Non-cellular and cellular composites of polyurethanes and vinyl polymers

Claim 2

A process for preparing non-cellular polyurethane/vinyl polymer composite articles having a density of at least about 1 g/cc without the application of an external source of heat which process comprises: (I) admixing the components of a composition comprising (A) a liquid polyol free of nitrogen atoms and substantially free of ethylenic unsaturation or mixtures of such polyols having from about 2 to about 8 hydroxyl groups and an average OH equivalent weight of at least about 30; (B) an organic polyisocyanate which is substantially free of ethylenic unsaturation or a mixture of such polyisocyanates having an NCO equivalent weight of less than about 1000, with the proviso that when component (A) has an average of about 2 hydroxyl groups per molecule, said polyisocyanate has an average of at least about 2.5 NCO groups per molecule; (C) from about 15% to less than about 75% by weight of the combined weight of Components (A), (B), (C), (D) and (E) of a polymerizable ethylenically unsaturated monomer having an atmospheric boiling point above about 70° C; (d) an effective quantity of a suitable catalyst for polymerizing component (C); (e) an effective quantity of a suitable catalyst for urethane formation selected from the compounds of the metals cobalt, copper, vanadium, and mixtures thereof; and (F) from 0 to about 50% by weight based upon the combined weight of Components (A), (B), (C), (D), (E) and (F) of a modifier substance free from groups reactive with components (A), (B) or (C) at the conditions employed herein, said modifier substances being selected from the group consisting of (1) liquid substances having an atmospheric boiling point of at least about 150° C; (2) solid substances having a surface area of less than about 0.8 m 2 /gram and a particle size such that said substance will pass through a one-fourth inch square opening, is substantially free of any absorbed or occluded water and will not decompose at a temperature below the maximum exotherm temperature generated by the urethane forming reaction; (3) polymers of one or more ethylenically unsaturated monomers, said polymers having (a) a molecular weight such that the polymer has a grease melt index as determined with a 0.02-inch orifice employing a total weight of 2160 grams at 80° C of from about 1 to about 250 grams/minute; (b) a solubility parameter of at least about 8; and (c) a specific heat of at least about 0.35 calories/gram/° C; and (4) mixtures thereof; and wherein components (A) and (B) are present in quantities such that the NCO:OH equivalent ratio is from about 0.70:1 to about 1.5:1 and with the following provisos: (a) that the urethane exotherm temperature does not greatly exceed the boiling point of the monomer or mixtures of monomers employed as component (C); (b) that the combined quantity of component (C) and (F) be less than about 60% by weight based upon the combined weight of components (A), (B), (C) and (F); (c) that when Component (F-3) is employed as component (F), it is employed in quantities of 20% by weight of the combined quantities of components (A), (B) and (F); (ii) pouring the admixed composition into a suitable mold wherein said compositions solidifies to a solid having the aforesaid density; and (III) subsequently demolding the resultant articles from the mold.

Claim 3

The process of claim 1 wherein Components (A) and (B) are present in quantities such that the NCO:OH ratio is from about 0.9:1 to about 1.2:1 and the average OH equivalent weight of Component (A) is from about 30 to about 2500 and the average equivalent weight of Component (B) is less than about 750 and wherein Component (C) is essentially free of groups reactive with Components (A) or (B), has an atmospheric boiling point above about 100° C and is present in quantities of from about 20% to about 60%.

Claim 4

The process of claim 2 wherein Component (A) has an average OH equivalent weight of from about 50 to about 1000.

Claim 5

The process of claim 3 wherein Component (E) is a compound of cobalt, copper or mixtures thereof.

Claim 6

The process of claim 4 wherein Component (E) is an organic compound of cobalt.

Claim 7

The process of claim 5 wherein Component (E) is selected from the group consisting of cobalt naphthenate, Co II (dimethyl glyoxime) 2 , and cobalt acetate.4H 2 O.

