BARRIER LAYER FOR USE IN REFRIGERATOR CABINETS

Abstract: Disclosed herein is a composition for barrier layers for use in insulative cabinet wall structures, particularly those used in appliances such as refrigerators and dishwashers. The compositions of the barrier layer is resistant to the action of polyurethane foam blowing agents, and has (i) an effective amount of a modified polyolefin, which is most preferably, a polyethylene modified with a compound selected from the group consisting of maleic anhydride, maleic acid, maleic anhydride derivatives, maleic acid derivatives, and mixtures thereof; and (ii) an effective amount of a rubber. Optionally, and most preferably, the barrier layer composition may further contain (iii) an effective amount of a polyolefin selected from the group consisting of polyethylene, polypropylene, polybutylene, and copolymers thereof. The invention further provides thermoformable composites incorporating the above-described barrier layer as well as insulative cabinet wall structures incorporating the thermoformable composite. Finally, the invention further provides a method of making a thermoformable composite incorporating the barrier layer of the invention.

Description: BARRIER LAYER FOR USE IN REFRIGERATOR CABINETS The invention provides compositions which are resistant to the action of polyurethane foam blowing agents, barrier layers com¬ prised of said compositions, thermoformable composites incorpo¬ rating said barrier layers, methods of making said thermoformable composites, and insulative cabinet wall structures incorporating said thermoformable composites, the structures being useful in appliance constructions, particularly refrigerators and dishwash¬ ers. Typical refrigerator appliance cabinets consist of an outer metal cabinet, an inner plastic liner typically made of ABS (acrylo- nitrile-butadiene-styrene) or HIPS (high impact polystyrene) , and an insulating foam core, generally of polyurethane foam. Blowing agents for the polyurethane foam are locked into the foam. Freon or fluorotrichloromethane, a completely halogenated methane, is presently employed commercially as the blowing agent. However, increasing amounts of environmental regulations are urging, and in some cases mandating, that substitutes for Freon be found. The most promising proposed substitutes for Freon are halogenated hy¬ drocarbons containing at least one hydrogen atom. Polyurethane blowing agents, such as Freon and Freon substitutes like 2-fluoro-2,2-dichloroethane and 2,2-dichloro-l,l,l-tri- fluoroethane, can cause liner blistering, catastrophic cracks, tiny cracks (crazing) , and loss of impact properties (embrittle- ment), as well as stress whitening and/or dissolution. These Freon substitutes appear to be more chemically aggressive than Freon in attacking the liner. It is commonly believed that blow¬ ing agent attack of the liner occurs on cooling and condensation of the blowing agent to liguid. Conditions favorable to such cycles occur during shipping and storage. Shipping conditions can be simulated during fabrication by cycling the appliance cabinet from hot to cold to cause evaporation and condensation of the blowing agent (s) . Prior art attempts to address this problem have involved the use of barrier layers. A principal function of such layers is to im¬ pede the attack of the blowing agents upon the inner plastic liner. However, in addition to providing superior solvent resistant with respect to polyurethane foam blowing agents, bar¬ rier layer compositions must also exhibit certain processability characteristics. In particular, compositions intended for use as barrier layers in appliance cabinet construction must be extrud- able, thermoformable and regrindable. Extrudablity, as used herein, is intended to indicate that the composition can be extruded, either simultaneously or sub¬ sequently, with the materials which comprise the inner plastic liner or liners to form a thermoplastic composite. Thus, the com¬ position of the barrier layer must be adherable to the styrene based polymers commonly used to make the inner plastic liner. II- lustrative examples of styrene based polymers are ABS, HIPS, and mixtures thereof. The ability to co-extrude the barrier layer with the one or more layers of the inner liner provide signifi¬ cant cost and efficiency advantages. in addition, barrier layer compositions must be thermoformable. In particular, the barrier layer composition must not detract from the thermoformability of composite structures incorporating such barrier layers. If the resulting composites cannot be ther- moformed into the required inner cabinet shape, appliance cabinet manufacturers lose significant cost and production advantages. Those skilled in the art will appreciate that thermoformability is thus a requisite for compositions intended for use as barrier layers in appliance cabinet construction. Finally, the barrier layer composition must not negatively affect the regrindability or recyclability of the thermoformable composite. During the manufacturing