Open cell rigid thermoset foams and method

Claim 3

The method according to claim 1 in which: the cells are macroscopic.

Claim 4

The method according to claim 1 in which: the foam during the reexpanding is expanded to its original size and thickness.

Claim 5

The method according to claim 1 including: impregnating the foam with a finally divided filler material after it is reexpanded and before it is finally cured.

Claim 6

A method according to claim 4 in which: the filler is selected from the group consisting of silica, carbon black, magnesia, titanium dioxide, aluminum powder, aluminum silicate, lead silicate, bentonites, clay, lithipone, asbestos, vermiculite, graphite, and mixtures thereof.

Claim 7

The method according to claim 1 including: impregnating the foam with a finally divided filler material to substantially fill the open cells by immersing the foam in a liquid dispersion of the filler material.

Claim 8

A method according to claim 6 in which: the filler is selected from the group consisting of silica, carbon black, magnesia, titanium dioxide, aluminum powder, aluminum silicate, lead silicate, bentonites, clay, lithipone, asbestos, vermiculite, graphite, and mixtures thereof.

Claim 9

The method according to claim 1 in which the foam is formed by: admixing a B-stageable polymerizable thermosetting resin selected from the group consisting of a curable polyepoxide resin, a polyurethane formed from a polyester resin and an isocyanate compound, a polyurethane formed from a polyether resin and an isocyanate compound, and mixtures thereof; and a foaming agent for said resin in an amount sufficient to foam the same; curing the resin to said B-staged state of partial cure by heating the mixture to temperatures in the range of 50 degrees F. to 180 degrees F.; maintaining said temperatures for a time sufficient to foam the mixture and achieve said partial cure to produce a closed-cell structure; said softening of the partially cured foam structure being accomplished by heating the same until it can be indented with a finger; after said crushing, reexpanding the structure by heating the same until the structure is expanded; and accomplishing said final cure by heating the foam material.

Claim 10

The method according to claim 1 or 8 in which: the foam structure is compressed to approximately one-half of its original thickness to produce an open-celled foam structure; the temperature for reexpanding the crushed foam is in the range of 150 degrees F. to 250 degrees F. and is maintained for a period in the range of 10 to 30 minutes.

Claim 11

The invention according to claim 9 in which: after final cure, impregnating the resultant open-celled structure by soaking the same in a dispersion of a finally divided filler material in a liquid carrier; and removing the soaked and impregnated product, and draining the excess dispersion, and drying.

Claim 12

The method according to claim 8 in which the polyurethane is formed from a polyether resin and an isocyanate compound by mixing: a polymerizable polyether resin having a hydroxyl number greater than 400 and selected from the group consisting of polyethers formed by direct polymerization of oxides of normally gaseous aliphatic hydrocarbons, condensation of oxides of normally gaseous aliphatic hydrocarbons with an aliphatic polyalcohol having from 3 to 8 carbons in the molecule and 2 to 5 hydroxyl groups, and mixtures thereof; water; and an isocyanate having at least 2--NCO groups and copolymerizable with polyether and reactable with water to form carbon dioxide gas.

Claim 13

The method according to claim 8 in which the polyurethane is formed from a polyether resin and an isocyanate by admixing: a polymerizable polyether resin having a hydroxyl number in the range of 580 to 610 and selected from the group consisting of polyethers formed by a direct polymerization of oxides of normally gaseous aliphatic hydrocarbons, condensation of oxides of normally gaseous aliphatic hydrocarbons with an aliphatic polyalcohol having from 3 to 8 carbon atoms in the molecule and 2 to 5 hydroxyl groups, and mixtures thereof; a polyamide condensation product of polymerizable linoleic acid condensed with a polyamide having an amine value in the range of 290 to 320 in an amount in the range of 1 to 2 parts by weight; water in an amount in the range of 11/2 to 4 parts by weight; and toluene diisocyanate in an amount in the range of 160 to 170 parts by weight, each per 100 parts by weight of said polyether resin.

