CA2523329A1 - Resin composition for use in a froth spraying system - Google Patents

Abstract

A resin composition for use in a froth spraying system for forming polyurethane foam is disclosed. The resin composition comprises a Mannich polyol, at least one additional polyol other than a Mannich polyol, and a physical blowing agent. The Mannich polyol has a viscosity of at least 4,000 centipoise at 25 °C. The physical blowing agent is selected from the group of volatile non-halogenated C2 to C7 hydrocarbons, hydrofluoro-carbons, hydrochlorocarbons, and mixtures thereof. The physical blowing agent is present in an amount of greater than 10 parts by weight based on 100 parts by weight of the resin composition. A method of forming the polyurethane foam is also provided comprising the steps of providing the resin composition and a polyisocyanate, mixing the resin composition with the polyisocyanate in a mixing chamber to form a mixture, and discharging the mixture from a dispensing gun as the resin composition reacts with the polyisocyanate to form the polyurethane foam.

Description

RESIN COMPOSITION FOR USE IN A FROTH SPRAYING SYSTEM
BACKGROUND OF THE INVENTION
1. Field of the Invention [0001] The subject invention relates to a resin composition for use in a froth spray-ing system for forming polyurethane foam.

2. Description of the Related Art [0002] Various hydrofluorocarbons (HFC's) have been investigated in the industry as blowing agents for polyisocyanate based foams due to their low or nonexistent ozo-ne depletion potentials. Such a system would allow for production of an environmen-tally friendly closed cell polyurethane foam that exhibits improved cell structure and expands at a lower temperature range. These related art systems use a resin composi-tion that includes a Mannish polyol, at least one additional polyol other than a Mannish polyol, and chemical blowing agents. The chemical blowing agents increase the cost of preparing the polyurethane foam because the chemical blowing agents react with the polyisocyanate. Therefore, additional polyisocyanate is required to form the polyure-thane foam that increases the cost of producing the polyurethane foam.

[0003] Other related art systems have used, in addition to the chemical blowing agent, lower amounts of a physical blowing agent. The physical blowing agent is typi sally selected from hydrocarbons, hydrofluorocarbons, hydrochlorocarbons, and mix-tures thereof. One such example is disclosed in United States Patent No.
6,534,556 assigned to the assignee of the subject invention. The '556 patent uses no more than 10 parts by weight of the physical blowing agent because the resin composition be-comes saturated and additional physical blowing agent can not be added. This is par-ticularly true when the physical blowing agent is R-134a. Additionally, using an amount of 10 parts by weight or less of the physical blowing agent reduces the cost of produc-ing the polyurethane foam.
BRIEF SUMMARY OF THE INVENTION AND ADVANTAGES

[0004] The subject invention provides a resin composition for use in a froth spray-ing system for forming polyurethane foam. The resin composition comprises a Mannish polyol, at least one additional pofyol other than a Mannish polyol, and a physical blow-ing agent. The Mannish polyol has a viscosity of at least 4,000 centipoise at 25 °C. The physical blowing agent is selected from the group of volatile non-halogenated Cz to C~
hydrocarbons, hydrofluorocarbons, hydrochlorocarbons, and mixtures thereof.
The physical blowing agent is present in an amount of greater than 10 parts by weight based on 100 parts by weight of the resin composition.

[0005] The subject invention further provides a method of forming the polyurethane foam using the froth spraying system. The froth spraying system generally includes supply vessels, a spray machine, and a dispensing gun having a mixing chamber.
The method provides the resin composition and a polyisocyanate and mixes the resin com-position with the polyisocyanate in the mixing chamber to form a mixture. The mixture is discharged from the dispensing gun as the resin composition reacts with the polyiso-cyanate to form the polyurethane foam.

[0006] The subject invention provides a spray froth systsm that allows for improved delivery of a resin composition and a polyisocyanate. The spray froth system allows the resin composition to have increased amounts of physical blowing agents that have not been previously utilized advantageously. The polyurethane foam produced with such a system achieves the desired physical properties and characteristics.
DETAILED DESCRIPTION OF THE INVENTION

[0007] A froth spraying system mixes a resin composition and a polyisocyanate to form a mixture and the mixture is dispensed from a dispensing gun to form a polyure-thane foam. A first stream carries the resin composition from a storage tank or a pres-surized vessel to the dispensing gun. A second stream, separate from the first stream, carries the polyisocyanate from a storage tank or a pressurized vessel to the dispens-ing gun. The two streams are mixed together in a mixing chamber of the dispensing gun and begin to react. As the mixture continues to react, it is dispensed from the dis-pensing gun onto or in the direction of a substrate. In one embodiment, the substrate may include a wall having cavities therein for receiving the mixture. Other embodiments of the substrate may include pipes or any other equipment that requires insulation.
Typically, upon completing the reaction, the polyurethane foam acts as an insulation for the substrate.

[0008] The resin composition includes a physical blowing agent that causes the mixture to froth as the mixture exits the dispensing gun. However, those skilled in the art recognize that the mixture may not necessarily froth as it is dispensed from the dis-pensing gun. Those skilled in the art recognize that the physical blowing agent suffi-ciently and spontaneously vaporizes when the two combined streams are exposed to atmospheric pressure upon discharge. The vaporization of the physical blowing agent produces the froth. It is to be understood that not all of the physical blowing agent needs to vaporize instantaneously when discharged, but at least an amount sufficient to produce the froth should vaporize upon discharge from the dispensing gun.

[0009] The resin composition, in addition to the physical blowing agent, includes a Mannich polyol and at least one additional polyol other than the Mannich polyol. The resin composition may also include a catalyst system, surfactants, flame retardants, fillers, stabilizers, fungicides, pigments or dyes and bacteriostats. The resin composi-tion is substantially free of chemical blowing agents. Chemical blowing agents include any blowing agents that chemically react with the resin composition or the polyisocy-anate, such as, but not limited to, water. It is to be understood that, in the context of the subject invention, substantially free of chemical blowing agents is intended to indicate that the resin composition has less than 5 parts by weight, preferably less than 2.5 parts by weight, and most preferably less than 1.5 parts by weight, based on 100 parts by weight of the resin composition.

[0010] The Mannich polyol is made by alkoxylating a Mannich compound, which is the condensation product of phenol or a substituted phenol, formaldehyde, and an al-kanoamine, such as diethanol amine. For example, the Mannich reaction is conducted by premixing the phenolic compound with a desired amount of the ethanolamine and then slowly adding formaldehyde to the mixture at a temperature below the tempera-ture of Novolak formation. At the end of the reaction, water is stripped from the reaction mixture to provide a crude Mannich reaction product.