of appliance cabinets, the thermoformed inner cabinets are typically trimmed of excess composite material. The resulting trim or scrap material is often incorporated into virgin inner liner material, ie., styrene based polymer(s) . As a result, compatibility of the composition of the barrier layer with that of the inner liner materials is particu¬ larly important. The properties of the inner liner materials must not be negatively affected. Those skilled in the art will ap- preciate that the ability to recycle excess thermoformable composite material provides significant cost savings. Thus, it would be highly desirable to provide a barrier-layer composition capable of exhibiting (a) superior solvent resistant to polyurethane foam blowing agents, (b) extrudability and adher- ability with respect to inner liners and the manufacture of composite structures, (c) thermoformability once the barrier layer has been incorporated into a composite structure, and (d) regrindability with respect to the incorporation of scrap mate- rial in virgin liner material. Although several attempts have been made by the prior art to ad¬ dress this problem, none have provided the desired balance of properties. For example, U.S. Patent 5,118,174 to Benford et al discloses a multi-component laminated structure for use insulated appliance cabinet structures. The multi-component laminated structure con¬ tains a barrier layer which however provides insufficient solvent resistance and regrind capability. U.S. Patent 5,227,245 to Brands et al discloses a barrier layer for preventing solvent attack in insulative cabinet wall struc¬ tures which consists essentially of amorphous thermoplastic poly¬ ester resin which is a copolymer adduct of an aromatic dicarb- oxylic acid and an active hydrogen containing material. However, the polyester has extremely poor capability with styrenic resins and thus the barrier layer lacks the desired regrind capability. Finally, U.S. Patents 5,221,136 and 5,340,208 to Hauck et al, disclose a barrier layer comprised of a polyolefin and a block copolymer rubber which may be functionalized with maleic anhydride. However, some thermoformable composites prepared using these barrier layers have been found to exhibit less than optimum thermoformablity. Particularly, it has been found that the bar- rier layer can stick to the female molds employed in the thermo- forming process. In addition, such barrier layer compositions have been found to have limited regrind capability with styrenic based inner liner materials. Thus, it is an object of this invention to provide a barrier layer composition which is resistant to the action of polyure¬ thane foam blowing agents, and which exhibits desirable proces¬ sing characteristics such as extrudability, thermoformability, and regrindability. It is another object of the invention to provide a barrier layer which is adherable to one or more inner liner layers to form a thermoformable composite. More particularly, it is an object of the invention to provide a barrier layer which is extrudable with one or more inner liner layers to form a thermoformable composite. It is another object of the invention to provide a thermoformable composite which contains a barrier layer which protects one or more inner liner layers from the action of polyurethane foam blowing agents, and which furthermore has desirable regrind com¬ patibility with the materials comprising said inner liner layers. Finally, it is an object of the invention to provide an insulated cabinet wall structure which comprises a thermoformable composite which contains a barrier layer protecting the innerliner layers from the action of polyurethane foam blowing agents. These and other objects of the invention are provided with a par- ticular barrier layer composition (A) . The barrier layer composi¬ tion (A) is resistant to the action of polyurethane foam blowing agents and comprises (i) an effective amount of a modified poly¬ olefin, most preferably modified with a compound selected from the group consisting of maleic anhydride, maleic acid, maleic anhydride derivatives, maleic acid derivatives, and mixtures thereof; and (ii) an effective amount of a rubber. Optionally, and most preferably, the barrier layer composition (A) will fur¬ ther contain an effective amount of a polyolefin (iii) , selected from the group consisting of polyethylene, polypropylene, poly- butylene, and copolymers thereof and optionally styrenic based polymers (iv) . The invention further provides a thermoformable composite having a functional layer (I) comprising one or more sublayers of one or more styrenic based polymers, and a barrier layer (II) adhered to at least one surface of the functional layer (I), wherein the barrier layer (II) comprises the barrier layer composition (A) . The invention also provides an insulative wall cabinet structure having the thermformable composite in combination with an outer structural wall (III) and polyurethane foam insulation (IV) ad¬ hered to both of the barrier layer (II) and the outer structural