Claim 8

The process of claim 4 wherein Component (E) is an inorganic compound of cobalt.

Claim 9

The process of claim 7 wherein Component (E) is selected from CoCl 2 .6H 2 O, Co(NO 3 ) 2 .6H 2 O and (Co III (NH 3 ) 4 CO 3 )NO 3 .

Claim 10

The process of claim 4 wherein Component (E) is a copper compound.

Claim 11

The process of claim 9 wherein Component (E) is copper naphthenate.

Claim 12

The process of claim 3 wherein Component (E) is V 2 O 5 , VCl 3 or VOCl 2 .

Claim 13

The process of claim 4 wherein Component (A) is an adduct of glycerine, trimethylolpropane, pentaerythritol, sucrose or mixtures thereof with propylene oxide, ethylene oxide or mixtures thereof.

Claim 14

The process of claim 12 wherein Component (A) is an adduct of glycerine with propylene oxide.

Claim 15

The process of claim 13 wherein Component (C) contains styrene.

Claim 16

Non-cellular polyurethane/vinyl polymer composite articles having a density of at least about 1 g/cc which results from the admixture without the application of an external source of heat of a composition which comprises: (A) a liquid polyol free of nitrogen atoms and substantially free of ethylenic unsaturation or mixture of such polyols having from about 2 to about 8 hydroxyl groups and an average OH equivalent weight of at least about 30; (B) an organic polyisocyanate which is essentially free of ethylenic unsaturation or a mixture of such polyisocyanates having an NCO equivalent weight of less than about 1000, with the proviso that when Component (A) has an average of about 2 hydroxyl groups per molecule, said polyisocyanate has an average of at least about 2.5 NCO groups per molecule; (C) from about 15% to less than about 75% by weight of the combined weight of Components (A), (B), (C), (D) and (E) of a polymerizable ethylenically unsaturated monomer having an atmospheric boiling point above about 70° C of a mixture of such monomers; (D) an effective quantity of a suitable catalyst for polymerizing Component (C); (e) an effective quantity of a suitable catalyst for urethane formation selected from compounds of the metals cobalt, copper and vanadium; and (F) from 0 to about 50% by weight based upon the combined weight of Components (A), (B), (C), (D), (E) and (F) of a modifier substance free from groups reactive with Components (A), (B) or (C) at the conditions employed herein, said modifier substances being selected from the group consisting of (1) liquid substances having an atmospheric boiling point of at least about 150° C; (2) solid substances having a surface area of less than about 0.8 m 2 /gram and a particle size such that said substance will pass through a one-fourth inch square opening, is substantially free of any absorbed or occluded water and will not decompose at a temperature below the maximum exotherm temperature generated by the urethane forming reaction; (3) polymers of one or more ethylenically unsaturated monomers, said polymers having (a) a molecular weight such that the polymer has a grease melt index as determined with a 0.02-inch orifice employing a total weight of 2160 grams at 80° C, from about 1 to about 250 grams/minute, preferably from about 75 to about 2000 grams/minute; (b) a solubility parameter of at least about 8 and preferably from about 8 to about 12.5; (c) and a specific heat of at least about 0.35 calories/gram/° C; and (4) mixtures thereof; and wherein Components (A) and (B) are present in quantities such that the NCO:OH equivalent ratio is from about 0.75:1 to about 1.5:1 and with the following provisos: (a) that the urethane exotherm temperature does not greatly exceed the boiling point of the monomer employed as Component (C); (b) that the combined quantity of Components (C) and (F) be less than about 65% by weight based upon the combined weight of Components (A), (B), (C) and (F); (c) that when Component (F-3) is employed as Component (F), it is employed in quantities of about 20% by weight based upon the combined quantities of Components (A), (B) and (F).