Claim 14

The method according to claim 8 in which the polyurethane is formed from a polyether resin and an isocyanate by admixing: a polymerizable polyether resin having a hydroxyl number in the range of 580 to 610, a hydroxyl equivalent weight in the range of 97 to 92, and selected from the group consisting of polyethers formed by a direct polymerization of oxides of normally gaseous aliphatic hydrocarbons, condensation of oxides of normally gaseous aliphatic hydrocarbons with an aliphatic polyalcohol having from 3 to 8 carbon atoms in the molecule and 2 to 5 hydroxyl groups, and mixtures thereof; a polyamide condensation product of polymerized linoleic acid condensed with a polyamide having an amine value in the range of 290 to 320 in an amount in the range of 1 to 2 parts by weight; water in an amount in the range of 11/2 to 4 parts by weight; and toluene diisocyanate in an amount in the range of 160 to 170 parts by weight, each per 100 parts by weight of said polyether resin.

Claim 15

The method according to claim 8 in which a polyurethane is formed from a polyester resin and an isocyanate by admixing: a polymerizable polyester resin produced by condensing a polycarboxylic acid with a polyhydric alcohol, having a hydroxyl number in the range of from 350 to 500, and a molecular weight in the range of 500 to 1500; water; and an organic isocyanate having at least 2--NCO groups and copolymerizable with said polyester and reactable with said water to form carbon dioxide.

Claim 16

The method according to claim 8 in which the polyurethane is formed from the polyester resin and isocyanate by admixing: a polymerizable polyester resin produced by condensing a polycarboxylic acid with a polyhydric alcohol, having a hydroxyl number in the range of from 350 to 500, and a molecular weight in the range of 500 to 1500; a polyamide condensation product of linoleic acid condensed with a polyamine having an amine value in the range of 290 to 320 in an amount in the range of from 0.5 to 2 parts by weight; water in an amount in the range of 3 to 4 parts by weight; and polymethylene-polyphenylisocyanate in an amount in the range of from 160 to 170 parts by weight, each per 100 parts by weight of said polyester resin.

Claim 17

The method according to claim 15 in which the polyurethane foam is formed from a polyester resin: the closed-cell foam structure is softened by heating at a temperature in the range of 250 degrees F. to 300 degrees F. for a period in the range of 10 to 20 minutes; the closed-cells of the softened foam are crushed to be opened by compressing the foam to approximately one-half of its original thickness; the partially cured open-celled foam is reexpanded to its original size by heating at a temperature in the range of 250 degrees F. to 300 degrees F. for an interval in the range of 10 to 30 minutes; and the foam is finally cured by heating at a temperature in the range of 250 degrees F. to 260 degrees F. for an interval of from 50 to 70 minutes per each inch of thickness of the foam.

Claim 18

The method according to claim 16 in which the finally cured product is impregnated with a filler by: soaking the open-celled foam in a dispersion produced by mixing toluene, phenolic spar varnish in an amount in the range of 17 to 20 parts by weight of carbon black in an amount in the range of 3 to 4 parts by weight, and calcium titanite in an amount in the range of 1.5 to 2 parts by weight, each per 100 parts by weight of said toluene; allowing the excess toluene to drain from the foamed product; and drying the resultant cured impregnated open-celled foam material by heating the same at a temperature in the range of 140 degrees F. to 160 degrees F. until dry.

Claim 19

The method according to claim 14 in which the polyurethane foam is made from a polyether resin: the partially cured closed-cell foam structure is softened by heating to a temperature in the range of 250 degrees F. to 300 degrees F. for an interval in the range of 10 to 20 minutes; the closed cells of the softened partially cured foam are crushed by compressing the foam to approximately one-half of its original thickness to open the cells; the open-celled foam is reexpanded by heating at a temperature in the range of 250 degrees F. to 350 degrees F. for an interval in the range of 10 to 30 minutes to restore the foam to its original thickness; soaking the open-cell foam to impregnate the same in a dispersion of a mixture of toluene, phenolic spar varnish in an amount in the range of 17 to 20 parts by weight, of carbon black in an amount in the range of 3 to 4 parts by weight, and calcium titanite in an amount in the range of 0.5 to 2 parts by weight, each per 100 parts by weight of said toluene, whereby the open cells of the foam are impregnated with the carbon black and titanite; allowing the excess toluene to drain from the foam product; and drying the resultant cured impregnated open-celled polyurethane foam by heating the same at a temperature in the range of 140 degrees F. to 160 degrees F. until dry.