wall (III) so as to be placed there between. Finally, the invention provides a method of making the thermo¬ formable composite, requiring providing a functional layer (I) and adhering to the functional layer (I), a barrier layer (II) . Figure 1 is a schematic drawing of a refrigerator cabinet. Figure 2 is a schematic drawing of an inner cabinet serving as the inner plastic wall of the refrigerator of Figure 1. Figure 3 is a fragmentary cross-section of the thermformable composite forming the inner cabinet of Figure 2. Turning now to the drawings, it can be seen that Figure 1 illus¬ trates a particularly desirable end use application for the instant invention. The refrigerator appliance 1 has an insulative wall cabinet structure E which is comprised of an outer metal shell 2, inner cabinet 3, and a body of foamed-in-place insula¬ tion 4 there between. Inner cabinet 3 is formed of thermoformable composite 5 (see Fig. 2). Turning now to Figure 3, thermoformable composite 5 is comprised of a functional layer 6 and a barrier layer 7. Functional layer 6 serves as the visually pleasing portion of the interior of the refrigerator appliance 1. In general, the func¬ tional layer 6 will be comprised of one or more sublayers (8, 9) of one or more styrenic based polymers. Suitable examples of sty¬ renic based polymers include ABS, HIPS and mixtures thereof. A particularly preferred example is illustrated in Figure 3, wherein functional layer 6 is comprised of sublayers 8 and 9. In general, sublayer 8 will generally provide a visually pleasing high gloss appearance, while sublayer 9 will generally provide desirable performance characteristics such as good resistance to food contamination and normal wear and tear. Illustrative materials particularly suitable for use as sublayer 8 include HIPS. A particularly desirable material for use as sublayer 8 is a high gloss medium impact polystyrene (e.g. PS ® -7800, commer¬ cially available from BASF Corporation of Wyandotte, Michigan) . Illustrative materials suitable for use as sublayer 9 include bulk HIPS (e.g. a particularly desirable material is a high impact polystyrene, characterized by a nominal melt flow rate of 2.6 g/10' (measured according to ASTM; condition G) and a Vicat softening temperature of 102°C, PS-7100, also commercially avail¬ able from BASF Corporation) or ABS. In general, sublayers 8 and 9 will comprise functional layer 6. However, it will be appreciated that with the many polymer com¬ positions now available, functional layer 6 may also be comprised of either a single layer or more than two layers. In the particularly preferred embodiment described above, sub¬ layer 8 will generally comprise from between 1 to 10 percent by weight of the overall weight of functional layer 6 while sublayer 9 will generally comprise between 99 to 90 percent by weight of the overall weight of functional layer 6. More particularly, sub¬ layer 8 comprises from between 1 to 5 percent by weight while sublayer 9 comprises from between 99 to 95 percent of the total weight of functional layer 6. The barrier layer 7 may be comprised of: (i) an effective amount of a modified polyolefin; and (ii) an effective amount of a rubber (iii) of polyethylene, polypropylene, polybutylene, and copolymers thereof, and/or (iv) a styrenic based polymer. The barrier layer composition (A) will contain a modified poly¬ olefin (i) . As used herein, the term modified polyolefin is in¬ tended to describe polyolefin graft co-polymers derived from the graft polymerization of an unsaturated carboxylic acid or its functional derivative or another vinyl functional group contain¬ ing monomer onto any of the olefin polymers discussed below with respect to component (iii) . However, the olefin to be so modified will preferably be polyethylene (HDPE, LDPE, LLDPE) . The unsaturated carboxylic acid or its functional derivative or another vinyl functional group containing monomer which is to be grafted onto the above-mentioned olefin polymers, includes, for example, carboxylic acids such as acrylic acid, methacrylic acid, maleic acid, fumaric, itaconic and sorbic acid; acid anhydrides such as maleic anhydride and itaconic anhydride acid amides such as acrylamide and methacrylamide; epoxy group containing compounds such as glycidyl aerylate, glycidyl methacrylate hydroxyethyl group containing esters such as 2-hydroxyethyl meth- aerylate and polyethylene glycol monoacrylate; and metal salts such as sodium aerylate, sodium methacrylate and zinc aerylate. These graft monomers may be used alone or in combination. Among the acids and anhydrides that are particularly preferred are ma¬ leic anhydride and maleic acid and the derivatives thereof. The proportion of said graft monomers are preferably within the molar range of 0.005 to 5 percent based on component (i) . A pre¬ ferred embodiment of such polymer type includes the product ob¬ tained by grafting maleic acid or anhydride onto an HDPE. The graft copolymerization of the unsaturated carboxylic acid or its functional derivative or another vinyl