Claim 17

Non-cellular polyurethane/vinyl polymer composite articles having a density of at least about 1 g/cc which results from the admixture without the application of an external source of heat of a composition which comprises: (A) a liquid polyol free of nitrogen atoms and substantially free of ethylenic unsaturation or mixture of such polyols having from about 2 to about 8 hydroxyl groups and an average OH equivalent weight of at least about 30; (B) an organic polyisocyanate which is essentially free of ethylenic unsaturation or a mixture of such polyisocyanates having an NCO equivalent weight of less than about 1000, with the proviso that when Component (A) has an average of about 2 hydroxyl groups per molecule, said polyisocyanate has an average of at least about 2.5 NCO groups per molecule; (C) from about 15% to less than about 75% by weight of the combined weight of Components (A), (B), (C), (D) and (E) of a polymerizable ethylenically unsaturated monomer having an atmospheric boiling point above about 70° C of a mixture of such monomers; (D) an effective quantity of a suitable catalyst for polymerizing Component (C); (e) an effective quantity of a suitable catalyst for urethane formation selected from compounds of the metals cobalt, copper and vanadium; and (F) from 0 to about 50% by weight based upon the combined weight of Components (A), (B), (C), (D), (E) and (F) of a modifier substance free from groups reactive with Components (A), (B) or (C) at the conditions employed herein, said modifier substances being selected from the group consisting of (1) liquid substances having an atmospheric boiling point of at least about 150° C; (2) solid substances having a surface area of less than about 0.8 m 2 /gram and a particle size such that said substance will pass through a one-fourth inch square opening, is substantially free of any absorbed or occluded water and will not decompose at a temperature below the maximum exotherm temperature generated by the urethane forming reaction; (3) polymers of one or more ethylenically unsaturated monomers, said polymers having (a) a molecular weight such that the polymer has a grease melt index as determined with a 0.02-inch orifice employing a total weight of 2160 grams at 80° C, from about 1 to about 250 grams/minute, preferably from about 75 to about 2000 grams/minute; (b) a solubility parameter of at least about 8 and preferably from about 8 to about 12.5; (c) and a specific heat of at least about 0.35 calories/gram/° C; and (4) mixtures thereof; and wherein Components (A) and (B) are present in quantities such that the NCO:OH equivalent ratio is from about 0.75:1 to about 1.5:1 and with the following provisos: (a) that the urethane exotherm temperature does not greatly exceed the boiling point of the monomer employed as Component (C); (b) that the combined quantity of Components (C) and (F) be less than about 65% by weight based upon the combined weight of Components (A), (B), (C) and (F); (c) that when Component (F-3) is employed as Component (F), it is employed in quantities of about 20% by weight based upon the combined quantities of Components (A), (B) and (F).

Claim 18

The composite article of claim 15 wherein Components (A) and (B) are present in quantities such that the NCO:OH ratio is from about 0.9:1 to about 1.2:1 and the average OH equivalent weight of Component (A) is from about 30 to about 2500 and the average equivalent weight of Component (B) is less than about 750 and wherein Component (C) is essentially free of groups reactive with Components (A) or (B), has an atmospheric boiling point above about 100° C and is present in quantities of from about 20% to about 60%.

Claim 19

The composite article of claim 16 wherein Component (A) has an average OH equivalent weight of from about 50 to about 1000.

Claim 20

The composite article of claim 17 wherein Component (E) is a compound of cobalt, copper of mixtures thereof.

Claim 21

The composite article of claim 18 wherein Component (E) is an organic compound of cobalt.

Claim 22

The composite article of claim 19 wherein Component (E) is selected from the group consisting of cobalt naphthenate, Co II (dimethyl glyoxime) 2 , and cobalt acetate.4H 2 O.

Claim 23

The composite article of claim 18 wherein Component (E) is an inorganic compound of cobalt.

Claim 24

The composite article of claim 21 wherein Component (E) is selected from CoCl 2 .6H 2 O, Co(NO 3 ) 2 .6H 2 O and (Co III (NH 3 ) 4 CO 3 )NO 3 .

Claim 25

The composite article of claim 18 wherein Component (E) is a copper compound.