[0011] The Mannich reaction product is then alkoxylated with an alkylene oxide such as, for example, propylene oxide, ethylene oxide, or a mixture of propylene oxide and ethylene oxide. The alkylene oxide may suitably comprise from about 80 to parts by weight propylene oxide and from 0 to about 20 parts by weight ethylene oxide based on 100 parts by weight of the alkylene oxide. Alkoxylation of Mannich reaction products is described in United States Patent Nos. 3,297,597 and 4,137,265, the dis-closures of which are incorporated herein by reference.

[0012] The alkoxylation with propylene oxide is carried out by introducing the pro-pylene oxide, preferably under pressure, into a vessel containing the Mannich reaction product. No added catalyst is needed since the basic nitrogen in this product provides sufficient catalytic activity to promote the reaction. Reaction temperatures between about 30° C. and about 200° C. may be employed, but the preferred reaction tempera-tures are in the range of from about 90° to 120° C. Under these conditions, the phenolic hydroxyl group and the alkanolamino hydroxyls are reactive to form hydroxypropyl groups. Unreacted and partially reacted materials are removed from the final conden-sation product in any suitable manner (e.g., by vacuum stripping) to provide clear am-ber to brown liquids having hydroxyl numbers in the range of 400 to 550 and viscosities between about 4,000 and 45,000 centipoises at 25° C. The Mannich polyol preferably having a viscosity of at least 4,000 centipoise at 25 °C.

[0013) In a preferred embodiment of the present invention, the Mannich polyol is present in the resin composition in an amount of from 20 to 40 parts by weight based on 100 parts by weight of the resin composition. Preferably, the resin composition has a hydroxyl content of at least 400 mg KOH/g. Additionally, the Mannich polyol prefera-bly comprises an aromatic, amine polyol having a hydroxyl content of at least 400 mg KOH/g. The aromatic, amine polyol preferably has an amino content of at least 2.8 meq/g.

[0014) The resin composition also includes at least one additional polyol compound having at least two isocyanate-reactive hydrogens. The compounds having at least two isocyanate-reactive hydrogens preferably have an average hydroxyl number ranging from 150 to 800 mg KOH/g of compound.

[0015) Examples of these polyols include polythioether polyols, polyester amides and polyacetals containing hydroxyl groups, aliphatic polycarbonates containing hy-droxyl groups, amine-terminated polyoxyalkylene polyethers, polyester polyols, and polyoxyalkylene polyether polyols. In addition, mixtures of at least two of the aforesaid polyols can be used.

[0016] The term "polyester polyol° as used in this specification and claims includes any minor amounts of unreacted polyol remaining after the preparation of the polyester polyol andlor unesterified polyol (e.g., glycol) added after the preparation of the polyes-ter polyol. The polyester polyol can include up to about 40 weight percent free glycol.

[0017) Suitable polyester polyols can be produced, for example, from organic di-carboxylic acids with 2 to 12 carbons, preferably aliphatic dicarboxylic acids with 4 to 6 carbons, and multivalent alcohols, preferably diols, with 2 to 12 carbons, preferably 2 to 6 carbons. Examples of dicarboxylic acids include succinic acid, glutaric acid, adipic acid, suberic acid, azelaic acid, sebacic acid, decanedicarboxylic acid, malefic acid, fumaric acid, phthalic acid, isophthalic acid and terephthalic acid. The dicarboxylic ac-ids can be used individually or in mixtures. Instead of the free dicarboxylic acids, the corresponding dicarboxylic acid derivatives may also be used such as dicarboxylic acid mono- or di- esters of alcohols with 1 to 4 carbons, or dicarboxylic acid anhydrides.
Dicarboxylic acid mixtures of succinic acid, glutaric acid and adipic acid in quantity ra-tios of 20-35:35-50:20-32 parts by weight are preferred, especially adipic acid. Exam-ples of divalent and multivalent alcohols, especially diols, include ethanediol, diethylene glycol, 1,2- and 1,3-propanediol, dipropylene glycol, 1,4-butanediol, 1,5-pentanediol, 1,6-hexanediol, 1,10-decanediol, glycerine and trimethylolpropanes, tripropylene glycol, tetraethylene glycol, tetrapropylene glycol, tetramethylene glycol, 1,4-cyclohexane-dimethanof, or mixtures of at least two of these diols are preferred, especially mixtures of 1,4-butanediol, 1,5-pentanediol and 1,6-hexanediol. Furthermore, polyester polyols of lactones, e.g., e-caprolactone or hydroxycarboxylic acids, e.g., w-hydroxycaproic acid, may also be used.

[0018] The polyester polyols can be produced by polycondensation of organic po-lycarboxylic acids, e.g., aromatic or preferably aliphatic polycarboxylic acids and/or 5 derivatives thereof and multivalent alcohols in the absence of catalysts or preferably in an atmosphere of an inert gas, e.g., nitrogen, carbon dioxide, helium, argon, etc., in the melt at temperatures of 150° to 250° C, preferably 180°
to 220° C, optionally under reduced pressure, up to the desired acid value which is preferably less than 10, espe-cially less than 2. In a preferred embodiment, the esterification mixture is subjected to polycondensation at the temperatures mentioned above up to an acid value of 30 to 80, preferably 30 to 40, under normal pressure, and then under a pressure of less than 500 mbar, preferably 50 to 150 mbar. The reaction can be carried out as a batch process or as a continuous process. When present, excess glycol can be distilled from the reac-tion mixture during andlor after the reaction, such as in the preparation of low free gly-col-containing polyester polyols usable in the present invention. Examples of suitable esterification catalysts include iron, cadmium, cobalt, lead, zinc, antimony, magnesium, titanium and tin catalysts in the form of metals, metal oxides or metal salts.
However, the polycondensation may also be preformed in liquid phase in the presence of diluents and/or chlorobenzene for aziotropic distillation of the water of condensation.

[0019] To produce the polyester polyols, the organic polycarboxylic acids and/or derivatives thereof and multi-valent alcohols are preferably polycondensed in a mole ratio of 1:1-1.8, more preferably 1:1.05-1.2.

[0020] After transesterification or esterification, the reaction product can be reacted with an alkylene oxide to form a polyester polyol mixture. This reaction desirably is catalyzed. The temperature of this process should be from about 80° to 170°C, and the pressure should generally range from about 1 to 40 atmospheres.

