PROCESS FOR PRODUCTION OF LOW DENSITY WATER-BLOWN RIGID FOAMS WITH FLOW AND DIMENSIONAL STABILITY

Abstract: The invention provides a method for making water-blown closed cell rigid foams comprising using as a polymer base a polyol selected from the group consisting of: (a) a polyester polyol with an average functionality of at least 1.6 and an OH value of at least 200; and (b) a polyether polyol with an average functionality of at least 2 and an OH value of at least 200. The invention also provides water-blown closed cell rigid foams comprising a polymer base selected from the group consisting of: (a) a polyester polyol with an average functionality of at least 1.6 and an OH value of at least 200; and (b) a polyether polyol with an average functionality of at least 2 and an OH value of at least 200.

Description: PROCESS FOR PRODUCTION OF LOW DENSITY WATER-BLOWN RIGID FOAMS WITH FLOW A DIMENSIONAL STABILITY BACKGROUND OF THE INVENTION This application is a continuation-in-part of U.S. Patent Application Serial No. 07/937,052, filed August 27, 1992. Field of the Invention This invention is in the field of water-blown foams and the method for production of such foams. Description of the Prior Art U.S. Patent No. 5,010,116 describes a water-blown foam consisting of a mixture of polyether polyols, amine, organo etallic and triazine/quaternary ammonium salt catalysts, surfactant, and 0.4%-4.0% water reacted with diphenylmethane diisocyanate. Although the density of the foam is not indicated, it would be expected that a free rise cup density of at least 1.8 lbs./cu.ft. would be obtained with a formulation containing 4.0% water. U.S. Patent No. 5,070,115 describes the process for producing a rigid foam from reacting an organic isocyanate with a mixture consisting of a polyester polyol with an OH value of at least 150, and/or a polyether polyol with an OH value of at least 200 which is combined with a polyether with an OH value less than 100. An NCO/OH ratio of 100-130 is used. The foam may have a density between 1.25 and 12.5 lbs./cu.ft. The examples cited use 4.0 parts of water and have densities ranging from 2.05 to 2.75 lbs./cu.ft. European Patent Application No. 450,197 Al describes foam formulations suitable for preparing water-blown heat- insulating material using polyols as softening point improvers and heat-insulating material obtained therefrom. European Patent Application No. 408,408 describes methods of producing rigid urethane foam by reacting blend polyol with polyisocyanate and water as blowing agent. Because several fully halogenated hydrocarbons (chlorofluorocarbons, commonly referred to as CFC's) normally used as blowing agent are believed to cause environmental problems (for instance, their role in the deterioration of the stratospheric ozone layer) , there is much effort in research for developing an alternative blowing agent that may (partly or wholly) replace the halogenated hydrocarbon as blowing agent in the standard foam formulations. It was recognized that water, functioning as a reactant forming carbon dioxide (C0 2 ) which acts as a chemical blowing agent, might replace the objected halogenated hydrocarbons. For example, European patent application published under No. 0,358,282 discloses foam formulations useful in the preparation of soft flexible polyurethane foam comprising water which is added as a replacement for chlorofluorocarbons. The reaction between the isocyanate and water produces carbon dioxide gas. The use of polyester polyols in formulations with high water levels and amine catalysts usually results in base catalyzed hydrolysis of the polyester. The hydrolysis of the polyester in the blend dramatically reduces the shelf- life of the resin blend. High molecular weight polyethers are typically employed in amounts of at least about 10% to improve the surface adhesion of the foam and to reduce surface friability. SUMMARY OF THE INVENTION The present invention provides a water-blown urethane foam which could be molded at a 1.9 minimum in-place density and which would exhibit flowability and dimensional stability comparable to a CFC-blown system of the same density. The invention relates to the production of a rigid foam made from reacting an organic isocyanate with a mixture of polyols, water, surfactants, catalysts, and other additives such as flame retardants, fillers, and viscosity