Claim 26

The composite article of claim 23 wherein Component (E) is copper naphthenate.

Claim 27

The composite article of claim 17 wherein Component (E) is V 2 O 5 , VCl 3 or VOCl 2 .

Claim 28

The composite article of claim 18 wherein Component (A) is an adduct of glycerine, trimethylolpropane, pentaerythritol, sucrose or mixtures thereof with propylene oxide, ethylene oxide or mixtures thereof.

Claim 29

The composite article of claim 26 wherein Component (A) is an adduct of glycerine with propylene oxide.

Claim 30

The composite article of claim 27 wherein Component (C) contains styrene.

Claim 31

Cellular polyurethane/vinyl polymer composites articles having substantially uniform cells, a density of less than 1 g/cc and which results without the application of an external source of heat after admixture of a composition which comprises (A) a liquid polyol free of nitrogen atoms and substantially free of ethylenic unsaturation or mixture of such polyols having from about 2 to about 8 hydroxyl groups and an average OH equivalent weight of at least about 30; (B) an organic polyisocyanate which is substantially free of ethylenic unsaturation or a mixture of such polyisocyanates having an average NCO equivalent weight of less than about 300, with the proviso that when Component (A) has an average of about 2 hydroxyl groups per molecule, said polyisocyanate has an average of at least about 2.5 NCO groups per molecule; (C) from about 15% to less than about 75% by weight of the combined weight of Components (A), (B), (C), (D) and (E) of a polymerizable ethylenically unsaturated monomer having an atmospheric boiling point above about 70° C or a mixture of such monomers; (D) an effective quantity of a suitable catalyst for polymerizing Component (C); (e) an effective quantity of a suitable catalyst for urethane formation selected from the compounds of the metals cobalt, copper and vanadium; and (F) from 0 to about 50% by weight based upon the combined weight of Components (A), (B), (C), (D), (E) or (F) of a modifier substance free from groups reactive with Components (A), (B) or (C) at the conditions employed herein, said modifier substances being selected from the group consisting of (1) liquid substances having an atmospheric boiling point of at least about 150° C; (2) solid substances having a surface area of less than about 0.8 m 2 /gram and a particle size such that said substance will pass through a 1/4-inch square opening, is substantially free of any absorbed or occluded water and will not decompose at a temperature below the maximum exotherm temperature generated by the urethane forming reaction; (3) polymers of one or more ethylenically unsaturated monomers, said polymers having (a) a molecular weight such that the polymer has a grease melt index as determined with a 0.02-inch orifice employing a total weight of 2160 grams/80° C of from about 1 to about 250 grams/minute; (b) a solubility parameter of at least about 8; and (c) a specific heat of at least about 0.35 calories/gram/° C; and (4) mixtures thereof; and (G) a foam-forming system which comprises (1) a foaming agent selected from the group consisting of (a) low boiling vaporizable organic liquids having a boiling point below the reaction exotherm temperature; (b) substances which decompose thermally to release CO 2 or release water vapor at the exotherm temperature; (c) a solid particulate substance which will pass through a 2 mm square opening and which has a surface area of at least 0.8 m 2 /gram; (d) an inorganic metal hydrate characterized as having a solubility in anhydrous ethyl alcohol of less than about 1.2 grams per 100 grams and a weight loss of at least 5% when subjected to a temperature of 115° C for 30 minutes at atmospheric pressure; (e) water; and (f) mixtures thereof; and (2) a cell control agent; and wherein Components (A) and (B) are present in quantities such that the NCO:OH equivalent ratio is from about 0.7:1 to about 1.5:1; Component (G-1) is present in quantities sufficient to provide the desired density and Component (G-2) is present in quantities sufficient to provide substantially uniform cells; and with the following provisos: (a) that the urethane exotherm temperature does not greatly exceed the boiling point of the monomer or mixture of monomers employed as Component (C); (b) that the combined quantity of Components (C) and (F) be less than about 60% by weight based upon the combined weight of Components (A), (B), (C) and (F); (c) that when Component (G-1-c) or (G-1-d) is employed as the blowing agent, Component (G-2) is not required; (d) that when Component (F-3) is employed as Component (F) it is employed in quantities to about 20% by weight based upon the combined weight of Components (A), (B) and (F).