functional group contain¬ ing monomer onto the olefin polymer can be conducted using vari¬ ous method. For example, the olefin polymer, the graft monomer and a free-radical initiator are mixed together and kneaded in a molten state. In another method, the graft monomer are incorpo- rated in a solution or suspension of the olefin polymer in a suitable solvent. A most preferred material for use as modified polyolefin (i) is a modified polyolefin, characterized by a melt index of 1.2 g/10 min, measured according to ASTM D1238 and a density of 0.961 g/cm 3 , measured according to ASTM D1505 (e.g. Plexar ® PX209, commercially available from Quantum of Cincinnati, Ohio). The barrier layer composition (A) will further comprise a rubber (ii) . Suitable rubbers will generally be synthetic block copolymer rubbers. Illustrative examples include styrene block diblock, styrene-ethylene/butylene-styrene triblock, styrene-eth- ylene/butylene-styrene triblock functionalized with maleic anhydride, maleic acid or admixtures thereof, or combinations of any of the above. Particularly suitable rubbers (ii) are linear styrene-butadiene-styrene rubbers (e.g. Stereon ® 840A, a linear styrene-butadiene-styrene rubber with a styrene content of 43% by weight, a Mw of 94000, and a M /M n value of 1.40 commercially available from Firestone Tire & Rubber Co., and Finaclear ® 520, a linear styrene-butadiene-styrene rubber with a styrene content of 43% by weight, a M w of 85000 and a M w /M n value of 1.10, commer¬ cially available from Fina of Houston, Texas. Optionally, and most preferably, the barrier layer composi¬ tion (A) will also contain a polyolefin (iii) . Although the com¬ position containing components (i) and (ii) is capable of provid¬ ing desirable performance properties, the incorporation of poly¬ olefin (iii) provides significant cost advantages without any significant decrease in the performance or processing properties of the compositions or barrier layers of the invention. Broadly speaking, the polyolefin component (iii) is defined to include the various types of polyethylene and polypropylenes, polybutylenes, and the well-known copolymers thereof. While the polyolefins other than polyethylene can provide blends in accor¬ dance with the present invention, it is the polyethylenes which are the preferred group. Included in the polyethylenes are the HDPE materials made by polymerizing ethylene using so-called Ziegler-Natta coordination catalysts to provide linear (non- branched) high density polyethylene (densities = 0.941 to 0.965 qis/cc) LLPE materials made by polymerizing ethylene using free- radical catalysts under high pressures and high temperatures to provided branched polyethylenes (densities = 0.910 to 0.934 g/ml); the LLDPE materials prepared from ethylene and minor amounts of alpha, beta-et ylenically unsaturated C to Cι alkenes under Ziegler-Natta conditions to provide essentially linear low density polyethylenes but with alkyl side chains from the α-ole- fin components (densities = 0.88 to 0.935 g/ml). Preferred within this polyethylene group are the high density polyethylenes as de¬ scribed above. In addition, suitable polyolefins (iii) will also have melt flow indexes (MFI) of between 1 to 10, with the most preferred poly¬ olefins having MFI's of between 1 to 3. A particularly preferred polyolefin is the high density polyethylene characterized by a density of 0.96 g/ml, measured according to ASTM D1505 and a melt index of 1.15 g/10 min, measured according to ASTM D1238 (e.g. commercially available as LM-6187 HDPE from Quantum of Cincin¬ nati, Ohio) . Finally, the barrier layer composition (A) may further optionally contain a styrenic based polymer (iv) . The styrenic polymer com¬ ponent (iv) of the present invention is a polystyrene resin or ABS (acrylonitrile-butadiene-styrene) copolymer. The polystyrene resins includes styrene homopolymer (crystal polystyrene) , or rubber modified polystyrene (high impact polystyrene (HIPS) ) . The polystyrene is a high molecular weight polymer, preferably, hav¬ ing a molecular weight (weight average) greater than about 150,000 g/mol. Rubber modified polystyrene, which is most pre¬ ferred, is a well-known material which is polystyrene modified by an elastomer such as polybutadiene or styrene-butadiene copolymer. This material is described, for example, in Modern Plastics Encyclopedia, McGraw-Hill, p.72 (1983- 1984). It can be prepared by polymerizing styrene monomer in the presence of poly¬ butadiene or styrene-butadiene copolymer. The ABS copolymer re- sins that can be used in the present invention are well known to those skilled in the art, the preparation of such material is disclosed in, for example, U.S. Nos. 3,563,845; 3,565,746; and 3,509,237 all of which are incorporated herein by reference. In general, the barrier layer composition (A) generally may have from (i) 1 to 70 parts by weight of a modified polyolefin, (ii) 1 tp 40 parts by weight of a rubber, (iii) 0 to 90 parts by weight of a polyolefin and (iv) 0 to 50 parts by weight of a