Polyurethane and polyisocyanurate rigid foams suitable for roofing insulation

Abstract

Polyurethane foams having a NFPA 101 Class B rating (ASTM E-84) which pass the FM 4450 Calorimeter Test are produced by reacting: (a) an organic polyisocyanate, (b) at least one polyether polyol or polyester polyol with a nominal hydroxyl functionality of at least 2.0, (c) a blowing agent composition and (d) at least one halogen-free flame retardant. The blowing agent composition includes: (1) no more than 10% by weight, based on total weight of the foam-forming composition, of one or more hydrocarbons having an LEL less than 2% by volume in air, and/or (2) a hydrocarbon having an LEL greater than 2% by volume in air, and (3) up to 1% by weight, based on total weight of foam-forming composition, of water.

Claims

1. A polyurethane foam comprising the reaction product of a polyurethane foam-forming composition consisting of: a) at least 55% by weight based on total weight of foam-forming composition of an organic polyisocyanate, b) at least one polyether polyol or polyester polyol with a nominal hydroxyl functionality of at least 2.0, c) 4.11 to 8% by weight, based on total weight of foaming-forming composition, of a pentane selected from n-pentane, isopentane, cyclopentane or a mixture thereof, d) 0.21 to 0.40% by weight, based on total weight of foam-forming composition, of water, e) triethyl phosphate or resorcinol bis(diphenyl phosphate), f) one or more catalysts, g) a polyether polysiloxane copolymer, and h) optionally one or more of a chain extender and a cross-linker, wherein the polyurethane foam has a density of less than 1.8 pounds per cubic foot, a flame spread index of 26 to 75 according to ASTM E-84, and passes an FM 4450 Calorimeter Test.

2. The polyurethane foam of claim 1, wherein the organic polyisocyanate comprises polymeric MDI and is present in an amount of 55% to 67% by weight, based on the total weight of the foam-forming composition.

3. The polyurethane foam of claim 1, wherein the foam has isocyanurate linkages.

4. An insulated roof assembly comprising: (a) a deck; (b) insulation panels mechanically attached to the deck, wherein the insulation panels comprise the polyurethane foam of claim 1.

5. The polyurethane foam of claim 1 having a flame spread index of 35 to 65 according to ASTM E-84.

6. The polyurethane foam of claim 1 wherein the one or more catalysts consist of an amine catalyst and a metal carboxylate trimer catalyst.

7. The polyurethane foam of claim 1 wherein the pentane comprises n-pentane.

8. The polyurethane foam of claim 1, wherein the pentane consists of n-pentane.

9. A polyurethane foam comprising the reaction product of a polyurethane foam-forming composition consisting of: a) at least 55% by weight based on total weight of foam-forming composition of an organic polyisocyanate, b) an isocyanate reactive composition comprising at least one polyether polyol or polyester polyol with a nominal hydroxyl functionality of at least 2.0, c) 6.47 to 8% by weight, based on total weight of foaming-forming composition, of a pentane selected from n-pentane, isopentane, cyclopentane or a mixture thereof, d) 0.15 to 0.40% by weight, based on total weight of foam-forming composition, of water, e) triethyl phosphate or resorcinol bis(diphenyl phosphate), f) one or more catalysts, g) a polyether polysiloxane copolymer, and h) optionally one or more of a chain extender and a cross-linker, wherein the polyurethane foam has a density of less than 1.8 pounds per cubic foot, a flame spread index of 26 to 75 according to ASTM E-84, and passes an FM 4450 Calorimeter Test.

10. The polyurethane foam of claim 9, wherein the organic polyisocyanate comprises polymeric MDI and is present in an amount of 55% to 67% by weight, based on the total weight of the foam-forming composition.

11. The polyurethane foam of claim 9, wherein the foam has isocyanurate linkages.

12. An insulated roof assembly comprising: (a) a deck; (b) insulation panels mechanically attached to the deck, wherein the insulation panels comprise the polyurethane foam of claim 9.

13. The polyurethane foam of claim 9 having a flame spread index of 35 to 11 according to ASTM E-84.

14. The polyurethane foam of claim 9 wherein the one or more catalysts consist of an amine catalyst and a metal carboxylate trimer catalyst.

15. The polyurethane foam of claim 9 wherein the pentane comprises n-pentane.

16. The polyurethane foam of claim 9, wherein the pentane consists of n-pentane.

Description

BRIEF DESCRIPTION OF THE DRAWING

(1) FIG. 1 illustrates the layout for the insulation boards for the roof assembly for the FM 4450 calorimeter Test conducted on foams produced in Examples 8-13.