Claim 32

Cellular polyurethane/vinyl polymer composites articles having substantially uniform cells, a density of less than 1 g/cc and which results without the application of an external source of heat after admixture of a composition which comprises (A) a liquid polyol free of nitrogen atoms and substantially free of ethylenic unsaturation or mixture of such polyols having from about 2 to about 8 hydroxyl groups and an average OH equivalent weight of at least about 30; (B) an organic polyisocyanate which is substantially free of ethylenic unsaturation or a mixture of such polyisocyanates having an average NCO equivalent weight of less than about 300, with the proviso that when Component (A) has an average of about 2 hydroxyl groups per molecule, said polyisocyanate has an average of at least about 2.5 NCO groups per molecule; (C) from about 15% to less than about 75% by weight of the combined weight of Components (A), (B), (C), (D) and (E) of a polymerizable ethylenically unsaturated monomer having an atmospheric boiling point above about 70° C or a mixture of such monomers; (D) an effective quantity of a suitable catalyst for polymerizing Component (C); (e) an effective quantity of a suitable catalyst for urethane formation selected from the compounds of the metals cobalt, copper and vanadium; and (F) from 0 to about 50% by weight based upon the combined weight of Components (A), (B), (C), (D), (E) or (F) of a modifier substance free from groups reactive with Components (A), (B) or (C) at the conditions employed herein, said modifier substances being selected from the group consisting of (1) liquid substances having an atmospheric boiling point of at least about 150° C; (2) solid substances having a surface area of less than about 0.8 m 2 /gram and a particle size such that said substance will pass through a 1/4-inch square opening, is substantially free of any absorbed or occluded water and will not decompose at a temperature below the maximum exotherm temperature generated by the urethane forming reaction; (3) polymers of one or more ethylenically unsaturated monomers, said polymers having (a) a molecular weight such that the polymer has a grease melt index as determined with a 0.02-inch orifice employing a total weight of 2160 grams/80° C of from about 1 to about 250 grams/minute; (b) a solubility parameter of at least about 8; and (c) a specific heat of at least about 0.35 calories/gram/° C; and (4) mixtures thereof; and (G) a foam-forming system which comprises (1) a foaming agent selected from the group consisting of (a) low boiling vaporizable organic liquids having a boiling point below the reaction exotherm temperature; (b) substances which decompose thermally to release CO 2 or release water vapor at the exotherm temperature; (c) a solid particulate substance which will pass through a 2 mm square opening and which has a surface area of at least 0.8 m 2 /gram; (d) an inorganic metal hydrate characterized as having a solubility in anhydrous ethyl alcohol of less than about 1.2 grams per 100 grams and a weight loss of at least 5% when subjected to a temperature of 115° C for 30 minutes at atmospheric pressure; (e) water; and (f) mixtures thereof; and (2) a cell control agent; and wherein Components (A) and (B) are present in quantities such that the NCO:OH equivalent ratio is from about 0.7:1 to about 1.5:1; Component (G-1) is present in quantities sufficient to provide the desired density and Component (G-2) is present in quantities sufficient to provide substantially uniform cells; and with the following provisos: (a) that the urethane exotherm temperature does not greatly exceed the boiling point of the monomer or mixture of monomers employed as Component (C); (b) that the combined quantity of Components (C) and (F) be less than about 60% by weight based upon the combined weight of Components (A), (B), (C) and (F); (c) that when Component (G-1-c) or (G-1-d) is employed as the blowing agent, Component (G-2) is not required; (d) that when Component (F-3) is employed as Component (F) it is employed in quantities to about 20% by weight based upon the combined weight of Components (A), (B) and (F).