[0021] While the aromatic polyester polyols can be prepared from substantially pure reactant materials, more complex ingredients can be used, such as the side stream, waste or scrap residues from the manufacture of phthalic acid, terephthalic acid, dimethyl terephthalate, polyethylene terephthalate, and the Pike.
Compositions containing phthalic acid residues for use in the invention are (a) ester-containing by-products from the manufacture of dimethyl terephthalate, (b) scrap polyalkylene te-rephthalates, (c) phthalic anhydride, (d) residues from the manufacture of phthalic acid or phthalic anhydride, (e) terephthalic acid, (f) residues from the manufacture of te-rephthalic acid, (g) isophthalic acid, (h) trimellitic anhydride, and (i) combinations there-of. These compositions may be converted by reaction with the polyols of the invention to polyester polyols through conventional transesterification or esterification proce-dures.

[0022] Other materials containing phthalic acid residues are polyalkylene te-rephthalates, especially polyethylene terephthalate (PET), residues or scraps.
Still other residues are dimethyl terephthalate (DMT) process residues, which are waste or scrap residues from the manufacture of DMT. The term °DMT process residue" refers to the purged residue which is obtained during the manufacture of DMT in which p-xylene is converted through oxidation and esterification with methanol to the desired product in a reaction mixture along with a complex mixture of byproducts. The desired DMT and the volatile methyl p-toluate byproduct are removed from the reaction mixture by distillation leaving a residue. The DMT and methyl p-toluate are separated, the DMT
is recovered and methyl p-toluate is recycled for oxidation. The residue which remains can be directly purged from the process or a portion of the residue can be recycled for oxidation and the remainder diverted from the process or, if desired, the residue can be processed further as, for example, by distillation, heat treatment and/or methanolysis to recover useful constituents which might otherwise be lost, prior to purging the residue from the system. The residue which is finally purged from the process, either with or without additional processing, is herein called DMT process residue.

[0023] Polyoxyalkylene polyether polyols, which can be obtained by known meth-ods, are preferred for use as the additional polyhydroxyl compounds. For example, polyether polyols can be produced by anionic polymerization with alkali hydroxides such as sodium hydroxide or potassium hydroxide or alkali alcoholates, such as so-dium methylate, sodium ethylate, or potassium ethylate or potassium isopropylate as catalysts and with the addition of at least one initiator molecule containing 2 to 8, pref erably 3 to 8, reactive hydrogens or by cationic polymerization with Lewis acids such as antimony pentachloride, boron trifluoride etherate, etc., or bleaching earth as catalysts from one or more alkylene oxides with 2 to 4 carbons in the alkylene radical.
Any suit-able alkylene oxide may be used such as 1,3-propylene oxide, 1,2-and 2,3-butylene oxide, amylene oxides, styrene oxide, and preferably ethylene oxide and 1,2-propylene oxide and mixtures of these oxides. The polyalkylene polyether polyols may be pre-pared from other starting materials such as tetrahydrofuran and alkylene oxide-tetrahydrofuran mixtures; epihalohydrins such as epichlorohydrin; as well as aralkylene oxides such as styrene oxide. The polyalkylene polyether polyols may have either pri-mary or secondary hydroxyl groups.

[0024] Included among the polyether polyols are polyoxyethylene glycol, poly-oxypropylene glycol, polyoxybutylene glycol, polytetramethylene glycol, block copoly-mers, for example, combinations of polyoxypropylene and polyoxyethylene glycols, poly- 1,2-oxybutylene and polyoxyethylene glycols, poly-1,4-tetramethylene and poly-oxyethylene glycols, and copolymer glycols prepared from blends or sequential addi-tion of two or more alkylene oxides. The polyalkylene polyether polyols may be pre-pared by any known process such as, for example, the process disclosed by Wurtz in 1859 and Encyclopedia of Chemical Technology, Vol. 7, pp. 257-262, published by Interscience Publishers, Inc. (1951) or in United States Patent No. 1,922,459.

[0025] Polyethers which are preferred include the alkylene oxide addition products of polyhydric alcohols such as ethylene glycol, propylene glycol, dipropylene glycol, trimethylene glycol, 1,2-butanediol, 1,5-pentanediol, 1,6-hexanediol, 1,7-heptanediol, hydroquinone, resourcinol glycerol, glycerine, 1,1,1-trimethylol-propane, 1,1,1-trimethylolethane, pentaerythritol, 1,2,6-hexanetriol, a-methyl glucoside, sucrose, and sorbitol. Also included within the term °polyhydric alcohol" are compounds derived from phenol such as 2,2-bis(4-hydroxyphenyl)-propane, commonly known as Bisphenol A.

[0026] One preferred additional polyether polyol of the present invention is Vora-nol~ 370, a sucrose based polyether polyol having a hydroxyl number of approximately 370 and commercially produced by the Dow Chemical Company. Other preferred addi-tional polyether polyols are Pluracol~ PEP 450 and 550 polyether tetrols having hy-~droxyl numbers of approximately 560 and 450, respectively and commercially produced by BASF Corporation, and Pluracol~ GP 730 that is a polyether triol having a hydroxyl number of approximately 270 and commercially available from BASF Corporation.

[0027] Suitable organic amine initiators which may be condensed with alkylene oxides include aromatic amines such as aniline, N-alkylphenylenediamines, 2,4'-, 2,2', and 4,4'-methylenedianiline, 2,6- or 2,4-toluenediamine, vicinal toluenediamines, o-chloro-aniline, paminoaniline, 1,5-diaminonaphthalene, methylene dianiline, the various condensation products of aniline and formaldehyde, and the isomeric diaminotoluenes;
and aliphatic amines such as mono-, di-, and trialkanolamines, ethylene diamine, pro-pylene diamine, diethylenetriamine, methylamine, ethanolamine, diethanolamine, N-methyl- and N-ethylethanolamine, N-methyl- and N-ethyldiethanolamine, triethanola-mine, triisopropanolamine, 1,3-diaminopropane, 1,3-diaminobutane, and 1,4-diaminobutane. Preferable amines include polyoxypropylenediamine, such as Jeffam-ine~ D-230 commercially produced by Huntsman Corporation.

[0028] It is to be understood that the polyols initiated by an amine can also be initi-ated with a polyhydric alcohol, such as when a mixed initiator of an aliphatic ami-ne/polyhydric alcohol is used like an amine/sucrose package.

[0029] Suitable polyhydric polythioethers which may be condensed with alkylene oxides include the condensation product of thiodiglycol or the reaction product ~f a di-carboxylic acid such as is disclosed above for the preparation of the hydroxyl-containing polyesters with any other suitable thioether glycol.