Claim 22

A method according to claim 19 including: soaking the open-celled foam in a dispersion produced by mixing a liquid carrier, and a finally divided filler in an amount in the range of 3 to 20 parts by weight, per 100 parts by weight of the carrier, whereby the foam cells are impregnated with the filler; removing the impregnated foam from the dispersion; allowing excess liquid carrier to drain from the foam; and drying and curing the resultant impregnated open-celled foam by heating.

Claim 25

4' diamino diphenyl methane in an amount in the range of 23 to 27 parts by weight; a blowing agent mixture of a polyepoxide having a ##STR7## equivalency in the range of 175 to 210, and N,N' dimethyl N,N' dinitrosoterephthamide in an amount of 1 part by weight per 3 parts by weight of said polyepoxide, said blowing agent mixture being present in an amount in the range of 23 to 27 parts by weight; a plasticizer comprising a liquid mixture of polysulfide polymers produced by condensing an alkaline polysulfide with a dihalide in an amount in the range of 9 to 11 parts by weight; and triethylene tetramine in an amount in the range of 2 to 3 parts by weight, each per 100 parts by weight of modified polyepoxide; gelled the resulting mixture in a mold by maintaining the same at a temperature in the range of 50 degrees F. to 90 degrees F. for a period in the range of 8 to 16 hours; force foaming and partially curing the resultant gelled product by heating the same to a temperature in the range of 110 degrees F. to 130 degrees F. for an interval in the range of 3 to 5 hours; heating the mixture at a temperature in the range of 140 degrees F. to 160 degrees F. for an interval in the range of 3 to 5 hours; and subsequently heating the mixture to a temperature in the range of 190 degrees F. to 210 degrees F. for a period in the range of 50 to 70 minutes for each inch of thickness of the resulting closed-cell product; softening the product to a temperature in the range of 195 degrees F. to 205 degrees F.; compressing the closed-cell product to approximately one-half the original expanded thickness to cause the walls forming the closed cells to rupture to produce an open-celled product; reexpanding the open-celled foam material by heating to a temperature in the range of 210 degrees F. to 215 degrees F. and maintaining the temperature for an interval in the range of 10 to 30 minutes.

Claim 26

4' diamino diphenyl methane in an amount in the range of 23 to 27 parts by weight; a blowing agent mixture of a polyepoxide having a ##STR7## equivalency in the range of 175 to 210, and N,N' dimethyl N,N' dinitrosoterephthamide in an amount of 1 part by weight per 3 parts by weight of said polyepoxide, said blowing agent mixture being present in an amount in the range of 23 to 27 parts by weight; a plasticizer comprising a liquid mixture of polysulfide polymers produced by condensing an alkaline polysulfide with a dihalide in an amount in the range of 9 to 11 parts by weight; and triethylene tetramine in an amount in the range of 2 to 3 parts by weight, each per 100 parts by weight of modified polyepoxide; gelled the resulting mixture in a mold by maintaining the same at a temperature in the range of 50 degrees F. to 90 degrees F. for a period in the range of 8 to 16 hours; force foaming and partially curing the resultant gelled product by heating the same to a temperature in the range of 110 degrees F. to 130 degrees F. for an interval in the range of 3 to 5 hours; heating the mixture at a temperature in the range of 140 degrees F. to 160 degrees F. for an interval in the range of 3 to 5 hours; and subsequently heating the mixture to a temperature in the range of 190 degrees F. to 210 degrees F. for a period in the range of 50 to 70 minutes for each inch of thickness of the resulting closed-cell product; softening the product to a temperature in the range of 195 degrees F. to 205 degrees F.; compressing the closed-cell product to approximately one-half the original expanded thickness to cause the walls forming the closed cells to rupture to produce an open-celled product; reexpanding the open-celled foam material by heating to a temperature in the range of 210 degrees F. to 215 degrees F. and maintaining the temperature for an interval in the range of 10 to 30 minutes.