Claim 33

The composite article of claim 29 wherein Components (A) and (B) are present in quantities such that the NCO:OH ratio is from about 0.9:1 to about 1.2:1 and the average equivalent weight of Component (A) is from about 30 to about 2500 and the equivalent weight of Component (B) is less than about 750 and wherein Component (C) is essentially free of groups reactive with Components (A) or (B), has an atmospheric boiling point above about 100° C and is present in quantities of from about 20% to about 60% and said composite has a density of from about 0.025 to about 0.8 g/cc.

Claim 34

The composite article of claim 30 wherein Component (A) has an average OH equivalent weight of from about 50 to about 1000.

Claim 35

The composite article of claim 31 wherein Component (E) is a compound of cobalt, copper or mixtures thereof.

Claim 36

The composite article of claim 32 wherein Component (E) is an organic compound of cobalt.

Claim 37

The composite article of claim 33 wherein Component (E) is selected from the group consisting of cobalt naphthenate, Co II (dimethyl glyoxime) 2 , and cobalt acetate.4H 2 O.

Claim 38

The composite article of claim 32 wherein Component (E) is an inorganic compound of cobalt.

Claim 39

The composite article of claim 35 wherein Component (E) is selected from CoCl 2 .6H 2 O, Co(NO 3 ) 2 .6H 2 O and (Co III (NH 3 ) 4 CO 3 )NO 3 .

Claim 40

The composite article of claim 32 wherein Component (E) is a copper compound.

Claim 41

The composite article of claim 37 wherein Component is copper naphthenate.

Claim 42

The composite article of claim 31 wherein Component (E) is V 2 O 5 , VCl 3 or VOCl 2 .

Claim 43

The composite article of claim 32 wherein Component (A) is an adduct of glycerine, trimethylolpropane, pentaerythritol, sucrose or mixtures thereof with propylene oxide, ethylene oxide or mixtures thereof.

Claim 44

The composite article of claim 40 wherein Component (A) is an adduct of glycerine with propylene oxide.

Claim 45

The composite article of claim 41 wherein Component (C) contains styrene.