DETAILED DESCRIPTION OF THE INVENTION

(2) It has unexpectedly been found that use of 1 or more less flammable hydrocarbon blowing agents (i.e., hydrocarbons with LEL values greater than 2%) and blends of such less flammable hydrocarbon blowing agents with more flammable hydrocarbons (i.e., hydrocarbons with LEL values less than 2%) with non-halogen containing flame retardants in a foam-forming mixture is particularly advantageous because rigid polyurethane foams that can withstand exposure to the 5000 Btu/min flaming heat source applied in E-84 testing to the extent that a Class B designation can be obtained and that flammability criteria in FM 4450 testing are met. The halogen-free rigid polyurethane foams produced in accordance with the present invention can be made at lower density while still meeting the ASTM E-84 NFPA 101 Class B and passing the FM 4450 Roof calorimeter test standards for roofing applications.

(3) The present invention will now be described for purposes of illustration and not limitation. Except in the operating examples, or where otherwise indicated, all numbers expressing quantities, percentages, functionalities and so forth in the specification are to be understood as being modified in all instances by the term about.

(4) The foam-forming compositions of the present invention include: a) at least 50% by weight based on total weight of the foam-forming composition, of an organic polyisocyanate, b) at least one isocyanate-reactive polyether or polyester polyol with a nominal functionality of at least 2.0, c) a hydrocarbon blowing agent mixture that includes: i. no more than 10% by weight, based on total weight of the foam-forming composition, preferably, no more than 8% by weight, most preferably, from 2 to 8% by weight, of one or more hydrocarbon compounds having individual LEL less than 2% by volume in air, and/or ii. one or more hydrocarbon compounds having an individual LEL greater than 2% by volume in air, and iii. up to 1% by weight, based on total weight of the foam-forming composition, of water,
and d) at least one halogen-free flame retardant compound.

(5) These compositions produce a polyurethane foam having a density ranging from 1.60 pcf (25.6 kg/m.sup.3) to 5 pcf (80.1 kg/m.sup.3) that meets the NFPA 101 Class B ASTM E-84 standard and passes the FM 4450 Roof calorimeter test when reacted.

(6) The LEL for a combustible gas is defined as the lowest concentration of that gas in air by volume that will ignite or catch fire in the presence of an ignition source. Hydrocarbon gases commonly used to make PIR rigid foam insulation include n-pentane, isopentane, and cyclopentane which have LEL values of 1.5%, 1.4%, and 1.1% at 20 C. and 1 atmosphere of pressure, respectively.

(7) The LEL value for any gas or vapor can be found in the Material Safety Data Sheets from the suppliers of that material or in reference materials such as the NIOSH Pocket Guide to Chemical Hazards. The amount of these compounds used depends upon the desired foam density and may range from about 2% to 15% by weight, based on total weight of the system. Even though the blowing agent is only a small portion of the total foam-forming system, it exerts a disproportionate effect on flammability performance in tests where an ignition source is used in the presence of a controlled draft such as in the ASTM E-84 Tunnel test.

(8) In the present invention, the amount of extremely flammable material or combination of materials with an LEL of less than 2% must be limited to no more than 10%, preferably, less than 8%, most preferably, from 2 to 8% by weight, based on total weight of the foam-forming system. Examples of suitable hydrocarbons having an LEL of less than 2% which are suitable as blowing agents in the foam-forming reaction mixtures of the present invention include: n-pentane, isopentane, cyclopentane, butane, hexane, 2,2-dimethylbutane, 2-methylpentane, butenes, hexenes, and pentenes. The most preferred extremely flammable hydrocarbon compounds are n-pentane, isopentane, cylcopentane and mixtures thereof with LEL values less than 2%.

(9) Some water is included in the foam-forming mixture in an amount necessary to achieve the desired density as carbon dioxide generated by reaction of the water with the isocyanate acts as a co-blowing agent.

(10) It is, of course, possible to use a combination of extremely flammable material(s) having an LEL of less than 2% with some amount of a slightly less flammable material having an LEL greater than 2% by volume in air. The amount of the less flammable hydrocarbon will vary depending upon the foam properties sought, e.g., density. Examples of suitable hydrocarbons having an LEL greater than 2% by volume in air include: acetone, acetaldehyde, dimethyl carbonate, dimethyl ether, methylal, ethyl formate, methyl acetate, and methyl formate. Methyl formate is most preferred.

(11) In addition to the hydrocarbon blowing agent, some water is included in the blowing agent composition. The appropriate amount of water is determined on the basis of the desired foam density to be generated by the carbon dioxide gas co-blowing agent.