[0030] The hydroxyl-containing polyester may also be a polyester amide such as is obtained by including some polyester amide such as is obtained by including some amine or amino alcohol in the reactants for the preparation of the polyesters.
Thus, polyester amides may be obtained by condensing an amino alcohol such as ethanola-mine with the polycarboxylic acids set forth above or they may be made using the sa-me components that make up the hydroxyl-containing polyester with only a portion of the components being a diamine such as ethylene diamine. Suitable polyacetals which may be condensed with alkylene oxides include the reaction product of formaldehyde or other suitable aldehyde with a dihydric alcohol or an alkylene oxide such as those disclosed above.

[0031] Suitable aliphatic thiols which may be condensed with alkylene oxides in-clude alkanethiols containing at least two --SH groups such as 1,2-ethanedithiol, 1,2-propanedithiol, 1,2-propanedithiol, and 1,6-hexanedithiol; alkene thiols such as 2-butene-1,4-dithiol; and alkyne thiols such as 3-hexyne- 1,6-dithiol.

[0032] In one preferred embodiment of the subject invention, the at feast one addi-- tional polyol is selected from the group of sucrose-initiated polyether polyols, polyether tetrols, polyether triols, and mixtures thereof. The at least one additional polyol is pre-sent in an amount of from greater than 0 to 35 parts by weight based on 100 parts by weight of the resin composition.

[0033] As discussed above, physical blowing agents are those which boil as the mixture reacts exothermically and forms the polyurethane foam, preferably at 50° C, or less. The most preferred physical blowing agents are those which have a zero ozone depletion potential. Examples of physical blowing agents are the volatile non-hafogenated hydrocarbons having two to seven carbon atoms such as alkanes, al-kenes, cycloalkanes having up to 6 carbon atoms, dialkyl ether, cycloalkylene ethers and ketones; and hydrofluorocarbons (HFCs).

[0034] Examples of volatile non-halogenated hydrocarbons include linear or bran-ched alkanes, e.g. butane, isobutane, 2,3-dimethylbutane,n- and isopentane and tech-nical-grade pentane mixtures, n- and isohexanes, n- and isoheptanes, n- and isooc-tanes, n- and isononanes, n- and isodecanes, n- and isoundecanes, and n- and isodedecanes. Since very good results are achieved with respect to the stability of emulsions, the processing properties of the reaction mixture and the mechanical prop-erties of polyurethane foam products produced when n-pentane, isopentane or n-hexane, or a mixture thereof is used, these alkanes are preferably employed.
Further-more, specific examples of alkenes are 1-pentene, 2-methylbutene, 3-methylbutene, and 1-hexene; of cycloalkanes are cyclobutane, preferably cyclopentane, cyclohexane or mixtures thereof; specific examples of linear or cyclic ethers are dimethyl ether, di-ethyl ether, methyl ethyl ether, vinyl methyl ether, vinyl ethyl ether, divinyl ether, tetra-hydrofuran and furan; and specifiic examples of ketones are acetone, methyl ethyl ke-tone and cyclopentanone. Preferentially, cyclopentane, n- and isopentane, n-hexane, and mixtures thereof are employed.

[0035] Suitable hydrofluorocarbons include difluoromethane (HFC-32); 1,1,1,2-tetrafluoroethane (HFC-134a); 1,1,2,2-tetrafluoroethane (HFC-134); 1,1-difluoroethane (HFC-152a); 1,2-difluoroethane (HFC-142), trifluoromethane; heptafluoropropane (R-227a); hexafluoropropane (R-136); 1,1,1-trifluoroethane; 1,1,2-trifluoroethane; fluoro-ethane (R-161); 1,1,1,2,2-pentafluoropropane; pentafluoropropylene (R-2125a);
1,1,1,3-tetrafluoropropane; tetrafluoropropylene (R-2134a); difluoropropylene (R-2152b); 1,1,2,3,3-pentafluoropropane; 1,1,1,3,3-pentafluoro-n-butane; and 1,1,1,3,3-pentafluoropentane (245fa).

[0036] In one preferred embodiment, the physical blowing agent is selected from the group of cyclopentane, isopentane, n-pentane, trans-1,2-dichloroethylene, and mix-tures thereof. The physical blowing is present in an amount of greater than 10 parts by weight, preferably greater than 10 to 40 parts by weight, and more preferably greater than 10 to 30 parts by weight, based on 100 parts by weight of the resin composition.

[0037] In a most preferred embodiment, the physical blowing agent is cyclopen tane. Cyclopentane has a boiling point of 322 K. (49°C at 760 mm/Hg) and readily va porizes to froth the mixture as it exits the dispensing gun. The mixture may not froth as it exits the dispensing gun depending on processing temperatures of the mixture. The cyclopentane may be added to the resin composition at the dispensing gun as a sepa-rate stream; blended into the resin composition supply vessel immediately prior to dis-pensing; or it may be pre-blended into the resin composition, stored, and shipped in the pressurized vessel to a manufacturer of the polyurethane foams of the present inven-tion. To make the resin composition by any of these methods, cyclopentane is metered into the resin composition, and, optionally, but preferably, blended until a homogenous solution is formed. In one embodiment the vessel containing the resin composition is pressurized at 150-300 psig, and depending on the type of dispensing method em-ployed as discussed further below, may also be pre-combined with an inert gas such as nitrogen.

[0038] The amount of cyclopentane employed will depend upon the desired density of the polyurethane foam and the limits of its solubility in a particular resin composition.
However, the related art compositions were limited by the physical blowing agent be-cause the resin composition saturates at a relatively small amount. For example, when the physical blowing agent is R-134a, the resin composition saturates at about 10 parts by weight based on 100 parts by weight of the resin composition. Therefore, in order to ensure that the polyurethane foam has the desired density, additional physical blowing agents or chemical blowing agents had to be used. The subject invention uses the physical blowing agent in an amount greater than 10 parts by weight based on parts by weight of the resin composition, which eliminates the need for additional phy-sical blowing agents or chemical blowing agents. This is particularly advantageous since the chemical blowing agents react with the polyisocyanate and generally requires more polyisocyanate to form the polyurethane foam. Since the subject invention is sub-stantially free of chemical blowing agents, less polyisocyanate is consumed and the 5 cost of producing the polyurethane foam is also reduced.

[0039] The resin composition may also include a catalyst system. The catalyst sys-tem is selected from at least one of a curing catalyst, a blow catalyst, and a gelation catalyst. The catalyst system may be employed to greatly accelerate the reaction of the 10 compounds containing isocyanate-reactive hydroxyl groups with the modified or un-modified polyisocyanates. Curing catalysts also function to shorten tack time, promote green strength and prevent foam shrinkage. Suitable curing catalysts are organometal-lic catalysts, preferably organo-lead catalysts, although it is possible to employ metals such as tin, titanium, copper, mercury, cobalt, nickel, iron, vanadium, antimony, bis-muth, lithium, and manganese. Preferred curing catalysts include lead octoate and lead napthanate. The curing catalyst is preferably present in an amount of from 0.01 to 0.9 parts by weight based on 100 parts by weight of the resin composition.