modifiers. The sole blowing agent is carbon dioxide formed by the reaction of water and isocyanate. The ratio between the isocyanate and hydroxyl groups (including water) is between 100 and 200. The polyol mixture used as the base of the formulation consists of a polyester polyol with an average functionality of at least 1.6 and a hydroxyl value greater than 200 and/or a polyether polyol with an average functionality of at least 2.0 and a hydroxyl value of at least 200. A polyether polyol with an average functionality of at least 1.6 and a hydroxyl value of less than 120 may also be included in the mixture. The resultant foams have a free rise cup density between about 1 and about 2.5 lbs./cu.ft., and are useful for pour-in-place and spray applications. Such applications include pipe insulation and a variety of void filling applications such as, for example, residential and commercial insulation, appliance (e.g., refrigerators and freezers) insulation, and also as flotation for boats and other watercraft. The invention produces low density foams which flow well, are stable and exhibit excellent adhesion to metal and treated thermoplastic substrates. Whereas the previous state-of-the art only allowed for commercially viable foam with a minimum in-place density of about 2.4 lbs./cu.ft., the present invention enables in-place densities of as low as 1.9 lbs./cu.ft. to be achieved. Thus, the invention yields commercially viable foams prepared without chlorofluorcarbons having excellent flow and dimensional stability at the desired lower densities, densities unobtainable in prior art foams prepared without chlorofluorocarbons at required flow and dimensional stabilities. The urethane foams of the invention are dimensionally stable at lower densities than have been possible from the teachings of the prior art. The lower densities are obtained by employing higher amounts of water with polyol blends comprised mostly of polyester. The invention further provides resin blends useful for preparing the urethane foams of the invention where the blends have dramatically increased shelf-life. DETAILED DESCRIPTION OF TH INVENTION The present invention relates to foams suitable for preparing water-blown rigid urethane foams with flow and dimensional stability. The water-blown foams are prepared by contacting a resin blend with an isocyanate. The resin blends typically comprise a mixture of polyols (the polymer base or polyol blend, water, surfactants, and catalysts) . The formulations for preparing water-blown closed cell rigid foam are as follows: PolymerBase The components of the polymer base of the resin blend composition are: parts by weight 1. a polyester polyol with an average 0 - 100 a functionality of at least 1.6 and an OH value of at least 200 2. a polyether polyol with an average 0 - 100" functionality of at least 2 and an OH value of at least 200 3. a polyether polyol with an average 0 - 10 a functionality at least 1.6 and an OH value of less than 120 ' •■ preferred quantities of polyols. The polyol blend component of the resin may be prepared to contain: (a) a polyester polyol; (b) a polyester polyol and a polyether polyol with an average functionality of at least 2 and an OH value of at least 200; (c) a polyester polyol and a polyether polyol with an average functionality of at least 1.6 and an OH value of less than 120; (d) a polyether polyol with an average functionality of at least 2 and an OH value of at least 200; (e) a polyether polyol with an average functionality of at least 2 and an OH value of at least 200 and a polyether polyol with an average functionality of at least 1.6 and an OH value of less than 120; or (f) a polyester polyol, a polyether polyol with an average functionality of at least 2 and an OH value of at least 200, and a polyether polyol with an average functionality of at least 2 and an OH value of less than 120. In more preferred embodiments of the invention, the polyol blend will contain between about 50-90 parts by weight of the polyester polyol; in particularly preferred embodiments the polyester polyol will be present in the polyol blend at about 70-90 parts by weight. In more preferred embodiments of the invention, the polyol blend will contain between about 5-50 parts by weight of a polyether polyol with an average functionality of at least 2 and an OH value of at least 200; a most preferred embodiment