Claim 46

A process for preparing cellular polyurethane/vinyl polymer composite articles having substantially uniform cells, a density of less than 1 g/cc which process comprises: (I) admixing the components of a composition comprising (A) a liquid polyol free of nitrogen atoms and essentially free of ethylenic unsaturation or mixture of such polyols having from about 2 to about 8 hydroxyl groups and an average OH equivalent weight of at least about 30; (B) an organic polyisocyanate which is essentially free of ethylenic unsaturation or a mixture of such polyisocyanates having an NCO equivalent weight of less than about 300 with the proviso that when Component (A) has an average of about 2 hydroxyl groups per molecule, said polyisocyanate has an average of at least about 2.5 NCO groups per molecule; (C) from about 15% to less than about 75% by weight of the combined weight of Components (A), (B), (C), (D) and (E) of a polymerizable ethylenically unsaturated monomer having an atmospheric boiling point above about 70° C or a mixture of such monomers; (D) an effective quantity of a suitable catalyst of polymerizing Component (C); (e) an effective quantity of a suitable catalyst for urethane formation selected from compounds of the metals cobalt, copper and vanadium; and (F) from 0 to about 50% by weight based upon the combined weight of Components (A), (B), (C), (D), (E) and (F) of a modifier substance free from groups reactive with Components (A), (B) or (C) at the conditions employed herein, said modifier substances being selected from the group consisting of (1) liquid substances having an atmospheric boiling point of at least about 150° C; (2) solid substances having a surface area of less than about 0.8 m 2 /gram and a particle size such that said substance will pass through a 1/4-inch square opening, is substantially free of any absorbed or occluded water and will not decompose at a temperature below the maximum exotherm temperature generated by the urethane forming reaction; (3) polymers of one or more ethylenically unsaturated monomers, said polymers having (a) a molecular weight such that the polymer has a grease melt index as determined with a 0.02-inch orifice employing a total weight of 2160 grams at 80° C of from about 1 to about 250 grams/minute; (b) a solubility parameter of at least about 8; and (c) a specific heat of at least about 0.35 calories/gram/° C; and (4) mixtures thereof; and (G) a foam-forming system which comprises (1) a foaming agent selected from the group consisting of (a) low boiling vaporizable organic liquids having a boiling point below the reaction exotherm temperature; (b) substances which decompose thermally to release CO 2 or release water vapor to the exotherm temperature; (c) a solid particulate substance which will pass through a 2 mm square opening and which has a surface area of at least 0.8 m 2 /gram; (d) an inorganic metal hydrate characterized as having a solubility in anhydrous ethyl alcohol of less than about 1.2 grams per 100 grams and a weight loss of at least 5% when subjected to a temperature of 115° C for 30 minutes at atmospheric pressure; (e) water; (f) mixtures thereof; and (2) a cell control agent; and wherein Components (A) and (B) are present in quantities such that the NCO:OH equivalent ratio is from about 0.75:1 to about 1.5:1, Component (G-1) is present in quantities sufficient to provide the desired density and Component (G-2) is present in quantities sufficient to provide substantially uniform cells; and with the following provisos: (a) that the urethane exotherm temperature does not greatly exceed the boiling point of the monomer or mixture of monomers employed as Component (C); (b) that the combined quantity of Components (C) and (F) be less than about 60% by weight based upon the combined weight of Components (A), (B), (C) and (F); (c) that when Component (G-1-c) or (G-1-d) is employed as the blowing agent, Component (G-2) is not required; (d) that when Component (F-3) is employed as the modifier component, it is employed in quantities of 20% by weight of the combined weight of Components (A), (B) and (F); (ii) pouring the admixed composition into a suitable mold wherein said composition expands and solidifies to a foam having the aforesaid density; and (III) subsequently demolding the resultant foamed article from the mold.