styrenic based polymer, wherein the components (i) to (iv) add up to the total weight of the barrier layer composition A. A preferred barrier layer composition will have from (i) 5 to 40 parts by weight of a modified polyolefin, (ii) 5 to 30 parts by weight of a rubber, (iii) 20 to 80 parts by weight of a polyolefin and (iv) 0 to 48 parts by weight of a styrenic based polymer, wherein the components (i) to (iv) add up to the total weight of the barrier layer composition A. Most preferably, the barrier layer composition of the Invention will have from (i) 5 to 30% parts by weight of a modified polymer, (ii) 5 to 20% parts by weight of a rubber, (iii) 30 to 70% parts by weight of a polyolefin and (iv) 0 to 30% parts by weight of a styrenic based polymer, wherein the components (i) to (iv) add up to the total weight of the barrier layer composition. Two particularly preferred embodiments of the barrier layer com¬ position (A) are set forth below: Embodiment # 1 Embodiment # 2 [parts by weight] [parts by weight] Modified polyolefin (i) 15-25 15-25 Rubber (ii) 10-20 10-20 Polyolefin (iii) 60-70 35-45 Styrene polymer (iv) - 20-40 Components (i) - (iv) of the barrier layer composition (A) will be processed by well-known processing methods so as to form a homogeneous mixture. The mixture may be pelletized as necessary or may be immediately formed into a layer by well-known polymer processing techniques. Turning now to thermoformable composite 5, barrier layer 7 will normally be from 1 to 50 percent by weight of the total weight of composite 5, while functional layer 6 will be from 50 to 99 per¬ cent by weight, based on the weight of composite 5. More particu¬ larly, functional layer 6 and barrier layer 7 will respectively comprise 70 to 99 percent by weight and 30 to 1 percent by weight of the overall weight of composite 5. It is most preferred if composite 5 has from 80 to 95 percent functional layer 6 and 5 to 20 percent by weight of barrier layer 7. More preferably, thermoformable composite 5 will be formed by the simultaneous coextrusion of barrier layer 7 directly onto sub¬ layer 9. In this preferred embodiment, sublayer 9 will be coex¬ tensive with and adhered to sublayer 8. Alternatively, a pre- viously made barrier layer 7 may be subsequently laminated to functional layer 6 and more preferably, to sublayer 9. Those skilled in the art will appreciate that well-known lamination technologies involving the application of increased heat and/or pressure are sufficient to form thermoformable composite 5. Thermoformable composite 5 will generally be thermoformed into an appliance cabinet structure such as that illustrated in Figure 2 as inner cabinet 3. Those skilled in the art will appreciated that such processing techniques are well-known in the art and generally involve a stamping process utilizing cooperating male and female molds. It will be appreciated that at most molding op¬ erations, a surface of barrier 7 will face outward, away from the interior of inner cabinet 3 and thus will be in contact with the female mold. Accordingly, it is an aspect of desirable thermo- formability that barrier layer 7 not adhere to the female mold during the thermoforming process. Thermoformed inner cabinet 3 is then assembled with outer shell a so that a gap exists there between. A polyurethane foam composi- tion is placed therein and foamed in situ between inner cabinet 3 and outer shell 2 to form foamed-in-place insulation 4. The re¬ sulting structure of inner cabinet 3, outer shell 2 and foamed- in-place insulation 4 there between is herein defined to be insu¬ lative wall cabinet structure E. The outer shell 2 may be comprised of well known materials suit¬ able for use as the outer surface of an appliance construction. While hard rigid plastics may be suitable, metal is most pre¬ ferred. In the present invention, the preferred foamed-in-place insula¬ tion 4 is polyurethane foam. Polyurethane foam can be prepared by mixing intimately under reaction conditions an organic polyiso- cyanate with an isocyanate reactive, active hydrogen-containing compound such as, for example, a polyol in the presence of a blowing agent and introducing the foam-forming mixture into the space between the inner cabinet 3 and outer metal shell 2 of the cabinet. Blowing agents employed in the preparation of the polyurethane are generally organic compounds having an atmospheric boiling point of from about -50°C. to about +100°C. Generally, such compounds selected for this purpose are halogenated organic compounds especially those containing fluorine and or chlorine as this additionally helps confers good thermal insulation proper¬ ties to the foam. In the present invention, the preferred blowing agent for use in preparing the polyurethane foam 4 are those comprising a hydroha- locarbon. Hydrohalocarbons are preferred over perhalogenated carbon compounds due to their generally lower ozone depleting potentials, though the use of perhalogenated carbon compounds such as tric lorofluoromethane and dichlorodifluoromethane in small amounts