[0040] Blow catalysts include tertiary amines and promote urethane linkage forma-tion. Examples of blow catalysts are polyoxypropylenediamines which include triethyl-amine,3-methoxypropyldimethylamine, triethylenediamine, tributylamine, dimethylcy-clohexylamine, dimethylbenzylamine, N-methyl-, N-ethyl- and N-cyclohexylmorpholine, N,N,N',N'-tetramethylethylenediamine, N,N,N',N'-tetramethylbutanediamine or-hexanediamine, N,N,N'-trimethyl isopropyl propylenediamine, pentamethyldiethyl-enetriamine, tetramethyldiaminoethylether, bis(-dimethylaminopropyl)urea, dimeth-ylpiperazine, 1-methyl-4-dimethylaminoethylpiperazine, 1,2-dimethylimidazole, azabicylo[3.3.0]octane and preferably 1,4-diazabicylo[2.2.2]octane, and alkanolamine compounds, such as triethanolamine, triisopropanolamine, N-methyl- and N-ethyldiethanolamine and dimethylethanolamine.

[0041] Another type of blow catalysts is tertiary amine ether catalysts.
Typical terti-ary amine ether blow catalysts include, but are not limited to, N,N,N,N"-tetramethyl-2,2'-diaminodiethyl ether; 2-dimenthyaminoethyl-1,3-dimenthylamineo-propyl ether;
and N,N-dimorpholinoethyl ether. Most preferred is pentamethyldiethylenetriamine. The blow catalyst is preferably present in an amount of from 0.01 to 3 parts by weight based on 100 parts by weight of the resin composition.

[0042] The blow catalyst can be used in its pure form or dissolved in a carrier such as a glycol. When the catalyst system is dissolved in a carrier, the amounts stated herein as parts by weight refers to the amount of catalyst system and does not include the weight of the carrier.

[0043] Preferably, the catalyst system of the present invention includes at least one cure catalyst and at least one blow catalyst described above. More preferably, the cata-lyst system also includes the gelation catalyst, such as triethylenediamine in a dipro-pylene glycol carrier, which is commercially produced under the trade name Dabco~
LV-33 by the Air Products Corporation. The gelation catalyst is preferably present in an amount of from 0.01 to 3 parts by weight based on 100 parts by weight of the resin composition.

[0044] The resin composition may also include a flame retardant. The flame retar-dant is preferably present in an amount of from 5 to 25 parts by weight based on 100 parts by weight of the resin composition. Examples of suitable flame retardants are tricresyl phosphate, tris(2-chloroethyl) phosphate, tris(2-chloropropyl) phosphate, and tris(2,3-dibromopropyl) phosphate. Yet another suitable flame retardant is PHT
4 Diol, Tetrabromophthalic Acid, commercially available from Great Lakes Chemical Com-pany. In addition to these halogen-substituted phosphates, it is also possible to use inorganic or organic flame retardants, such as red phosphorous, aluminum oxide hy-drate, antimony trioxide, arsenic oxide, ammonium polyphosphate (Exolit~) and calcium sulfate, molybdenum trioxide, ammonium molybdate, ammonium phosphate, pentab-romodiphenyloxide, 2,3-dibromopropanol, hexabromocyclododecane, dibromoethyldi-bromocyclohexane, expandable graphite or cyanuric acid derivatives, e.g., melamine, or mixtures of two or more flame retarding agents, e.g., ammonium polyphosphates and melamine, and, if desired, corn starch, or ammonium polyphosphate, melamine, and expandable graphite and/or, if desired, aromatic polyesters, in order to flame retard the polyisocyanate polyaddition products.

[0045] A surfactant may also be included in the resin composition and the surfac-tant is preferably present in an amount of from 0.01 to 5.0 parts by weight based on 100 parts by weight of the resin composition. Examples of suitable surfactants that may be used are compounds which serve to support homogenization of the starting materi-als and may also regulate the cell structure of the polyurethane foam.
Specific exam-ples are salts of sulfonic acids, e.g., alkali metal salts or ammonium salts of fatty acids such as oleic or stearic acid, of dodecylbenzene- or dinaphthylmethanedisulfonic acid, and ricinoleic acid; foam stabilizers, such as siloxaneoxyalkylene copolymers and other organopoiysiloxanes, oxyethylated alkyl-phenols, oxyethylated fatty alcohols, pariffin oils, castor oil esters, ricinoleic acid esters, Turkey red oil and groundnut oil, and cell regulators, such as paraffins, fatty alcohols, and dimethylpolysiloxanes. A
particularly preferred non-silicone surfactant is LK-443 commercially produced by Air Products Corporation.

[0046] The polyisocyanate that may be used in the present invention includes all essentially known aliphatic, cycloaliphatic, araliphatic and preferably aromatic multiva-lent isocyanates. Specific examples include: alkylene diisocyanates with 4 to 12 car-bons in the alkylene radical such as 1,12-dodecane diisocyanate, 2-ethyl-1,4-tetramethylene diisocyanate, 2-methyl-1,5-pentamethylene diisocyanate, 1,4-tetramethylene diisocyanate and preferably 1,6-hexamethylene diisocyanate;
cycloa-liphatic diisocyanates such as 1,3- and 1,4-cyclohexane diisocyanate as well as any mixtures of these isomers, 1-isocyanato-3,3,5-trimethyl-5-isocyanatomethylcyclo-hexane (isophorone diisocyanate), 2,4- and 2,6-hexahydrotoluene diisocyanate as well as the corresponding isomeric mixtures 4,4', 2,2'- and 2,4'-dicyclohexylmethane diiso-cyanate as well as the corresponding isomeric mixtures and preferably aromatic diiso-cyanates and polyisocyanates such as 2,4- and 2,6-toluene diisocyanate and the cor-responding isomeric mixtures 4,4'-, 2,4'- and 2,2'-diphenylmethane diisocyanate and the corresponding isomeric mixtures, mixtures of 4,4'- and 2,4'-diphenylmethane diiso-cyanates and polyphenylenepolymethylene polyisocyanates (polymeric MDI), as well as mixtures of polymeric MDI and toluene diisocyanates.