will contain between about 10 and 30 parts by weight of this polyol. The polyether polyol with an average functionality of at least 1.6 and an OH value of less than 120 will be present in more preferred embodiments at between about 5-10 parts by weight. Examples of polyether polyols suitable in the present invention are alkoxylated diols, triols and higher OH or amino-functional starting materials, such as propoxylated mono- or diethylene glycol, propoxylated glycerol, propoxylated pentaerythritol, propoxylated sorbitol, etc. Other examples of suitable polyols are polyols prepared by ethoxylating or ethoxylating/propoxylating said starting materials. The high molecular weight polyethers suitable for use in accordance with the invention are known and may be obtained, for example, by polymerizing epoxides such as ethylene oxide, propylene oxide, butylene oxide, tetrahydrofuran, styrene oxide or epichlorohydrin in the presence of BF 3 or by chemically adding these epoxides, preferably ethylene oxide and propylene oxide, in admixture or successively to components containing reactive hydrogen atoms such as water, alcohols or amines. Polyethers modified by vinyl polymers, of the type formed, for example, by polymerizing styrene or acrylonitrile in the presence of polyether (U.S. Pat. Nos. 3,383,351; 3,304,273; 3,523,093; and 3,110,695; and German Patent 1,152,536), are also suitable, as are polybutadienes containing OH groups. In addition, polyether polyols which contain high molecular weight polyadducts or polycondensates in finely dispersed form or in solution may be used. Such modified polyether polyols are obtained when polyaddition reactions (e.g., reactions between polyisocyanates and amino functional compounds) or polycondensation reactions (e.g., between formaldehyde and phenols and/or amines) are directly carried out in situ in the polyether polyols. Suitable examples of polyesters include the reaction products of polyhydric, preferably dihydric alcohols (optionally in the presence of trihydric alcohols) , with polyvalent, preferably divalent, carboxylic acids. Instead of using the free carboxylic acids, it is also possible to use the corresponding polycarboxylic acid anhydrides or corresponding polycarboxylic acid esters of lower alcohols or mixtures thereof for producing the polyesters. The polycarboxylic acids may be aliphatic, cycloaliphatic, aromatic, and/or heterocyclic and may be unsaturated or substituted, for example, by halogen atoms. The polycarboxylic acids and polyols used to prepare the polyesters are known and described for example in U.S. Patents Nos. 4,644,029 and 4,644,047, and 4,644,048, herein incorporated by reference in their entirety. Suitable polythioethers, polyacetals, polycarbonates and other polyhydroxyl compounds are also disclosed in the above identified U.S. patents. Finally, representatives of the many and varied compounds which may be used in accordance with the invention may be found for example in High Polymers, Volume XVI, "Polyurethanes, Chemistry and Technology," by Saunders-Fritsch, Interscience Publishers, New York, London, Vol. I, 1962, pages 32-42 and 44-54, and Volume II, 1964 pages 5-6 and 198-199; and in Kunstoff- Handbuch, Vol. VII, Vieweg-Hochtlen, Carl Hanser Verlag, Munich, 1966, pages 45-71. Additional Resin Blend Components The other components of the resin composition are water, about 5-12 parts by weight, surfactant, about 0-5.0 parts by weight, amine catalyst, about 0-7.0 parts by weight, and isocyanurate catalyst, about 0-5.0 parts by weight. Water is added to the polyol blend as required to control the density of the resultant foam. The amount of water is from about 5 to 12 parts by weight, and more preferably 5-8 parts by weight based on 100 parts of the polyol resin blend. The above resin composition is reacted with an organic isocyanate with an average functionality of at least 2.0 at an NCO/OH ratio between about 100 and 200 to produce the foam. The resin blend and isocyanate are mixed with commercially available equipment. The resulting foam is suitable for pour-in-place and spray applications for rigid insulation, void-filling, and structural uses such as appliances, recreational products, and composite structures. By OH value is meant hydroxyl value, a quantitative measure of the concentration of hydroxyl groups, usually stated as mg KOH/g, i.e. , the