate or laminated product formed with other materials, such as hardboard, plasterboard, plastics, paper, metal, or a combination thereof. Advantageously, the polyurethane and polyisocyanurate foams prepared in the present invention may show improved processability when compared with foams from formulations and preparation methods that are similar except that the formulations do not comprise the specific formulated polyol used in the present invention. As used herein, the term “improved processability” refers to the capability of the foam to exhibit reduced defects, which may include but are not limited to shrinkage and deformation. This improvement may be particularly advantageous when the invention is used in the manufacture of sandwich panels. It is preferable that such reduced levels of shrinkage and deformation be less than about 0.5 percent as linear deformation, as tested according to European Standard EN 1603 at 80° C., with specimen dimensions recorded after 20 hours. Sandwich panels may be defined, in some embodiments, as comprising at least one relatively planar layer (i.e., a layer having two relatively large dimensions and one relatively small dimension) of the rigid foam, faced on each of its larger dimensioned sides with at least one layer, per such side, of flexible or rigid material, such as a foil or a thicker layer of a metal or other structure-providing material. Such a layer may, in certain embodiments, serve as the substrate during formation of the foam.
Also advantageously, the polyurethane and polyisocyanurate foams prepared in the present invention may exhibit improved fire behavior when compared with foams from formulations and preparation methods that are similar except that the formulations do not comprise the specific formulated polyol used in the present invention. As used herein, the term “improved fire behavior” refers to the capability of the foam to exhibit B2 fire behavior, which is defined as having a flame height of not higher than 15 centimeters when tested according to German Standard DIN 4102. In certain embodiments the invention may be useful in satisfying fire requirements based on new Euroclasses regulations (European Standard EN 12823).
In addition, the polyisocyanurate and polyurethane foams of the invention may exhibit improved curing properties, including improved green compressive strength and reduced post expansion at selected foam demolding time. Testing to determine these properties is described in the footnotes to Table 1 and Table 3, respectively. These features may be particularly advantageous when the invention is employed to produce insulated sandwich panels.
The description hereinabove is intended to be general and is not intended to be inclusive of all possible embodiments of the invention. Similarly, the examples hereinbelow are provided to be illustrative only and are not intended to define or limit the invention in any way. Those skilled in the art will be fully aware that other embodiments, within the scope of the claims, will be apparent, from consideration of the specification and/or practice of the invention as disclosed herein. Such other embodiments may include selections of specific components and proportions thereof; mixing and reaction conditions, vessels, deployment apparatuses, and protocols; performance and selectivity; identification of products and by-products; subsequent processing and use thereof; and the like; and those skilled in the art will recognize that such may be varied within the scope of the claims appended hereto.
Materials employed in the examples and/or comparative examples include the following, given in alphabetical order.
CM265 is an additive blend of water and VORANOL™ RN490 (50/50 by weight).
Five formulated polyols are prepared, each including a sucrose-initiated polyol (VORANOL™ RN490) and a Novolac-type polyol (IP 585). Only Example 1 includes an aliphatic polyester polyol, which is TERATE™ 2541V; the Comparative Examples replace the aliphatic polyester polyol with a polyether polyol of equivalent functionality. The formulated polyol is then, for Comparative Examples 2-5, combined with a chain extender, and, for Example 1 and Comparative Examples 2-5, a fire retardant, silicone surfactant, catalysts, water, and other components. The mixture is then reacted with an isocyanate (VORANATE™ M600) and n-pentane, at an index of 1.8, to form a free rise foam. The compositions of each formulation are shown in Table 1. Curing properties are tested by measuring green compressive strength at five (5) minutes, and the results are also shown in Table 1. Finally, the fire behavior of each of the foams is tested according to German Standard DIN 4102, with the results shown in Table 1.
It is seen that Example 1 shows improved curing (green compressive strength, GCS test) and fire behavior properties (German Standard DIN 4102 test, measuring flame height).
For comparative purposes, five formulations are prepared according to Table 2, using the same formulation method and means as used for Example 1 and Comparative Examples 2-5. Results of Comparative Example 6 show that combining an aromatic polyester polyol with an aromatic polyether polyol that is not a Novolac-type polyol does not improve curing properties when compared to Comparative Examples 7-10.
Three foam formulations are prepared using a high pressure foaming machine and the same evaluation methods as in previous Examples and Comparative Examples, with the formulations shown in Table 3. In this case Examples 12-13 each contain an aromatic polyester polyol, while Comparative Example 11 does not.
It is seen that Examples 12 and 13 show improved curing (reduced post expansion and enhanced green compressive strength results) and improved fire behavior properties (German Standard DIN 4102 test, measuring flame height), as compared with Comparative Example 11.
| Filing Document | Filing Date | Country | Kind | 371c Date |
|---|---|---|---|---|
| PCT/US2010/027563 | 3/17/2010 | WO | 00 | 9/8/2011 |
| Number | Date | Country | |
|---|---|---|---|
| 61165620 | Apr 2009 | US |