[0047] Frequently, the polyisocyanate may include so-called modified multivalent isocyanates, i.e., products obtained by the partial chemical reaction of organic diisocy-anates and/or polyisocyanates are used. Examples include diisocyanates and/or poly-isocyanates containing ester groups, urea groups, biuret groups, allophanate groups, carbodiimide groups, isocyanurate groups, andlor urethane groups. Specific examples include organic, preferably aromatic, polyisocyanates containing urethane groups and having an NCO content of 15 to 33.6 parts by weight, preferably 21 to 32 parts by weight, based on 100 parts by weight, e.g., with low molecular weight diols, triols, dial-kylene glycols, trialkylene glycols, or polyoxyalkylene glycols with a molecular weight of up to 1500; modified 4,4'-diphenylmethane diisocyanate or 2,4- and 2,6-toluene diiso-cyanate, where examples of di- and polyoxyalkylene glycols that may be used individu-ally or as mixtures include diethylene glycol, dipropylene glycol, polyoxyethylene glycol, polyoxypropylene glycol, polyoxyethylene glycol, polyoxypropylene glycol, and poly-oxypropylene polyoxyethylene glycols or -triols. Prepolymers containing NCO
groups with an NCO content of 9 to 25 parts by weight, preferably 14 to 21 parts by weight, based on 100 parts by weight and produced from the polyester polyols and/or prefera-bly polyether polyols described below; 4,4'-diphenylmethane diisocyanate, mixtures of 2,4'- and 4,4'-diphenylmethane diisocyanate, 2,4,-and/or 2,6-toluene diisocyanates or polymeric MDI are also suitable. Furthermore, liquid polyisocyanates containing car-bodiimide groups having an NCO content of 15 to 33.6 parts by weight, preferably 21 to 32 parts by weight, based on 100 parts by weight, have also proven suitable, e.g., based on 4,4'- and 2,4'- and/or 2,2'-diphenylmethane diisocyanate and/or 2,4'-and/or 2,6-toluene diisocyanate. The modified polyisocyanates may optionally be mixed to-gether or mixed with unmodified organic polyisocyanates such as 2,4'- and 4,4'-diphenylmethane diisocyanate, polymeric MDI, 2,4'- and/or 2,6-toluene diisocyanate.

[0048] Organic polyisocyanates which may be employed include aromatic, ali-phatic, and cycloaliphatic polyisocyanates and combinations thereof.
Representative of these types are the diisocyanates such as m-phenylene diisocyanate, 2,4-toluene dii-socyanate, 2,6-toluene diisocyanate, mixtures of 2,4- and 2,6-toluene diisocyanate, hexamethylene diisocyanate, tetramethylene diisocyanate, cyclohexane-1,4-diisocyanate, hexahydrotoluene diisocyanate (and isomers), naphthalene-1,5-diisocyanate, 1-methoxyphenyl-2,4-diisocyanate, 4,4'-diphenylmethane diisocyanate, mixtures of 4,4'- and 2,4'-diphenylmethane diisocyanate, 4,4'-biphenylene diisocy-anate, 3,3'-dimethoxy-4,4'-biphenyl diisocyanate, 3,3'-dimethyl-4,4'-biphenyl diisocy-anate and 3,3'-dimethyldiphenylmethant-4,4'-diisocyanate; the triisocyanates such as 4,4',4"-triphenylmethane triisocyanate, and toluene 2,4,6-trisocyanate; and the tetraiso-cyanates such as 4,4'- dimethldiphenylmethane-2,2',5,5'-tetraisocyanate and polymeric polyisocyanates such as polymethylene polyphenylene polyisocyanate, and mixtures thereof. Especially useful due to their availability and properties are 4,4'-diphenyl-methane diisocyanate, polymethylene polyphenylene polyisocyanate, or mixtures thereof for rigid foams, or a mixture of the foregoing with toluene diisocyanates for semi-rigid foams.

[0049] Crude polyisocyanates may also be used in the compositions of the present invention, such as crude toluene diisocyanate obtained by the phosgenation of a mix-ture of toluenediamines or crude diphenylmethane isocyanate obtained by the phos-genation of crude isocyanates as disclosed in United States Patent No.
3,215,652.

[0050] In a preferred embodiment, the froth spraying system includes a resin sup-ply vessel, a polyisocyanate supply vessel, a spray machine, and a dispensing gun having a mixing chamber. Each of the supply vessels may be pressured as understood by those skilled in the art. The resin composition is provided in a stream from the resin supply vessel to the spray machine and from the spray machine to the dispensing gun.
The resin composition is provided separate from the isocyanate, such that the isocy-anate is also provided in a stream from the polyisocyanate supply vessel to the spray machine and from the spray machine to the dispensing gun.

[0051] The spraying system according to the subject invention monitors flammable gas levels to detect leaks in the stream of the resin composition. In order to monitor these gas levels, the supply vessel for the resin composition is located in a storage room, which also contains the spray machine and the hoses, and is isolated from an area to be sprayed. This area would be classified for Class 1, Zone 2, Group D. The storage room also typically includes the spray machine. The spray machine is prefera-bly a fixed proportioner machine with two positive displacement pumps, one for the isocyanate and the other for the resin. The spray machine heats the two liquid compo-nents up to the desired temperature (typically between 26-66°C), pressurizes the com-ponents (typically between 4000-20,400 kPa), then delivers them through separate hoses to the spray gun with the mixing head. A spray operator sprays the foam onto the desired substrate, such as a concrete wall, OSB, etc. Typical manufacturers of spray machines are Gusmer Inc, Graco Inc, and Glas-Craft.

[0052] The storage room is also isolated from an operation chamber. The operation chamber houses electrical components that operate the spraying system, such as a generator, a compressor, and/or an electrical panel. It is important that the operation chamber be sealed from the storage room incase of a leak in the system of flammable gas because any sparks generated in the electrical components may ignite an explo-sion.

[0053] In operation, a truck would have each of these areas located in a truck box.
Since these areas are separated, the entire truck box does not need to be explosion proof, only the area storing the supply vessels needs to be explosion proof.
The cost to produce the polyurethane foam is significantly reduced if only a portion of the truck bed needs to be explosion proof because this reduces the cost of the equipment required to spray the materials.

[0054] The subject invention monitors the flammable gas level by positioning sen-sors in the storage room near the spray machine and the supply vessels. When the flammable gas levels are detected above a predetermined threshold, then the froth spraying system is deactivated. Preferably, the froth spraying system is deactivated when the level of flammable gas reaches 20°!°. Additionally, an alarm may be activated to alert the user of increased flammable gas levels when it reaches 10%.
Additionally, a sensor on the user monitors the flammable gas levels at the area where the polyure-thane foam is being sprayed to alert the user of flammable gas levels in the spray area.