number of milligrams of potassium hydroxide equivalent to the hydroxyl groups in lg of substance. By NCO/OH ratio, or NCO/OH index, is meant 100 times the actual molar ratio of isocyanate groups to hydroxyl groups (including those contributed by water) in the reaction between the polyol blend and the polyisocyanate. By functionality is meant the number of reactive groups, e.g. , hydroxyl groups, in a chemical molecule. By free rise cup density is meant the average density, in pounds per cubic foot (lbs./cu.ft.), of the foam in a paper (free rise) cup. It is determined by adding the formulation to the cup of known volume, allowing the foam to form, removing excess foam from above the upper rim of the cup, weighing the cup, and determining the density. By free rise density is meant the density, in lbs./cu.ft., of a core foam sample removed from a foam prepared in a paper cup. Because the core of a foam sample is less dense than the exterior, the free rise density value is normally lower than the free rise cup density. By molded core density is meant the density, in lbs./cu.ft., of a core sample of foam removed from a foam prepared in a mold. By molded overall density is meant the average density, in lbs./cu.ft., of a foam prepared in a mold. Polvisocγanate Component Examples of polyisocyanates useful in the process of preparing polyurethane foams are well-known in the art, and are selected from, for instance, aliphatic, cycloaliphatic, and preferably aromatic polyisocyanates; and combinations thereof. Representatives of these types are diisocyanates such as 2,4-toluene diisocyanate, 2,6-toluene diisocyanate, mixtures of 2,4- and 2,6-toluene diisocyanate, 1,5-naphthene diisocyanate, 2,4-methoxyphenyl diisocyanate, 4,4'- diphenylmethane diisocyanate, 4,4'-biphenylene diisocyanate, 3,3 '-dimethoxy-4,4'-biphenylene diisocyanate, 3 ,3'-dimethyl- 4,4'-biphenylene diisocyanate, and 3 ,3'-dimethyl-4,4'- diphenyl ethane diisocyanate; triisocyanates such as 4,4'4"- triphenylmethane triisocyanate, and 2,4, 6-toluene triisocyanate; and the tetraisocyanates such as 4,4'- dimethyl-2,2' ,5,5'-diphenylmethane tetraisocyanate; and polymeric isocyanates such as polymethylenepolyphenylene polyisocyanate. In order to form the polyurethane foam, a catalyst useful in preparing foams is employed in the usual manner. Suitable catalysts that may be used are described in European Patent Application No. 0,358,282, and include: tertiary amines such as, for example triethylenediamine, N- methylmorpholine, N-ethylmorpholine, diethylethanolamine, N- cocomorpholine, l-methyl-4-dimethylaminoethylpiperazine, 3- methoxypropyldimethylamine, N,N,N -tri ethy1isopropy1 propylenediamine, 3-diethylaminopropyl-diethylamine, dimethylbenzylamine, dimethylcyclohexylamine, and the like. It has been unexpectedly discovered that resin blends prepared with specific amine catalysts have dramatically improved shelf lives compared to resins prepared with other catalysts. The specific amine catalysts are especially suitable for use in resin blends with polyester polyols and higher amounts (at least 4.5%) of water. These amine catalysts are dimethylaminoethoxyethanol (DMAEE) and 70% bis (2-dimethylaminoethyl) ether in dipropylene glycol. One skilled in the art will recognize that modifications may be made in the present invention without deviating from the spirit or scope of the invention. The invention is illustrated further by the following examples which are not to be construed as limiting the invention or scope of the specific procedures described herein. Example 1 General Procedures for Making Water-blown Foams Three five-gallon pails of resin blend were prepared by weighing into each: Stepanpol®PS-2502A 15000g Stepanpol®PE-3603 3000g Stepanpol®PS-3708 2000g Water HOOg Dabco DC5357 400g DMAEE 200g Dabco K-15 400g The pails were mixed on a roller until a uniform mixture was obtained. The resin blend was added to the resin storage tank of a Cannon H-100 metering machine. The isocyanate storage tank contained Mondur MR. The machine was set up with the following process parameters: A .35 second shot was dispensed into a Lily IT10 paper cup. The following data was recorded: Cream time 4 seconds Gel time 28 seconds Cup density 1.54 lbs./cu.ft. Free Rise Density 1.25 lbs./cu.ft. A 0.58 second shot was dispensed into a 15"xl5"x4" mold lined with polyethylene for release