(12) The amount of water included in the foam-forming reaction mixture will generally range from about 0.05% to about 1% by weight, based on total weight of the foam-forming system, preferably from about 0.10% to about 0.80%, most preferably, from about 0.10% to about 0.40% by weight.

(13) The blowing agent composition of the present invention reduces the need for highly efficient vapor phase radical scavengers so that condensed phase flame retardants free of halogen can be used to produce Class B rigid foam systems.

(14) For higher density foams (i.e., foams having a density of at least 1.80 pounds per cubic foot (28.8 kg/m.sup.3), preferably, from 1.80 pcf (28.8 kg/m.sup.3) to 5 pcf (80.1 kg/m.sup.3), most preferably, from 1.85 pcf (29.6 kg/m.sup.3) to 3 pcf (48.1 kg/m.sup.3)) meeting the NFPA 101 Class B ASTM E-84 standard and passing the FM 4450 Roof calorimeter test, the blowing agent composition need only include (i) up to 1% by weight, based on total weight of foam-forming system, preferably, from 0.10% to 0.80% by weight, most preferably, from 0.10% to 0.40% by weight, of water to produce carbon dioxide (CO.sub.2) as a co-blowing agent and (ii) less than 10% by weight, based on total weight of the foam-forming composition, preferably, from 2% to 10% by weight, most preferably, from 2% to 8% by weight, of one or more hydrocarbon compounds having LEL values less than 2%.

(15) Generally, no hydrocarbon blowing agent with an LEL greater than 2% is required to prepare foams having densities greater than about 1.85 pcf (29.6 kg/m.sup.3) with a halogen-free flame retardant. However, inclusion of a hydrocarbon blowing agent with an LEL greater than 2% in amounts of up to 5% by weight, based on total weight of foam-forming system is within the scope of the present invention. The optimum amount of hydrocarbon blowing agent with an LEL value of greater than 2% by volume in air to achieve a desired balance of flammability performance, thermal conductivity, compressive strength, and dimensional stability can be readily determined by those skilled in the art.

(16) For lower density foams at the higher end of the FSI Class B range(i.e., foams having a density of less than 1.80 pcf (28.8 kg/m.sup.3), preferably from 1.50 pcf (24 kg/m.sup.3) to 1.85 pcf (29.6 kg/m.sup.3), most preferably, from 1.60 pcf (25.6 kg/m.sup.3) to 1.80 pcf (28.8 kg/m.sup.3)), the blowing agent composition used to produce foams in accordance with the present invention need only include (i) one or more hydrocarbon compounds having an individual LEL less than 2% by volume in air and (ii) no more than 1% by weight, based on total weight of the foam-forming system, preferably, from 0.10% to 0.80% by weight, most preferably, from 0.10% to 0.40% by weight, of water. Although one or more hydrocarbons having an LEL value greater than 2% by volume in air may be included in the blowing agent composition for lower density foams in amounts of up to 5% by weight, it is preferred that no more than 2% by weight and most preferred that no hydrocarbon having an LEL value of greater than 2% by volume in air be included in such blowing agent composition.

(17) For lower density foams with better flame spread performance(i.e., foams having a density of less than 1.80 pcf (28.8 kg/m.sup.3), preferably from 1.50 pcf (24 kg/m.sup.3) to 1.85 pcf (29.6 kg/m.sup.3), most preferably, from 1.60 pcf (25.6 kg/m.sup.3) to 1.80 pcf (28.8 kg/m.sup.3)), the blowing agent composition used to produce foams in accordance with the present invention need only include (i) one or more hydrocarbon compounds having an individual LEL greater than 2% by volume in air and (ii) no more than 1% by weight, based on total weight of the foam-forming system, preferably, from 0.10% to 0.80% by weight, most preferably, from 0.10% to 0.40% by weight, of water. Although one or more hydrocarbons having an LEL value less than 2% by volume in air may be included in the blowing agent composition for lower density foams in amounts of up to 7% by weight, it is preferred that no more than 5% by weight and most preferred that no more than 2% of hydrocarbon having an LEL value of less than 2% by volume in air be included in such blowing agent composition.

(18) The optimum amount of hydrocarbon is dependent upon the LEL for the compound or blend. Higher LEL values allow more blowing agent to be used in rigid foam production to lower density or increase isocyanate index.

(19) Any of the known polyfunctional isocyanates may be used in the practice of the present invention. Examples of suitable polyisocyanates include: substituted or unsubstituted aromatic, aliphatic, and cycloaliphatic polyisocyanate compounds having at least two isocyanate groups.