[0055] If the flammable gas levels are detected in the storage room, after deactivat-ing the froth spraying system, the storage room is vented to reduce the flammable gas levels therein. At least one fan is located within the storage room to draw out the flam-mable gas. The froth spraying system is re-activated in response to the flammable gas levels dropping below the predetermined threshold. Likewise, if the flammable gas lev-els at the area to be sprayed are above the predetermined threshold, the operator is notified. . The area to be sprayed, if properly ventilated, may include enclosed areas such as, but not limited to, crawl spaces and the like.

[0056] The spray froth system also includes at least one reactant supply tank for imposing gas pressure to drive the reactants from the supply vessels and a fixed ratio positive displacement pump, specifically designed for the spray application of polyure-thane foams. Any means for imposing pressure to drive the reactants from the supply vessels may be used. Typically, a pressurized gaseous inert propellant, such as a ni-trogen tank, is used having valued outlets communicating via suitable conduits with the inlets to the supply vessels. The supply vessels are kept under pressure to provide the driving force needed to propel the reactants from the supply vessels. The pressure in the pressurized supply vessels is generally 150-300 psig. However, pressure may be as low as 50 psig without using an additional pump. If an additional pump is used to withdraw the component from the vessel, then pressure may be as low as 0.5 psig to act as a positive pressure and to prevent a vacuum from occurring in the vessel.

[0057] It is generally necessary, for the proper functioning of the spray froth sys-tem, that the viscosity of the contents of each of the supply vessels be no greater than about 1200 cps at 25°C. And more preferably no more than about 800 cps.
This, of course, means that the materials in each tank may have to be properly selected or for-10 mulcted, as the case may be, in order to meet this viscosity requirement.
The viscosity values mentioned herein are measured at 25°C and at 80psig (544 psi).

[0058] By using the fixed ratio, positive displacement pump, specifically designed for the spray application of polyurethane foams, the volume ratio of the isocyanate 15 stream and the resin composition stream can be held at 1:1.
Examples [0059] The following examples are intended to illustrate, but in no way limit, the scope of the present invention. The spray froth system used in this example comprised:
(a) a first supply vessel for supplying the isocyanate reactant, (b) a second supply ves-sel for supplying the resin composition, (c) a nitrogen pressure tank having a valued outlet in communication, via a distributing valve, with inlets to the two supply vessels, and (d) a fixed ratio positive displacement pump, (e) and LEL detector (lower explosion limit) commercially available from BW Technologies and Drager.

[0060] The components forming the resin composition are listed Table 1, below, and are in parts by weight, unless other indicated.

Components Example Example Mannich Polyol 27.82 32.72 Additional Polyol 29.02 31.00 Surfactant - 1.50 --Catalyst A 0.27 --Catalyst B 0.09 --Catalyst C -- 0.50 Catalyst D -- 0.18 Physical Blowing 20.00 15.00 Agent Chemical Blowing 0.30 0.6 Agent Flame Retardant 20.00 10.00 FR Agent -- 10.00 Cross-linker A 1.00 --Total 100.00 100.00 Table 1: Resin Composition [0061] The Mannich polyol is Mannich-based and has a functionality of about 4 and a hydroxyl number of about 470. The Mannich polyol is commercially available as Tha-nol~ R470X from Dow Chemical. The additional polyol is an ethylene diamine based polyether polyol having a hydroxyl number of about 800 and a functionality of about 4.
The additional polyol is commercially available as Jeffol~ 8290 from Huntsman Petro-chemical.

[0062] The surfactant is a non-silicone, organic surfactant commercially available as LK-221~ from Air Products and Chemicals. Catalyst A is a low-viscosity liquid amine catalyst that is blend of 20% triethylenediamine and 80% dimethylethanolamine.
Cata-lyst A is an amine based catalyst commercially available as DABCO~ R-8020 from Air Products and Chemicals. Catalyst B is lead octoate having about 24% lead.
Catalyst C
is an amine based catalyst commerically available from Toyocat as RX-5.

[0063) The physical blowing agent is cyclopentane having a boiling point of about 49°C, commercially available as EXXOLT"~ HP-95 from Exxon Mobil Chemcial. The chemical blowing agent is water. The flame retardant is tris-(chloroisopropyl) phos-phate. The cross-linker A is glycerine having a functionality of three. FR
agent acts as a fire retardant and is an aromatic polyester polyol having a functionality of about 2 and hydroxyl number of about 305 mg KOH/g commercially available from Invista as Ter-ate~ 4020.

[0064) The resin composition of Table 1 was sprayed in a 1:1 volumetric ratio with a polyisocyanate through the spray froth system described above. The polyisocyanate is polyphenylenepolymethylene polyisocyanates (polymeric MDI) commercially avail-able as Lupranate M20S from BASF Corp. The resin composition and the polyisocy-anate reacted to form the polyurethane foam.

[0065] Table 2 below lists the physical properties for a sample of the resultant po-lyurethane foam having the dimensions 1"x 4"x 4". The sample was tested in accor-dance ASTM D 1622-98 "Standard Test Method for Apparent Density of Rigid Cellular Plastics", ASTM D 1621-00 "Standard Test Method for Compressive Properties of Ri-gid Cellular Plastics" Procedure A, ASTM C 518-98 "Standard Test Method for Steady-State Thermal Transmission Properties by Means of the Heat Flow Meter Apparatus", ASTM D 2126-99 "Standard Test Method for Response of Rigid Cellular Plastics to Thermal and Humid Aging", ASTM E 96-00 "Standard Test Method for Water Vapor Transmission & Materials," Procedure A, ASTM D 6226-98 "Standard test method for Open Cell Content of Rigid Cellular Plastics" and ASTM D 2842-97 "Standard Test Method for Water Absorption of Rigid Cellular Plastics".
Property Example 1 Example 2 Density (pct] 1.83 1.97 Initial K Factor 0.02159 0.02107 (W/mk) Compressive Strength @10% 20.73 28.00 (Psi) Water Absorption 0.83 N/A
(%) Closed Cell (%) 85.17 N/A

Water Vapor Permeance 102.00 N/A

(mg/Pas m2) -1"
Core Water Vapor Permeance ~ 61.20 ~ N/A

(mg/Pas m2) -1"
Skin Table 2: Physical Properties of Polyurethane Foam [0066] The polyurethane foam sample also underwent dimensional stability analy-sis. Table 3 illustrates the results of the dimensional stability analysis listed in %volume change.

Time/Temp Example Example 24 Hours 80 C 0.55 1.10 7 Days 80 C 3.12 2.32 14 Days 80 C 3.80 3.08 28 Days 80 C 5.14 N/A

Table 3: Dimensional Stability Analysis [0067] The polyurethane foams formed according to the subject invention have a satisfactory dimensional stability. After 24 hours at 80 °C, Example 1 had 0.55% vol-ume change and Example 2 had 1.10% volume change, both measured from the origi-nal sample volume. After 7 days at 80 °C, Example 1 had 3.12% volume change and Example 2 had 2.32% volume change, both measured from the original sample vol-ume.