purposes. The following physical properties were measured: Overall density 2.33 lbs./cu.ft. Core density 1.93 lbs./cu.ft. Compressive Strength parallel 27.0 psi perpendicular 18.4 psi K-factor, initial 0.160 BTU in./hr.ft. 2 °F Shear strength 18.8 psi Tensile strength 37.8 psi Closed cell constant 96.1 % Dimensional Stability 28 days @ -20°F 0.17 % vol. chg. 28 days § 158 ϋ F 0.69 % vol. chg. 28 days § 158°F/ 5.17 % vol. chg. 100% r.h. Example 2 Variations in Foam Pro erties Sample 1 illustrates a low density formulation which is reacted at a high NCO/OH index to improve flow and dimensional stability. Sample 2 is a slightly higher density foam which incorporates a high functionality polyether to improve dimensional stability. Sample 3 is a low density foam which is mixed at a 110 NCO/OH index, and incorporates a high functionality polyether to improve dimensional stability and a high molecular weight polyether to improve surface cure. Stepanpol®PS-2502-A is a modified diethylene glycol phthalate polyester polyol sold by Stepan Company, Northfield, Illinois, and having an OH value of about 230- 250. Stepanpol®PE-3603 is an alkoxylated glycerine polyether polyol sold by Stepan Company of Northfield, Illinois, and having an OH value of about 350-390. Stepanpol®PE-3708 is an alkoxylated sucrose polyether polyol sold by Stepan Company of Northfield, Illinois, and having an OH of about 365-395. Poly G 85-36 is an alkoxylated glycerine polyether 5 polyol sold by the Olin Corp. and having an OH value of about 36. Dabco®DC5357 is a polysiloxane surfactant composed of dimethyl, methyl (polyethylene oxide) siloxane copolymer and is sold by Air Products Corporation of Allentown, 0 Pennsylvania. Niax®A-l is a catalyst which contains about 70% bis(2- dimethylaminoethyl) ether in 30% dipropylene glycol. This catalyst is sold by Union Carbide Corporation of Danbury, Connecticut. 5 DMAEE is dimethylaminoethoxyethanol and is commercially available from Texaco as Texacat® ZR-70. Dabco®K-15 is a mixture of 75% potassium 2-ethylhexoate and 25% diethyl glycol. Mondur MR® commercially available from Miles, 0 Pittsburgh, Pennsylvania, is polymethylene polyphenyl isocyanate having an isocyanate content of about 31.5%. Example 3 A pour foam was prepared essentially as set forth in U.S. Patent No. 5,010,116 (Colafati) at column 3, lines 10- 25 56, at an NCO/OH index (ratio) of 100 and 4 parts of water per hundred parts of polyol (php) together with the highest catalyst levels described. The isocyanate used was Mondur MR, a diphenylmethane diisocyanate available from Miles, Inc. This is formulation 1 in Table 1 below. 30 Another foam was prepared essentially according to the teaching of Colafati except that the amount of water was increased to 7 php as in Example 2 of the above-identified application. The isocyanate used was Mondur MR. This is Formulation 2 in Table 1 below. Formulations 1 and 2 were 35 each molded in a 12x12x2 inch mold at a density which was 1.3 times the free rise density. Test specimens (4x4x1 inch) were cut from the core of the blocks and tested for % volume change after 7 days at 158°F. Formulations 1 and 2 and their results are shown below: TABLE 1 LHT-240 1 Poly G 74-532 2 L5420 3 Polycat 8 4 Curithane 52 5 Dabco TMR 6 Water NCO/OH Index A/B ratio 7 Material Temp. , °F Mix Time, sec. Cream Time, sec. String Time, sec. Free Rise Cup Density, lbs./cu.ft. Comments Free Rise Cup Shrinkage Molded Core density, lbs./cu.ft. % volume change, 1 week at 158 °F 1 LHT-240 is an oxyalkylated glycerine. 2 Poly G 74-532 is a rigid polyether polyol with a functionality greater than 3.8 and a hydroxyl number of from about 300-500. 3 L5420 is a polyalkylenoxidemethylsiloxane copolymer. 4 Polycat 8 is N,N-dimethylcyclohexylamine. 5 Curithane 52 is a polyisocyanurate catalyst. 