Claim 27

A method according to claim 21 including: soaking the open-celled foam in a dispersion produced by mixing toluene, phenolic spar varnish in an amount in the range of 17 to 20 parts by weight, carbon black in an amount in the range of 3 to 4 parts by weight, and calcium titanite an amount in the range of 1.5 to 2 parts by weight, each per 100 parts by weight of said toluene, whereby the foam is impregnated with carbon black and calcium titanite; removing the resulting open-celled foam product from the dispersion; allowing excess toluene to drain from the foam product; and drying and curing the resultant impregnated open-celled foam by heating at a temperature in the range of 140 degrees F. to 160 degrees F. until dried.

Claim 28

A method according to claim 21 including: finally curing the reexpanded foam by heating to a temperature in the range of 240 degrees F. to 270 degrees F. for a period of from 50 to 70 minutes per inch of thickness of the product.

Claim 29

A method according to claim 23 including impregnating the finally cured open-celled foam: soaking the open-celled foam in a dispersion produced by mixing toluene, phenolic spar varnish in an amount in the range of 17 to 20 parts by weight, carbon black in an amount in the range of 3 to 4 parts by weight, and calcium titanite in an amount in the range of 1.5 to 2 parts by weight, each per 100 parts by weight of said toluene; allowing the excess toluene to dry from the foam product; and drying the resultant cured impregnated open-celled foam material by heating at a temperature in the range of 140 degrees F. to 160 degrees F. until dry.

Claim 30

A rigid porous, deformation resisting, non-resilient inflexible, thermoset resin foam having macroscopic open cells formed by: admixing a B-stagable polymerizable thermosetting resin mixture selected from the group consisting of a curable polyepoxide resin, a polyurethane formed from a polyester resin and an isocynate compound, a polyurethane formed from a polyether resin and an isocynate compound, and mixtures thereof, and a forming agent for the resin mixture in an amount sufficient to foam the same; B-staging the resulting curable mixture by heating to a temperature in the range of 50 degrees F. to 180 degrees F. and maintaining the temperature for a time sufficient to foam the mixture and partially cure the same to produce a partially cured closed-cell foam material; softening the resulting partially cured foam material by heating until it can be indented with a finger; compressing and crushing the softened closed-cell foam to approximately one-half its original thickness to cause the walls forming the cells to rupture to produce an open-celled foam; reexpanding the opened-celled foam by heating until the structure is expanded.

Claim 31

A rigid porous, deformation resisting, non-resilient inflexible, thermoset resin foam having macroscopic open cells formed by: admixing a B-stagable polymerizable thermosetting resin mixture selected from the group consisting of a curable polyepoxide resin, a polyurethane formed from a polyester resin and an isocynate compound, a polyurethane formed from a polyether resin and an isocynate compound, and mixtures thereof, and a forming agent for the resin mixture in an amount sufficient to foam the same; B-staging the resulting curable mixture by heating to a temperature in the range of 50 degrees F. to 180 degrees F. and maintaining the temperature for a time sufficient to foam the mixture and partially cure the same to produce a partially cured closed-cell foam material; softening the resulting partially cured foam material by heating until it can be indented with a finger; compressing and crushing the softened closed-cell foam to approximately one-half its original thickness to cause the walls forming the cells to rupture to produce an open-celled foam; reexpanding the opened-celled foam by heating until the structure is expanded.

Claim 32

A rigid foam according to claim 25 in which: the open-celled foam by is finally cured by heating to a temperature in the range of 150 degress F. to 250 degrees F. and maintaining the temperature for the necessary length of time to achieve a final cure.

Claim 33

A rigid foam according to claim 25 in which the foam is impregnated by: soaking the same in a dispersion of a filler material in a liquid carrier; removing the soaked and impregnated product; draining the excess dispersion; and drying.

Claim 34

A rigid form according to claim 27 in which: the filler is selected from the group consisting of silica, carbon black, magnesia, titanium dioxide, aluminum powder, aluminum silicate, lead silicate, bentonites, clay, lithipone, asbestos, vermiculite, graphite, and mixtures thereof.

Claim 35

A rigid foam according to claim 27 in which: the impregnated open-celled foam is finally cured by heating to a temperature in the range of 150 degrees F. to 250 degrees F. and maintaining the temperature for the necessary length of time to achieve a final cure.