[0068] Obviously, many modifications and variations of the present invention are possible in light of the above teachings. The invention may be practiced otherwise than as specifically described within the scope of the appended claims.

Claims (32)

1. A resin composition for use in a froth spraying system for forming polyurethane foam, said resin composition comprising:
a Mannich polyol having a viscosity of at least 4,000 centipoise at 25 °C;
at least one additional polyol other than a Mannich polyol; and a physical blowing agent selected from the group of volatile non-halogenated to C7 hydrocarbons, hydrofluorocarbons, hydrochlorocarbons, and mixtures thereof and present in an amount of greater than 10 parts by weight based on 100 parts by weight of said resin composition.

2. A resin composition as set forth in claim 1 wherein said resin composition is sub-stantially free of chemical blowing agents.

3. A resin composition as set forth in claim 2 wherein said physical blowing agent is selected from the group of cyclopentane, isopentane, n-pentane, trans-1,2 dichloroethylene, and mixtures thereof.

4. A resin composition as set forth in claim 1 wherein said physical blowing agent is present in an amount of from greater than 10 to 40 parts by weight based on parts by weight of said resin composition.

5. A resin composition as set forth in claim 1 wherein said resin composition has a hydroxyl content of at least 400 mg KOH/g.

6. A resin composition as set forth in claim 1 further comprising a flame retardant present in an amount of from 5 to 25 parts by weight based on 100 parts by weight of said resin composition.

7. A resin composition as set forth in claim 1 wherein said Mannich polyol com-prises an aromatic, amino polyol having a hydroxyl content of at least 400 mg KOH/g.

8. A resin composition as set forth in claim 7 wherein said Mannich polyol com-prises an aromatic, amino polyol having an amino content of at least 2.8 meq/g.

9. A resin composition as set forth in claim 7 wherein said Mannich polyol is present in an amount of from 20 to 40 parts by weight based on 100 parts by weight of said resin composition.

10. A resin composition as set forth in claim 1 wherein said at least one additional polyol is selected from the group of sucrose-initiated polyether polyols, polyether tetrols, polyether triols, and mixtures thereof.

11. A resin composition as set forth in claim 1 wherein said at least one additional polyol is present in an amount of from greater than 0 to 35 parts by weight based on 100 parts by weight of said resin composition.

12. A resin composition as set forth in claim 1 further comprising a catalyst system comprising at least one of a curing catalyst, a blow catalyst, and a gelation cata-lyst.

13. A resin composition as set forth in claim 12 wherein said curing catalyst com-prises lead octoate present in an amount of from 0.01 to 0.9 parts by weight based on 100 parts by weight of said resin composition.

14. A resin composition as set forth in claim 12 wherein said blow catalyst comprises one of pentamethyldiethylenetriamine and polyoxypropylenediamine and the blow catalyst is present in an amount of from 0.01 to 3 parts by weight based on 100 parts by weight of said resin composition.

15. A resin composition as set forth in claim 12 wherein said gelation catalyst com-prises triethylenediamine in a dipropylene glycol carrier and the gelation catalyst is present in an amount of from 0.01 to 3 parts by weight based on 100 parts by weight of said resin composition.

16. A resin composition as set forth in claim 1 further comprising a surfactant present in an amount of from 0.01 to 5.0 parts by weight based on 100 parts by weight of said resin composition.

17. A method of forming a polyurethane foam using a froth spraying system including supply vessels, a spray machine, and a dispensing gun having a mixing cham-ber, said method comprising the steps of:

providing a resin composition comprising a Mannich polyol having a viscosity of at least 4,000 centipoise at 25 °C, at least one additional polyol other than a Mannich polyol, and a physical blowing agent selected from the group of volatile non-halogenated C2 to C7 hydrocarbons, hydrofluorocarbons, hydrochlorocar-bons, and mixtures thereof and used in an amount of greater than 10 parts by weight based on 100 parts by weight of the resin composition;

providing a polyisocyanate;

mixing the resin composition with the polyisocyanate in the mixing chamber to form a mixture; and discharging the mixture from the dispensing gun to form the polyurethane foam.

18. A method as set forth in claim 17 wherein the physical blowing agent is selected from the group of cyclopentane, isopentane, n-pentane, trans-1,2-dichloroethylene, and mixtures thereof.

19. A method as set forth in claim 17 wherein the physical blowing agent is used in an amount of from 10 to 40 parts by weight based on 100 parts by weight of the resin composition.

20. A method as set forth in claim 17 wherein the resin composition has a hydroxyl content of at least 400 mg KOH/g.

21. A method as set forth in claim 17 wherein the Mannich polyol is used in an amount of from 20 to 40 parts by weight based on 100 parts by weight of the resin composition.

22. A method as set forth in claim 17 wherein the at least one additional polyol is selected from the group of sucrose-initiated polyether polyols, polyether tetrols, polyether triols, and mixtures thereof.

23. A method as set forth in claim 17 wherein the at least one additional polyol is used in an amount of from greater than 0 to 30 parts by weight based on 100 parts by weight of the resin composition.

24. A method as set forth in claim 17 comprising providing the resin composition in a stream from a resin supply vessel to the spray machine and from the spray ma-chine to the dispensing gun.

25. A method as set froth in claim 24 wherein the step of providing the resin compo-sition is further defined as providing the resin composition separate from the iso-cyanate.

26. A method as set forth in claim 24 further comprising the step of monitoring flam-mable gas levels to detect leaks in the stream of the resin composition.

27. A method as set forth in claim 26 further comprising the step of deactivating the froth spraying system in response to detecting flammable gas levels above a predetermined threshold.

28. A method as set forth in claim 24 further comprising the step of storing the supply vessel for the resin composition in a storage room isolated from an area to be sprayed and isolated from an operation chamber housing electrical components.

29. A method as set forth in claim 28 further comprising the step of monitoring flam-mable gas levels within the storage room and deactivating the froth spraying sys-tem in response to detecting flammable gas levels above a predetermined threshold within the storage room.

30. A method as set forth in claim 29 further comprising the step of venting the stor-age room to reduce the flammable gas levels therein.

31. A method as set forth in claim 30 further comprising the step of reactivating the froth spraying system in response to the flammable gas levels dropping below the predetermined threshold.

32. A method as set forth in claim 28 further comprising the step of monitoring flam-mable gas levels at the area to be sprayed and alarming the operator in re-sponse to detecting flammable gas levels above a predetermined threshold at the area to be sprayed.