is not precluded from the present invention. Suitable hydrohalocarbon compounds include hydrochlorofluorocar- bons, hydrofluorocarbons and hydrochlorocarbons, particularly those having 1 to 3 carbon atoms due to their suitable boiling points. Preferred blowing agents for preparing the insulative polyure- thane foam used in the present invention include dichlorofluoroe- thane and its isomers, chlorodifluoroethane and its isomers, te- trafluorethane and its isomers and 1, 1,1-trichloroethane due to availability, ease of handling and the desirable physical proper¬ ties of polyurethane foams prepared therewith. However, those skilled in the art will appreciate that the use of other polyure¬ thane foam blowing agents is within the scope of the instant in¬ vention. The blowing agent is employed in quantities sufficient to provide for a foam having an overall bulk density of from about 10 to about 200, preferably about 15 to about 100, and more preferably about 18 to about 60 kg/m 3 . Active hydrogen-containing compounds which are useful in the preparation of the polyurethane foam include those materials hav¬ ing two or more groups which contain an active hydrogen atoms which can react with an isocyanate. Collectively, such compounds are referred to as polyahls. Preferred among such polyahl compounds are those having at least two hydroxyl, primary or sec- ondary amine, carboxylic acid, or thiol groups per molecule. Polyols, i.e., compounds having at least two hydroxyl groups per molecule, are especially preferred due to their desirable reac¬ tivity with polyisocyanates. Suitable isocyanate reactive materials for preparing rigid poly- urethanes include those having an equivalent weight of about 50 to about 700, preferably about 70 to about 300 and more Prefer- ably about 70 to about 150. Such isocyanate-reactive materials also advantageously have a functionality of at least 2, prefer¬ ably about 3, up to about 16, preferably up to about 8, active hydrogen atoms per molecule. Suitable additional isocyanate-reactive materials include poly¬ ether polyols, polyester polyols, polyhydroxyl-terminated acetal resins, hydroxyl-terminated amines and polyamines, and the like. Most preferred for preparing rigid foams, on the basis of perfor- mance, availability and cost, is a polyether polyol prepared by adding an alkylene oxide to an initiator having from about 2 to about 8, preferably about 3 to about 8 active hydrogen atoms. Polyisocyanates useful in making polyurethanes include aromatic, aliphatic and cycloaliphatic polyisocyanates and combinations thereof. Representative of these types are diisocyanates such as m- or p-phenylene diisocyanate, toluene-2,4-diisocyanate, tolu- ene-2, 6-diisocyanate, hexamethylene-1, 5-diisocyanate, tetramethy- lene-1,4-diisocyanate, eyelohexane-1,4-diisocyanate, hexahydroto- luene diisocyanate (and isomers), naphthalene-1, 5-diisocyanate, l-methylphenyl-2,4-phenyldiisocyanate, diphenylmethane-4,4 '-di- iso-cyanate, diphenylmethane-2,4'-diisocyanate, 4,4'-biphenylene- diisocyanate, 3, 3'-dimethoxy-4,4'-biphenylenediisocyanate and 3,3'-dimethyldiphenylpropane-4,4'-diisocyanate; triisocyanates such as toluene-2,4, 6—triisocyanate and polyisocyanates such as 4,4'-dimethyldiphenylmethane-2,2' , 5' ,5'-tetraisocyanate and the diverse polymethylene polyphenylpolyisocyanates. A crude polyisocy nate may also be used in the practice of this invention, such as the crude toluene diisocyanate obtained by the phosgenation of a mixture of toluene diamines or the crude diphenylmethane diisocyanate obtained by the phosgenation of crude diphenylmethanediamine. Especially preferred are methylene-bridged polyphenyl polyiso¬ cyanates, due to their ability to crosslink the polyurethane. The isocyanate index (ratio of equivalents of isocyanate to equiva¬ lents of active hydrogen-containing groups) is advantageously from about 0.9 to about 5.0, preferably about 0.9 to about 3.0, more preferably about 1.0 to about 1.5. In addition to the foregoing critical components, it is often de¬ sirable to employ certain other ingredients in preparing cellular polyurethane. Among these additional ingredients are water, catalyst, surfactant, flame retardant, preservative, colorant, antioxidants, reinforcing agent, filler, and the like. Water is often employed in the role as a blowing agent precursor and processing aid. Water can react with isocyanate leading to the generation of carbon dioxide gas which then functions as a blowing agent in the foam-forming reaction. When present, the water is preferably used in amounts not exceeding about 7, pre¬ ferably about 6, more preferably about 5 parts by weight per 100 parts by total weight active hydrogen-containing compound(s) present. Beneficial effects are seen when at least about 0.5 and preferably at least about 1 part of water per 100 parts total weight active hydrogen-containing compound(s) is present. Using amounts of water which exceed these ranges is possible but the resulting foam may have undesirable physical properties such as poor dimensional