Claim 36

A rigid foam according to claim 25 in which polyurethane is formed from a polyether resin and an isocyanate compound by mixing: a polymerizable polyether resin having a hydroxyl number greater than 400 and selected from the group consisting of polyethers formed by direct polymerization of oxides of normally gaseous aliphatic hydrocarbons, condensation of oxides of normally gaseous aliphatic hydrocarbons with an aliphatic polyalcohol having from 3 to 8 carbons in the molecule and 2 to 5 hydroxyl groups, and mixtures thereof; water; and an isocyanate having at least 2--NCO groups and copolymerizable with polyether and reactable with water to form carbon dioxide gas.

Claim 37

A rigid foam according to claim 25 in which the polyurethane is formed from a polyether resin and an isocyanate by admixing: a polymerizable polyether resin having a hydroxyl number in the range of 580 to 610 and selected from the group consisting of polyethers formed by a direct polymerization of oxides of normally gaseous aliphatic hydrocarbons, condensation of oxides of normally gaseous aliphatic hydrocarbons with an aliphatic polyalcohol having from 3 to 8 carbon atoms in the molecule and 2 to 5 hydroxyl groups, and mixtures thereof; a polyamide condensation product of polymerizable linoleic acid condensed with a polyamide having an amine value in the range of 290 to 320 in an amount in the range of 1 to 2 parts by weight; water in an amount in the range of 11/2 to 4 parts by weight; and toluene diisocyanate in an amount in the range of 160 to 170 parts by weight, each per 100 parts by weight of said polyether resin.

Claim 38

A rigid foam according to claim 25 in which the polyurethane is formd from a polyether resin and an isocyanate by admixing: a polymerizable polyether resin having a hydroxyl number in the range of 580 to 610, a hydroxyl equivalent weight in the range of 97 to 92, and selected from the group consisting of polyethers formed by a direct polymerization of oxides of normally gaseous aliphatic hydrocarbons, condensation of oxides of normally gaseous aliphatic hydrocarbons with an aliphatic polyalcohol having from 3 to 8 carbon atoms in the molecule and 2 to 5 hydroxyl groups, and mixtures thereof; a polyamide condensation product of polymerized linoleic acid condensed with a polyamide having an amine value in the range of 290 to 320 in an amount in the range of 1 to 2 parts by weight; water in an amount in the range of 11/2 to 4 parts by weight; and toluene diisocyanate in an amount in the range of 160 to 170 parts by weight, each per 100 parts by weight of said polyether resin.

Claim 39

A rigid foam according to claim 25 in which a polyurethane is formed from a polyester resin and an isocyanate by admixing: a polymerizable polyester resin produced by condensing a polycarboxylic acid with a polyhydric alcohol, having a hydroxyl number in the range of from 350 to 500, and a molecular weight in the range of 500 to 1500; water; and an organic isocyanate having at least 2--NCO groups and copolymerizable with said polyester and reactable with said water to form carbon dioxide.

Claim 40

A rigid foam according to claim 25 in which the polyurethane is formed from the polyester resin and isocyanate by admixing: a polymerizable polyester resin produced by condensing a polycarboxylic acid with a polyhydric alcohol, having a hydroxyl number in the range of from 350 to 500, and a molecular weight in the range of 500 to 1500; a polyamide condensation product of linoleic acid condensed with a polyamine having an amine value in the range of 290 to 320 in an amount in the range of from 0.5 to 2 parts by weight; water in an amount in the range of 3 to 4 parts by weight; and polymethylene-polyphenylisocyanate in an amount in the range of from 160 to 170 parts by weight, each per 100 parts by weight of said polyester resin.

Claim 41

A rigid foam according to claim 34 in which the polyurethane foam is formed from a polyester resin: the closed-cell foam structure is softened by heating at a temperature in the range of 250 degrees F. to 300 degrees F. for a period in the range of 10 to 20 minutes; the partially cured open-celled foam is reexpanded to its original size by heating at a temperature in the range of 250 degrees F. to 300 degrees F. for an interval in the range of 10 to 30 minutes; and the foam is finally cured by heating at a temperature in the range of 250 degrees F. to 260 degrees F. for an interval of from 50 to 70 minutes per each inch of thickness of the foam.