(20) Polyfunctional aromatic isocyanates are particularly preferred for making rigid polyurethane foam insulation. Examples of suitable aromatic isocyanates include: 4,4-diphenylmethane diisocyanate (MDI), polymeric MDI (PMDI), toluene diisocyanate, allophanate-modified isocyanates, isocyanate-terminated prepolymers and carbodiimide-modified isocyanates. Polymeric MDI having an average NCO functionality of from 2.2 to 3.3 and a viscosity of from 25 to 2000 mPas and prepolymers of such polymeric MDI prepared with polyols or other oligomers or polymers such as polyether or polyester polyols that contain active hydrogen atoms. The most preferred PMDI has a functionality of from 2.2 to 3.0 and a viscosity less than about 800 mPas at 25 C. The organic polyisocyanate used in the foam-forming system of the present invention may, of course, be a mixture of such polyisocyanates.

(21) The organic polyisocyanate(s) is/are included in the foam-forming system in an amount of at least 50%, preferably, from about 55% to about 75%, most preferably, from about 55% to about 67% by weight, based on total weight of the foam-forming system.

(22) Any material having at least two reactive groups capable of reacting with an isocyanate group is suitable for use in the polyurethane-forming reaction mixtures of the present invention. Particularly preferred isocyanate-reactive materials include polyester and polyether polyols having at least two isocyanate-reactive end groups, preferably, from 2 to 8 isocyanate-reactive end groups, most preferably, from 2 to 6 isocyanate-reactive end groups and blends thereof are particularly suitable for the practice of the present invention. Aromatic polyesters are most preferred because of their generally higher thermo-oxidative stability. Examples of commercially available polyester polyols suitable for use in the practice of the present invention are those sold by the Stepan Company under the name Stepanpol and those sold by Invista under the name Terate. Polyester or polyether polyols that contain halogenated flame retardants or additives are not suitable for use in the halogen-free reactive systems and foams of the invention. Preferred polyols for use in the present invention will generally have functionalities of from 2.0 to 8.0 and hydroxyl numbers of from about 25 mg KOH/gm to about 1000 mg KOH/gm. More preferred are aromatic polyester polyols having hydroxyl numbers from about 100 mg KOH/gm to about 500 mg KOH/gm and functionalities of from 2.0 to about 2.5. Most preferred are blends of aromatic polyester polyols and polyester or polyether polyols that contain renewable content derived from incorporation of regenerable materials such as fatty acid triglycerides, sugars, or natural glycerin.

(23) The polyol(s) is/are generally included in the foam-forming reaction mixture in an amount of from 10% to 45%, preferably, from 20% to 40%, most preferably, from 25% to 40% by weight, based on total weight of the foam-forming mixture.

(24) Hydrocarbon blowing agents are used in the reactive systems of the present invention. The term hydrocarbon is used herein to refer to chemical compounds composed primarily of carbon and hydrogen that may contain heteroatoms such as oxygen, nitrogen, sulfur, or other elements excluding halogens. Halogenated blowing agents are not used in the practice of the invention. For purposes of description of the invention, extremely flammable hydrocarbon blowing agents are defined as compounds with LEL values less than 2% by volume in air and include n-pentane, isopentane, cyclopentane, butane, hexane, 2,2-dimethylbutane, 2-methylpentane, butenes, hexenes, and pentenes. The most preferred extremely flammable hydrocarbon compounds are n-pentane, isopentane, cylcopentane or mixtures thereof with LEL values less than 2% that comprise less than 10% based on total system weight of the total reaction system. Formulation compositions comprised of less than 8% by weight on total system weight of extremely flammable hydrocarbon blowing agents are even more preferred.

(25) Slightly less flammable hydrocarbon compounds with LEL values equal to or greater than 2.0% by volume in air may be used in combination with extremely flammable blowing agents or used alone to further reduce flammability of the blowing agent mixture and/or produce rigid polyurethane materials with densities less than 1.85 lbs./ft.sup.3(29.6 kg/m.sup.3). Less flammable hydrocarbon blowing agents with LEL values greater than or equal to 2.5% such as acetone, acetaldehyde, dimethyl carbonate, dimethyl ether, methylal, ethyl formate, methyl acetate, and methyl formate are preferred in the practice of this aspect of the invention with methyl formate being most preferred as the slightly less flammable hydrocarbon blowing agent.