6 Dabco TMR is a quaternary ammonium salt. 7 A/B ratio refers to the ratio in parts by weight of the isocyanate (A) to the resin blend (B) . Formulations prepared according to Colafati to include either 4 or 7 parts of water by weight result in foams that exhibited severe free rise cup shrinkage. These foams are inferior to foams prepared according to the invention which, to the contrary, exhibit only slight cup shrinkage. Example 4 A foam was prepared essentially as described in Example 1 of U.S. Patent No. 5,070,115 (Welte) using Mondur MR as the isocyanate. This foam is Formulation 3 in Table 2 below. Another foam was prepared essentially according to Example 1 of Welte using Mondur MR as the isocyanate except that the amount of water was increased to 7 php as in Example 2 of the above-identified patent application. This foam is Formulation 4 in Table 2 below. Formulations 3 and 4 were each molded in a 12x12x2 inch mold at a density which was 1.3 times the free rise density. Test specimens (4x4x1 inch) were cut from the core of the blocks and tested for % volume change after 7 days at 158°F. Formulations 3 and 4 and their results are shown below: TABLE 2 # 3 #4 Multronol E-9111 1 30.00 30.00 Poly G 74-532 70.00 70.00 Tegostab B8421 2 2.50 2.50 Polycat 8 0.45 0.45 Water 4.00 7.00 NCO/OH Index 94 94 A/B ratio 3 130/100 165/100 Material Temp., °F 90 90 Mix Time, sec. 4 4 Cream Time, sec. 57 69 String Time, sec. 129 259 Free Rise Cup Density, 2.00 extreme shrinkage lbs./cu.ft. prevented density determination Cup Shrinkage severe extremely severe Molded Core density, lbs./cu.ft. 1.96 1.61 % volume change, 1 week at 158 -1.3 -1.8 °F Multronol E-9111 is a ethylene oxide capped polyether diol having an OH number of 28 and is available from Miles, Inc. Tegostab B8421 is a polyether siloxane silicone stabilizer. A/B ratio refers to the ratio in parts by weight of the isocyanate (A) to the resin blend (B) . Blends prepared according to Welte were not phase stable, i.e.. the flexible polyol was not compatible with the rigid polyol at 4 or 7 parts of water. At 7 parts of water, the separated phase was not pourable. Moreover, formulations 3 and 4 prepared according to Welte to include either 4 or 7 parts of water by weight result in foams that exhibited severe or extremely severe cup shrinkage. These foams are clearly inferior to foams prepared according to the invention which exhibit only slight cup shrinkage. In comparison, a foam prepared using 7 parts of water according to Example 2, Sample l, has the following dimensional stability: Free Rise Cup Density, lbs./cu.ft. 1.4 Molded core density, lbs./cu.ft. 1.59 % Volume Chg., 1 week@ 158°F -1.8 Example 5 Foams were prepared according to the invention essentially as described above to contain the following components: Formulation Number aged 5 days at 50°C. Pentamethyldiethylenetriamine. Trimethylaminoethylethanolamine. Tris-(3-dimethylaminopropyl)amine. Pentamethyldipropylenetriamine. The above data indicate that Niax A-l and Texacat ZR-70 provide dramatically improved shelf-life. From the foregoing, it will appreciated that although specific embodiments of the invention have been described herein for purposes of illustration, various modifications may be made without deviating from the spirit or scope of the invention.

Claims: WHAT IS CLAIMED IS: 1. In a process for making water-blown closed cell rigid foam of the type where an isocyanate is reacted with a polymer base containing at least one polyol, the improvement comprising preparing the polymer base to contain from about 5 to 8 parts by weight of water and a polyol selected from the group consisting of: (a) a polyester polyol with an average functionality of at least 1.6 and an OH value of at least 200; and (b) a polyether polyol with an average functionality of at least 2 and an OH value of at least 200. 2. The process of claim 1 wherein the polymer base contains 1 to 10%, by weight, of a polyether polyol with an average functionality of at least 1.6 and an OH value of less than 120. 3. The process of claim 1 wherein the polymer base is reacted with an organic isocyanate with an average functionality of at least 2 at an NCO/OH ratio between 100 and 200. 4. The process of claim 1 wherein the polymer base comprises between 50-90% by weight of a polyester polyol with an average functionality of at least 1.6 and an OH value of at least 200. 5. The process of claim 4, wherein the polyester polyol is present in the polymer base at between about 70- 90% by weight. 6. The process of claim 1, wherein the polymer base comprises between about 5-50% by weight of a polyether polyol with an average functionality of at least 2 and an OH value of at least 200. 7. The process of claim 6, wherein the polyether with an average functionality of at least 2 and an OH value of at least 200 is present in the polyol blend at about 10-30% by weight. 