stability and poor thermal insulation. In making polyurethane foam, it is generally highly preferred to employ a minor amount of a surfactant to stabilize the foaming reaction mixture until it cures. Such surfactants advantageously comprise a liquid or solid organosilicone surfactant. Other, less preferred surfactants include polyethylene glycol ethers of long chain alcohols, tertiary amine or alkanolamine salts of long chain alkyl acid sulfate esters, alkyl sulfonic esters and alkyl arylsulfonic acids. Such surfactants are employed in amounts suf¬ ficient to stabilize the foaming reaction mixture against col¬ lapse and the formation of large, uneven cells. Typically, about 0.2 to about 5 parts of the surfactant per 100 parts by total weight active hydrogen-containing compound(s) present are gener¬ ally sufficient for this purpose. One or more catalysts for the reaction of the active hydrogencon- taining compound(s) with the polyisocyanate are advantageously used. Any suitable urethane catalyst may be used, including ter¬ tiary amine compounds and organometallic compounds. Exemplary tertiary amine compounds include triethylenediamine, N-methyl morpholine, pentamethyldiethylenetriamine, tetramethylethylene- diamine, l-methyl-4-dimethylaminoethylpeperazine, 3-methoxy- N-diethyl-propylamine, N-ethyl morpholine, diethylethanol-amine, N,N-dimethyl-N' ,N'-dimethyl isopropylpropylenediamine, N-N-die- thyl-3-diethylaminopropylamine, dimethylbenzylamine and the like. Exemplary organometallic catalysts include organomercury, organo- lead, organoferric and organotin catalysts, with organotin catalysts being preferred among these. Suitable tin catalysts in¬ clude stannous chloride, tin salts of carboxylic acids such as dibutyltin di-2-ethyl hexanoate as well as other organometallic compounds. A catalyst for the trimerization of polyisocyanates, such as an alkali metal alkoxide, may also optionally be employed herein. Such catalysts are used in an amount which measurably in¬ creases the rate of reaction of the polyisocyanate. Typical amounts are about 0.001 to about 1 parts of catalyst per 100 parts by total weight of active hydrogen-containing compoun (s) present. In making a polyurethane foam, the active hydrogen-containing compound(s), polyisocyanate and other components are contacted, thoroughly mixed and permitted to react and to expand and cure into a cellular polymer. The particular mixing apparatus is not critical, and various types of mixing head and spray apparatus are conveniently used. It is often convenient, but not necessary, to pre-blend certain of the raw materials prior to reacting the polyisocyanate and active hydrogen-containing components. For example, it is often useful to blend the active hydrogen-contain¬ ing compounds (s) , blowing agent, surfactants, catalysts and other components except for polyisocyanates, and then contact this mix¬ ture with the polyisocyanate. Alternatively, all components can be introduced individually to the mixing zone where the polyiso¬ cyanate and polyols (s) are contacted. It is also possible to pre- react all or a portion of the active hydrogen-containing compound(s) with the polyisocyanate to form a prepolymer, al¬ though such is not preferred. EXAMPLES The following examples are given to illustrate the invention and should not be interpreted as limiting in any way. Unless other¬ wise stated, all parts and percentages are given in percent by weight. Example I Dichlorodifluoroethane Blistering Study Sheets of a high impact polystyrene, characterized by a nominal flow rate of 2.6 g/10 min (measured according to ASTM D1238, Condition G) , PS7100/protective barrier layer structures were ex¬ posed to the vapor of liquid dichlorodifluoroethane (HCFC 141-6) at 35°C by sealing sheet samples over the bottle opening. The sheet samples were prepared by compression laminating protective layer to PS7100 to have 2 mil layer on 28 mil PS7100. Barrier layers of various compositions described in Table 1 were prepared by compounding with a single screw extruder at 200°C. The effects of dichlorodifluoroethane diffusion through the specimens was monitored for chemical attack. Time was recorded when blistering occurred and the results are set forth in Table 1. The adhesion of the protective barrier layers to PS-7100 was evaluated by a hand pull peel strength test. Adhesion test results are included in Table 1. Table 1 - Dichlorodifluoroethane Blistering Test (Dichlorodifluoroethane vapor at 35°C) Sheet structure: 28 mil PS7100 bulk layer 2 mil protective layer Samples Protective Layer Protective Hours to Bonding Test No. Composition Layer Blister Thickness, mil 1 None (30 mil 0 2-3 — PS7100 alone) 2 LM-6187 HDPE 2 48-50 Poor 3 Plexar PX209 2 150-160 Poor 4 85% LM-6187 HDPE 2 16-18 Fair 15% Stereon 840A 1 5 85% Plexar PX209 2 94-96 Fair 15% Stereon 840A 1 6 43% LM-6187 HDPE 2 6-8 Good 42% PS5350 HIPS 15% Stereon 840A 7 43% Plexar PX209 2 16-18 Good 42% PS5350 HIPS 15% Stereon 840A 8 43% Plexar PX209 2 16-18 Good 42% PS5350 HIPS 15% FinaClear 520 9 50% Plexar PX209 2 22-26 