(26) Water also may be used in the practice of the invention to further control product density since it reacts with isocyanates to produce carbon dioxide gas as an auxiliary blowing agent. However, the thermal conductivity of CO.sub.2 is generally higher than those of hydrocarbon blowing agents, so the amount of water in the formulation must be controlled to prevent negative effects on the insulating ability of rigid foam produced by the practice of the invention. Consequently, no more than 1% by weight of water based on total system weight is used in the reactive system and levels less than 0.8% are preferred in the practice of the invention.

(27) Only halogen-free flame retardants are suitable for use in the reactive systems of the present invention. Suitable flame retardants may be nonreactive or reactive solids or liquids at normal temperatures and pressures. Halogen-free flame retardants, as that term is used herein, includes any compounds other than isocyanate-reactive materials that contain only carbon, hydrogen, oxygen and/or nitrogen that demonstrate a measurable improvement in flammability performance in ASTM E-84 when compared to the same reactive system without the flame retardant compound present. Suitable solid flame retardants include ammonium polyphosphates, melamine and its derivatives, borates, aluminum trihydrate (ATH), magnesium hydroxide, silicates, graphite, and nanoclay particles. However, liquid halogen-free flame retardants are preferred because equipment modifications are generally not required. Desirable halogen-free liquid flame retardants include halogen-free organophosphorus and silicone compounds. Suitable organophosphorus compounds include: phosphates, phosphonates, phosphites, phosphine oxides, phosphorus derivatives of iscyanate reactive materials such as diethyl N,N-bis(2-hydroxyethyl) aminomethyl phosphonate and phosphate esters of the Exolit OP 500 series. Triethyl phosphate, tributyl phosphate, tributoxyethyl phosphate, oligomeric ethyl ethylene phosphate, bisphenol A bis(diphenyl phosphate), resorcinol bis(diphenyl phosphate), diethyl ethyl phosphonate, and dimethyl propane phosphonate are preferred organophosphorus compounds for practice of the invention.

(28) Other additives known to be useful in the production of rigid foams such as surfactants, catalysts, processing aids, chain extenders, and cross-linkers may be added to the reactive systems of the present invention. Surfactants are generally copolymers of ethylene oxide/propylene oxide with polysiloxanes that control nucleation and cell-size distribution in the rigid foam and improve mixing of the blend components. Some of the commercially available surfactants include those of the Tegostab series from Evonik such as Tegostab 8513 and Tegostab 8465. Amine catalysts promote reaction of active hydrogen compounds such as polyols and water with isocyanates and may, along with metal carboxylates, trimerize isocyanate groups into highly thermally stable isocyanurate linkages. Pentamethyldiethylenetriamine (PMDETA), dimethylcyclohexylamine, and tris 2,4,6-dimethylaminomethyl phenol are examples of suitable amine catalysts. Potassium octoate and acetate are examples of suitable metal carboxylate trimer catalysts.

(29) Suitable amounts of such additives to be included in the foam-forming system of the present invention may be readily determined by those skilled in the art.

(30) Foams meeting the NFPA 101 Class B ASTM E-84 standard and passing the FM 4450 Roof calorimeter test are produced by reacting the organic polyisocyanate and the isocyanate-reactive composition in the presence of a halogen-free hydrocarbon blowing agent and optionally, water. Any of the known techniques for producing a rigid polyurethane foam may be used.

(31) The foams of the present invention are characterized by an NFPA 101 Class B rating measured in accordance with ASTM E-84 standard and by meeting the flammability criteria for an FM 4450 Class 1 rating. These foams are particularly useful for insulation applications and roofing assemblies.

(32) Processes for producing foams from the foam-forming compositions of the present invention are known to those skilled in the art. Examples of suitable processes include the known methods for producing polyisocyanurate laminated board stock insulation, methods for producing free-rise bunstock rigid foam insulation, froth-forming method for continuously producing glass fiber reinforced insulation boards in accordance with teachings of U.S. Pat. No. 4,572,865, continuous or discontinuous methods.

EXAMPLES

(33) The present invention is further illustrated, but is not to be limited, by the following examples in which all parts and percentages are parts by weight or percentages by weight, unless otherwise indicated.

(34) Characteristics and flammability test results for foams prepared from the foam-forming systems of the present invention are reported in the Tables. All ASTM E-84 (UL 723) tunnel tests were done on 2.75 (7 cm) thick samples without facer at Underwriters Laboratories Northbrook, Ill. facility while FM 4450 calorimeter tests were done on nominal 1.5 (3.8 cm) thick samples with facer. Thicker samples typically produce more smoke and higher flame spread in the tunnel and thinner samples are more likely to fail the calorimeter test. It is particularly noteworthy that inventive Example 13 made with 100% pentane as a blowing agent and inventive Example 10 made with an 80/20 blowing agent blend of pentane and methyl formate performed so poorly relative to the halogenated control comparative Example 8 in the predictive lab muffle furnace test. However, both samples easily passed the full-scale FM 4450 Roof calorimeter test. This observation supports the performance requirement that rigid foams of the invention with a Class B rating must pass the Factory Mutual test since smaller scale test results may be misleading.