Claim 47

A process for preparing cellular polyurethane/vinyl polymer composite articles having substantially uniform cells, a density of less than 1 g/cc which process comprises: (I) admixing the components of a composition comprising (A) a liquid polyol free of nitrogen atoms and essentially free of ethylenic unsaturation or mixture of such polyols having from about 2 to about 8 hydroxyl groups and an average OH equivalent weight of at least about 30; (B) an organic polyisocyanate which is essentially free of ethylenic unsaturation or a mixture of such polyisocyanates having an NCO equivalent weight of less than about 300 with the proviso that when Component (A) has an average of about 2 hydroxyl groups per molecule, said polyisocyanate has an average of at least about 2.5 NCO groups per molecule; (C) from about 15% to less than about 75% by weight of the combined weight of Components (A), (B), (C), (D) and (E) of a polymerizable ethylenically unsaturated monomer having an atmospheric boiling point above about 70° C or a mixture of such monomers; (D) an effective quantity of a suitable catalyst of polymerizing Component (C); (e) an effective quantity of a suitable catalyst for urethane formation selected from compounds of the metals cobalt, copper and vanadium; and (F) from 0 to about 50% by weight based upon the combined weight of Components (A), (B), (C), (D), (E) and (F) of a modifier substance free from groups reactive with Components (A), (B) or (C) at the conditions employed herein, said modifier substances being selected from the group consisting of (1) liquid substances having an atmospheric boiling point of at least about 150° C; (2) solid substances having a surface area of less than about 0.8 m 2 /gram and a particle size such that said substance will pass through a 1/4-inch square opening, is substantially free of any absorbed or occluded water and will not decompose at a temperature below the maximum exotherm temperature generated by the urethane forming reaction; (3) polymers of one or more ethylenically unsaturated monomers, said polymers having (a) a molecular weight such that the polymer has a grease melt index as determined with a 0.02-inch orifice employing a total weight of 2160 grams at 80° C of from about 1 to about 250 grams/minute; (b) a solubility parameter of at least about 8; and (c) a specific heat of at least about 0.35 calories/gram/° C; and (4) mixtures thereof; and (G) a foam-forming system which comprises (1) a foaming agent selected from the group consisting of (a) low boiling vaporizable organic liquids having a boiling point below the reaction exotherm temperature; (b) substances which decompose thermally to release CO 2 or release water vapor to the exotherm temperature; (c) a solid particulate substance which will pass through a 2 mm square opening and which has a surface area of at least 0.8 m 2 /gram; (d) an inorganic metal hydrate characterized as having a solubility in anhydrous ethyl alcohol of less than about 1.2 grams per 100 grams and a weight loss of at least 5% when subjected to a temperature of 115° C for 30 minutes at atmospheric pressure; (e) water; (f) mixtures thereof; and (2) a cell control agent; and wherein Components (A) and (B) are present in quantities such that the NCO:OH equivalent ratio is from about 0.75:1 to about 1.5:1, Component (G-1) is present in quantities sufficient to provide the desired density and Component (G-2) is present in quantities sufficient to provide substantially uniform cells; and with the following provisos: (a) that the urethane exotherm temperature does not greatly exceed the boiling point of the monomer or mixture of monomers employed as Component (C); (b) that the combined quantity of Components (C) and (F) be less than about 60% by weight based upon the combined weight of Components (A), (B), (C) and (F); (c) that when Component (G-1-c) or (G-1-d) is employed as the blowing agent, Component (G-2) is not required; (d) that when Component (F-3) is employed as the modifier component, it is employed in quantities of 20% by weight of the combined weight of Components (A), (B) and (F); (ii) pouring the admixed composition into a suitable mold wherein said composition expands and solidifies to a foam having the aforesaid density; and (III) subsequently demolding the resultant foamed article from the mold.

Claim 48

The process of claim 43 wherein Components (A) and (B) are present in quantities such that the NCO:OH ratio is from about 0.9:1 to about 1.2:1 and the average OH equivalent weight of Component (A) is from about 30 to about 2500 and the equivalent weight of Component (B) is less than about 250 and wherein Component (C) is essentially free of groups reactive with Components (A) or (B), has an atmospheric boiling point above about 100° C and is present in quantities of from about 20% to about 60%.

Claim 49

The process of claim 44 wherein Component (A) has an equivalent weight of from about 50 to about 1000.

Claim 50

The process of claim 45 wherein Component (E) is a compound of cobalt, copper or mixtures thereof.

Claim 51

The process of claim 46 wherein Component (E) is an organic compound of cobalt.

Claim 52

The process of claim 47 wherein Component (E) is selected from the group consisting of cobalt naphthenate, CO II (dimethyl glyoxime) 2 , and cobalt acetate.4H 2 O.

Claim 53

The process of claim 46 wherein Component (E) is an inorganic compound of cobalt.

Claim 54

The process of claim 49 wherein Component (E) is selected from CoCl 2 .6H 2 O, Co(NO 3 ) 2 .6H 2 O and (Co III (NH 3 ) 4 CO 3 )NO 3 .

Claim 55

The process of claim 46 wherein Component (E) is a copper compound.

Claim 56

The process of claim 51 wherein Component (E) is copper naphthenate.

Claim 57

The process of claim 45 wherein Component (E) is V 2 O 5 , VCl 3 or VOCl 2 .

Claim 58

The process of claim 46 wherein Component (A) is an adduct of glycerine, trimethylolpropane, pentaerythritol, sucrose or mixtures thereof with propylene oxide, ethylene oxide or mixtures thereof.

Claim 59

The process of claim 54 wherein Component (A) is an adduct of glycerine with propylene oxide.

Claim 60

The process of claim 55 wherein Component (C) contains styrene.