Good 35% PS5350 HIPS 15% Stereon 840A Materials Plexar PX209: Quantum maleic anhydride modified HDPE. (modified polyolefin (i)) LM-6187: Quantum HDPE with d=0.96, MPI=1.15. (polyolefin (iii)) PS5350: BASF high impact polystyrene, (styrenic based polymer (iv) ) Stereon 840A: Firestone S-B-S tri-block copolymer. (rubber (ii) ) FinaClear 520: Fina S-B-S tri-block copolymer. (rubber (ii)) Example 2 Reqrind Compatibility The regrind compatibility of a protective layer was evaluated by testing properties of specimens injection molded from blends con¬ taining 15% of protective layer, 83.5% P57100, and 1.5% PS7800. Results Summarized in Table 2 illustrated that protective layer compositions provide excellent regrind compatibility. While the samples discussed below exhibit optimum regrindability, it is an¬ ticipated that from 0.3 percent to 3 percent additional rubber (iii) could be incorporated into the remaining samples of Table 1 to enhance their regrind compatibility. Table 2: Regrind Compatibility Study Results A B C D E F G PS7100 98 83.5 83.5 83.5 83.5 83.5 83.5 PS7800 2 1.5 1.5 1.5 1.5 1.5 1.5 Sample 7 - 15 - - - - - Sample 8 - - 15 - - - - Sample 9 - - - 15 - - - Sample 10 - - - - 15 15 - Sample 15 - - - - - - - Sample 16 - - - - - - 15 MFR (200.0°C, 2.9 3.1 2.9 3.1 3.1 3.3 3.7 5. Okg) Vicat (°C) 101 102 102 102 102 102 102 Tensile 2485 2632 2689 2630 2694 2952 2946 Yield (psi) Tensile 3721 3773 3945 3738 3925 4024 3960 Break (psi) Tensile 54 75 77 74 68 68 63 Elongation (%) Tensile Mo¬ 181 179 176 169 176 177 175 dulus (Kpsi) Izod Impact 2.1 2.8 2.7 2.5 2.6 2.4 2.4 (ft-lbs/in) Gardner (in- 229 203 >320 204 312 243 210 lbs) Materials PS7100: BASF high impact polystyrene. PS7800: BASF high impact polystyrene. It should be understood that while the invention herein shown and described constitutes the preferred embodiment of the invention, it is not intended to illustrate all possible forms thereof. Var¬ ious embodiments of the inventions disclosed herein can be created by one or ordinary skill in the art without departing from the spirit and scope of the invent ion disclosed and claimed.

Claims: We claim: 1. A composition which is resistant to the action of polyure- thane foam blowing agents, the composition comprising: (i) an effective amount of a modified polyolefin; and (ii) an effective amount of a rubber. 2. The composition of claim 1 comprising: (i) from 1 to 70 parts by weight of a modified polyolefin; (ii) from 1 to 40 parts by weight of a rubber; (iii) from 0 to 90 parts by weight of a polyolefin selected from the group consisting of polyethylene, poly¬ propylene, polybutylene, and copolymers thereof and (iv) from 0 to 50 parts by weight of a styrenic based poly- ' mer; wherein all parts by weight sum up to the total weight of the composition. 3. The composition of claim 1 or 2 wherein the modified poly¬ olefin (i) is a polyethylene modified with a compound se- lected from the group consisting of maleic anhydride, maleic acid, maleic anhydride derivatives, maleic acid derivatives, and mixtures thereof. 4. The composition of either one of the claims 1 to 3 wherein rubber (ii) is a synthetic block copolymer rubber selected from the group consisting of styrene-butadiene diblock sty- rene-butylene-styrene triblock styrene-ethylene/butylene-sty- rene triblock; styreneethylene/butylene-styrene triblock functionalized with maleic anhydride, maleic acid or admix- tures thereof; or mixtures thereof. 5. The composition of either one of the claims 1 to 4 wherein polyolefin (iii) is an HDPE having a density of between 0.940 and 0.970 and a melt index of 1.00 to 1.30. The composition of either one of the claims 1 to 5 wherein the styrenic based polymer (iv) is HIPS. 7. A barrier layer capable of protecting one or more first lay¬ ers from the action of polyurethane foam blowing agents, the barrier layer comprising composition of either one of the claims 1 to 6. 5 8. A thermoformable composite comprising: (I) a functional layer comprising one or more sublayers of one or more styrenic based polymers; and 10 (II) a barrier layer of claim 7 adhered to at least one surface of the functional layer. 9. The thermoformable composite of claim 8 comprising: 15 50 to 99 parts by weight of the functional layer (I); and 1 to 50 parts by weight of the barrier layer (II); wherein all parts by weight add up to the total weight of the thermoformable composite. 20 10. An insulative cabinet wall structure, comprising (I) a functional layer comprising one or more sublayers of one or more styrenic based polymers; and 25 (II) a barrier layer of claim 7 adhered to at least one surface of the functional layer (III) an outer structural wall; and (IV) insulation adhered to both the barrier layer (II) and the outer structural wall (III) so as to be placed there- 30 between. 35 40 45

Inventors: SHU HRONG-ROANG, SHU, HRONG-ROANG
Applicants: BASF AG, BASF CORP, BASF AKTIENGESELLSCHAFT, BASF CORPORATION
Application year: 1995
Main classification: C08L51
IPC codes: B32B25, B32B27, C08L23, C08L25, C08L51, C08L53, F25D23