(35) Hand-Mix Lab Foam Preparation Procedure

(36) All B-side components (i.e., components included in the isocyanate-reactive component) with the exception of the blowing agent were blended with a mechanical flat blade turbine mixer. Blowing agent was added to the B-side resin blend and mixed briefly before the isocyanate was added and the resultant mixture was mixed at high speed for about 5 seconds. The mixture was then poured into a 12 (30.5 cm)12 (30.5 cm)2.5 (6.4 cm) cardboard box and the foam was allowed to rise freely. The rising foam surface was gently probed with a wooden stick to determine string gel and tack free time. In instances where a sample was needed to perform the Bayer Mini Tunnel Test (described below), the foam mixture was poured into two 14 (35.6 cm)6(16.2 cm)4 (10.2 cm) cardboard boxes so that four 12 (30.5 cm)6 (17.5 cm)1 (2.5 cm) samples could be cut from the foam cores.

(37) Bayer Alpha Mini Tunnel Test

(38) Performance in this small scale tunnel test roughly correlates to results obtained in the Steiner Tunnel used to conduct ASTM E-84 testing. Core foam samples are cut to 6 (17.5 cm)48 (121.9 cm)up to 2 (5.1 cm) thick. Multiple foam samples of equal length can be used for a total length of 48 inches (121.9 cm). Typically three sample sections 16 inches (40.6 cm) long are used to simulate the three 8 (243.8 cm) long samples in the full scale test. The sample sections are placed in the tunnel and ignited by the burner that is positioned such that the flame tip is 14 (35.6 cm) from the start end of the tunnel. Progression of the flame from the burning foam along the tunnel is recorded at timed intervals by an operator observing through windows installed in the tunnel floor. The operator actually monitors the flame by looking at the flame reflection in an angled mirror positioned underneath clear window floor of the raised tunnel apparatus. An optical sensor in the tunnel ventilation system gathers data that is used to calculate the smoke index. The Flame Spread Constant of a 48 inch (121.9 cm) sample (FSC.sub.48) is calculated using the following equation:

(39) $\frac{\mathrm{Average}\mathrm{Distance}-14}{{\mathrm{FSC}}_{48}}=\frac{29.9-14}{22}$

(40) Based on historical comparisons of results obtained for samples tested in both the Steiner Tunnel and the Bayer Alpha Mini Tunnel, a FSC.sub.48 of 28 or less and a smoke index of 200 or less is expected to correspond to an E-84 flame spread index of 25 or less with a smoke index of 450 or less. The alpha tunnel test does not correlate well with foam samples having a flame spread index (FSI) greater than 35 in the large scale ASTM E-84 tunnel test since the flame spread of such foams usually exceeds 48 inches (121.9 cm) in the lab tunnel.

(41) Bayer Muffle Furnace Test

(42) This test was designed to compare behavior of test materials to that of controls that are known to pass requirements of the Factory Mutual Roof calorimeter test (FM 4450). A foam sample with dimensions of 4 (10.2 cm)4 (10.2 cm)up to 2.5 (6.4 cm) was completely wrapped in aluminum foil. The mass of the foil and foam were recorded separately along with the foam height. A small muffle furnace containing a removable open top metal compartment sized to hold the foam sample was preheated to 450 C. The oven was opened briefly to insert the foil-wrapped foam sample into the metal holder and the foam was heated for 20 minutes at 450 C. The metal holder was removed from the oven and allowed to cool. The weight of foil-wrapped foam sample was recorded before gently un-wrapping the foam to measure and record its residual height at the sample's thinnest section of remaining foam. Also, the height of any foam area free of char was recorded. Test results are reported as % weight lost, % height retained, and the amount of no char in inches. The results are compared to those of a control sample that is known to pass the Roof calorimeter test with the expectation that the experimental sample will pass also if its results are equal to or better those of the control. However this assumption typically is only valid for samples prepared via a high-pressure mixing machine process as would be used to make the commercial product. As illustrated in Table 2, muffle furnace results for hand-mixed lab foams can differ markedly from those obtained using the same formulation on the laminator machine.