8. The process of claim 2, wherein the polyether polyol with an average functionality of at least 1.6 and an OH value of less than 120 is present in the blend at about 5-10%. 9. A water-blown foam made according to the process of claim 1 wherein the free rise density is between about 1 and about 2.5 pounds/ft 3 . 10. A water-blown closed cell rigid foam comprising an isocyanate and a polymer base containing from about 5 to 8 parts by weight of water and a polyol selected from the group consisting of: (a) a polyester polyol with an average functionality of at least 1.6 and an OH value of at least 200; and (b) a polyether polyol with an average functionality of at least 2 and an OH value of at least 200. 11. A water-blown closed cell rigid foam of claim 10 further comprising about l to 10 percent by weight of a polyether polyol with an average functionality of at least 1.6 and an OH value of less than 120. 12. The water-blown closed cell rigid foam of claim 11 wherein the polymer base comprises a polyester polyol with an average functionality of at least 1-6 and an OH value of at least 200. 13. The process of claim 10 wherein the polymer base comprises between 50-90% by weight of a polyester polyol with an average functionality of at least 1.6 and an OH value of at least 200. 14. The process of claim 11, wherein the polyester polyol is present in the polymer base at between about 70- 90% by weight. 15. The process of claim 10, wherein the polymer base comprises between about 5-50% by weight of a polyether polyol with an average functionality of at least 2 and an OH value of at least 200. 16. The process of claim 15, wherein the polyether with an average functionality of at least 2 and an OH value of at least 200 is present in the polymer base at about 10-30% by weight. 17. The process of claim 11, wherein the polyether polyol with an average functionality of at least 1.6 and an OH value of less than 120 is present in the blend at about 5-10%. 18. The water-blown closed cell rigid foam of claim 10, wherein the polymer base comprises a polyether polyol with an average functionality of at least 2 and an OH value of at least 200. 19. The water-blown closed cell foam of claim 10, wherein the polymer base comprises about 75% by weight of a polyester polyol with an average functionality of at least 1.6 and an OH value of at least 200, about 15% by weight of a polyether polyol with an average functionality of at least 2 and an OH value of at least 200, and about 10% by weight of a polyether polyol with an average functionality of at least 1.6 and an OH value of less than 120. 20. A water-blown closed cell rigid foam of claim 18 wherein the free rise density is between 1.30 and 2.5 lbs./cu.ft.. 21. The water-blown closed cell foam of claim 10, wherein the polymer base comprises about 75% by weight of a polyester polyol with an average functionality of at least 1.6 and an OH value of at least 200, and about 25% by weight of a polyether polyol with an average functionality of at least 2 and an OH value of at least 200. 22. The water-blown closed cell foam of claim 10, wherein the polymer base comprises about 80% by weight of a polyester polyol with an average functionality of at least 1.6 and an OH value of at least 200, and about 20% by weight of a polyether polyol with an average functionality of at least 1.6 and an OH value of less than 120. 23. A process for preparing a water-blown closed cell rigid foam comprising reacting an isocyanate with a polymer base containing from about 5 to 8 parts by weight of water and a polyester polyol with an average functionality of at least 1.6 and an OH value of at least 200; where the polymer base has less than about 10% of a polyether polyol with an average functionality of at least 2 and an OH value of at least 200. 24. In a process for making a water-blown closed cell urethane foam of the type where an isocyanate is reacted with a resin blend containing at least one polyol, the improvement comprising preparing the resin blend to contain at least 4.5% water and an amine catalyst selected from the group consisting of dimethylaminoethoxyethanol and bis(2- dimethylaminoethyl) ether

Inventors: MAGNUS GEORGE, MOSTER JOANNE M, SCHUMACHER DONALD W, MAGNUS, GEORGE, MOSTER, JOANNE, M., SCHUMACHER, DONALD, W.
Applicants: MAGNUS GEORGE, MOSTER JOANNE M, SCHUMACHER DONALD W, STEPAN CO, STEPAN COMPANY
Application year: 1993
Main classification: C08G18
IPC codes: C08G18