(43) Pilot Line Laminator Unit

(44) PIR laminated boardstock foam samples were prepared on Bayer's pilot-scale Hennecke unit at the Pittsburgh, Pa. USA facility. The laminator was approximately 26 feet (7.9 m) long and equipped with a single mix-head which made boards that were 30 inches (76.2 cm) wide. The mix-head was outfitted with a two-stream T made with CPVC piping. The B side resin blend (i.e., polyol-containing component) was premixed with the third-streamed blowing agent inline via a special Triple Action Dispersion Device (TADD) from Komax, Inc. prior to entering the static mixer and exiting the mix-head after being subjected to impingement mixing at 1800 psi (126.6 kg/cm.sup.2) to 2500 psi (175.8 kg/cm.sup.2). The conditions used for foams made in this study were as follows:

(45) TABLE-US-00001 Total Feed Rate 22 to 45 lbs./min (10-20.4 kg/min) Resin Temperature 82 F. Isocyanate Temperature 82 F. Platen Temperature 145 F. Line Speed 34 to 38 ft./min (10.4-11.6 m/min)
The nominal board thickness for tested foams in Table 3 was set at 1.5 inches (3.8 cm) unless otherwise noted and the foam was laminated with black facer. The board was perforated on the top surface using a weighted spiked roller as it exited the unit.
ASTM E-84 (UL 723) Tunnel Testing

(46) All foam samples for this test were prepared at a nominal thickness of 3.0 (7.6 cm) with standard black facer. The top and bottom (0.6 cm) of foam was slit from the boards to remove the facer. The slit samples were tested at Underwriters Laboratories Fire Protection facilities in Northbrook, Ill. as developmental materials.

(47) Roof Assembly for FM 4450 calorimeter Test

(48) The roof assembly was built by personnel at Factory Mutual's test laboratory in West Glocester, R.I. and was composed of the following layered sequence: 1. Approved 18 gauge steel deck. 2. Rigid foam roof insulation samples with standard black facer, mechanically attached to the deck. 3. 3 ply organic felt Built-Up roof with hot asphalt applied at 25 lbs. per 100 square feet (1.22 kg/m.sup.2). 4. 60 lb. (27.2 kg) flood coat of asphalt.

(49) The layout for installation of these roof insulation boards was slightly different from the conventional diagram based on 48-inch (122 cm) wide commercial product and is shown in FIG. 1. In the conventional assembly, a 36-inch (91.4 cm) wide panel and 24-inch (61 cm) wide panel form a single vertical seam in the assembly, but the installation used for testing of roofing assemblies made with the foams of the present invention required that two vertical seams using two 24-inch (61 cm) wide boards and a single 12-inch (30.5 cm) wide panel be used because the pilot laminator unit could only make boards with a maximum width of 30 inches (76.2 cm). No thermal barrier was used between the deck and foam insulation and no cover board was used on top of the foam insulation.

(50) Various formulations used to prepare rigid polyurethane foams based on the inventive reactive systems are shown in Tables 1, 2 and 3. The amounts listed in Tables 1, 2 and 3 are parts by weight.

(51) The materials used to produce the foams in the Examples which follow were: POLYOL: Stepanpol PS-2352 polyester polyol having a functionality of 2 and an OH Value of 235 which is commercially available from the Stepan Company. K-15: Potassium octoate which is commercially available under the name Dabco K-15 from Air Products Company, PMDETA: pentamethyldiethylenetriamine available under the name Desmorapid PV from Bayer MaterialScience. Polycat 46: Potassium acetate available under the name Polycat 46 from Air Products Company. B 8513: Surfactant available under the name Tegostab B 8513 from Evonik Industries. PCF: Halogenated flame retardant which is commercially available under the name Fyrol PCF from ICL-Supresta. TEP: Halogen-free flame retardant triethyl phosphate commercially available from Eastman Chemical. TEP-Z: Halogen-free flame retardant commercially available under the name Levagard TEP-Z available from Lanxess. RDP: Resorcinol bis(diphenyl phosphate), halogen-free flame retardant which is commercially available under the name Fyrolflex RDP from ICL-Supresta, n-Pentane: The blowing agent n-pentane. MF: The blowing agent methyl formate. NCO: Polymeric MDI which is commercially available under the name Mondur 489 from Bayer MaterialScience.

(52) TABLE-US-00002 TABLE 1 Hand-Mixed Foams Example 1 2 3 POLYOL 29.55 27.42 33.00 TEP 2.25 3.50 RDP 3.56 B 8513 0.72 0.54 0.76 K-15 1.44 1.19 1.06 Polycat 46 0.23 0.23 PMDETA 0.11 0.21 0.08 Water 0.22 0.10 0.15 n-Pentane 5.61 6.75 6.47 NCO 60.3 60.0 55.0 Index 2.75 2.75 2.50 Density (pcf) 1.75 1.76 1.73 [kg per m.sup.3] [28] [28.2] [27.7] Mini Tunnel FSC 37 38 SDI 218 170

(53) TABLE-US-00003 TABLE 2 Muffle Furnace Results: Hand-Mix vs Machine (Laminator) Example 4* 5* 6* 7* Hand-mix Hand-mix Laminator Laminator POLYOL 28.00 28.00 28.08 28.08 PCF 3.70 3.70 3.71 3.71 B-8513 0.70 0.70 0.70 0.70 K-15 1.42 1.42 1.42 1.42 Polycat 46 0.22 0.22 0.22 0.22 PMDETA 0.11 0.11 0.12 0.12 Water 0.14 0.14 0.14 0.14 n-pentane 6.12 6.12 6.02 6.02 NCO 59.58 59.58 59.58 59.58 Index 3.00 3.00 3.00 3.00 Density (pcf) 1.75 [28] 1.75 [28] 1.71 [27.4] 1.74 [27.9] [kg/m.sup.3] Thickness, 1.99 [5.1] 1.48 [3.8] 2.18 [5.5] 1.64 [4.2] Initial (in.) [cm] Muffle Furnace Height, % 83 81 57 47 Retention Weight, % 37 37 44 46 Lost No Char (in.) 0.65 [1.7] 0.44 [1.1] 0.61 [1.5] 0.30 [0.8] [cm] *Comparative Example

(54) TABLE-US-00004 TABLE 3 Laminator Board Samples Example 8* 9 10 11 12 13 POLYOL 28.04 29.47 29.14 29.07 28.40 33.00 PCF 4.01 TEP 2.25 3.55 3.50 RDP 3.58 5.62 B 8513 0.70 0.72 0.71 0.71 0.70 0.76 K 15 1.42 1.42 1.41 1.42 1.42 1.06 Polycat 46 0.22 0.23 0.23 0.23 0.23 PMDETA 0.11 0.11 0.11 0.11 0.11 0.08 Water 0.14 0.22 0.22 0.22 0.21 0.15 n-Pentane 5.88 4.21 4.11 4.23 4.14 6.47 MF 1.05 1.03 1.06 1.03 NCO 59.5 60.3 59.5 59.4 58.1 55.0 Index 3.00 2.75 2.75 2.75 2.75 2.50 Density (pcf) [kg/m.sup.3] 1.73 [27.7] 1.78 [28.5] 1.78 [28.5] 1.79 [28.7] 1.71 [27.4] 1.67 [26.8] Bd. Thickness (in.) 1.67 [4.2] 1.64 [4.2] 1.62 [4.1] 1.65 [4.2] 1.69 [4.3] 1.70 [4.3] [cm] Compressive Strength 14.6 [1] 14.4 [1] 17.0 [1.2] 18.8 [1.3] 16.1 [1.1] 15.8 [1.1] 10% Defl. (psi) [kg/cm.sup.2] Init. K-factor @ 35 F., 0.158 0.157 0.154 0.156 0.157 0.161 Btu-in./hr.ft.sup.2 F. Mini Tunnel FSC 33 34 34 35 32 33 SDI 107 206 195 172 131 97 Muffle Furnace Height, % Retention 49.7 2.4 2.5 68.6 71.5 10.2 Weight, % Lost 48.8 52.6 50.3 49.0 49.1 52.0 No Char (in.) [cm] 0.145 [0.37] 0 0 0.495 [1.26] 0.385 [1] 0 ASTM E-84 Thickness (in.) [cm] 2.75 [7] 2.75 [7] 2.75 [7] 2.75 [7] Density (pcf) [kg/m.sup.3] 1.71 [27.4] 1.75 [28] 1.71 [27.4] 1.54 [24.7] FSI 45 40 35 65 SDI 170 145 150 195 NFPA 101 Rating Class B Class B Class B Class B FM Calorimeter Fuel Contribution Rates BTU/ft..sup.2/min. Pass Pass Pass Pass Pass 3 min. (410 max) 190 207 89 118 246 5 min. (390 max) 190 207 89 117 244 10 min. (360 max) 159 205 89 117 243 30 min. Avg. (285 133 154 87 87 167 max) *Comparative Example

(55) The foregoing examples of the present invention are offered for the purpose of illustration and not limitation. It will be apparent to those skilled in the art that the embodiments described herein may be modified or revised in various ways without departing from the spirit and scope of the invention. The scope of the invention is to be measured by the appended claims.