Claim 42

A rigid foam according to claim 35 in which the finally cured product is impregnated with a filler by: soaking the open-celled foam in a dispersion produced by mixing toluene, phenolic spar varnish in an amount in the range of 17 to 20 parts by weight of carbon black in an amount in the range of 3 to 4 parts by weight, and calcium titanite in an amount in the range of 1.5 to 2 parts by weight, each per 100 parts by weight of said toluene; allowing the excess toluene to drain from the foamed product; and drying the resultant cured impregnated open-celled foam material by heating the same at a temperature in the range of 140 degrees F. to 160 degrees F. until dry.

Claim 43

A rigid foam according to claim 33 in which the polyurethane foam is made from a polyether resin: the partially cured closed-cell foam structure is softened by heating to a temperature in the range of 250 degrees F. to 300 degrees F. for an interval in the range of 10 to 20 minutes; the closed cells of the softened partially cured foam are crushed by compressing the foam to approximately one-half of its original thickness to open the cells; the open-celled foam is reexpanded by heating at a temperature in the range of 250 degrees F. to 350 degrees F. for an interval in the range of 10 to 30 minutes to restore the foam to its original thickness; soaking the open-cell foam to impregnate the same in a dispersion of a mixture of toluene, phenolic spar varnish in an amount in the range of 17 to 20 parts by weight, of carbon black in an amount in the range of 3 to 4 parts by weight, and calcium titanite in an amount in the range of 0.5 to 2 parts by weight, each per 100 parts by weight of said toluene, whereby the open cells of the foam are impregnated with the carbon black and titanite; allowing the excess toluene to drain from the foam product; and drying the resultant cured impregnated open-celled polyurethane foam by heating the same at a temperature in the range of 140 degrees F. to 160 degrees F. until dry.

Claim 44

A rigid porous, deformation resisting, non-resilient inflexible, thermoset resin foam having macroscopic open cells formed by, admixing a modified polyepoxide produced by reacting a polyepoxide having a ##STR8## equivalency greater than one with a curing and hardening agent therefor, said curing and hardening agent being present in a relatively small amount and less than the amount sufficient to harden and cure the polyepoxide, a curing and hardening agent for epoxies in an amount sufficient to harden and completely cure the modified polyepoxide, and a decomposable blowing agent in an amount sufficient to foam the modified polyepoxide; gelling the resultant mixture by maintaining the same at a temperature in the range of 45 degrees F. to 130 degrees F. for an interval in the range of 6 to 24 hours; force foaming and partially curing the gelled product by heating to a temperature in the range of 90 degrees F. to 150 degrees F. to an interval in the range of 2 to 6 hours to form a closed-cell foam; softening the foam by heating at a temperature in the range of 150 degrees F. to 250 degrees F.; compressing and crushing the softened foam to open the cells; and reexpanding the crushed open-celled foam by heating to a temperature in the range of 150 degrees F. to 250 degrees F.

Claim 45

A rigid porous, deformation resisting, non-resilient inflexible, thermoset resin foam having macroscopic open cells formed by, admixing a modified polyepoxide produced by reacting a polyepoxide having a ##STR8## equivalency greater than one with a curing and hardening agent therefor, said curing and hardening agent being present in a relatively small amount and less than the amount sufficient to harden and cure the polyepoxide, a curing and hardening agent for epoxies in an amount sufficient to harden and completely cure the modified polyepoxide, and a decomposable blowing agent in an amount sufficient to foam the modified polyepoxide; gelling the resultant mixture by maintaining the same at a temperature in the range of 45 degrees F. to 130 degrees F. for an interval in the range of 6 to 24 hours; force foaming and partially curing the gelled product by heating to a temperature in the range of 90 degrees F. to 150 degrees F. to an interval in the range of 2 to 6 hours to form a closed-cell foam; softening the foam by heating at a temperature in the range of 150 degrees F. to 250 degrees F.; compressing and crushing the softened foam to open the cells; and reexpanding the crushed open-celled foam by heating to a temperature in the range of 150 degrees F. to 250 degrees F.

Claim 46

A rigid foam according to claim 38 including: soaking the open-celled foam in a dispersion produced by mixing a liquid carrier, and a filler in an amount in the range of 3 to 20 parts by weight, per 100 parts by weight of the carrier, whereby the foam cells are impregnated with the filler; removing the impregnated foam from the dispersion; allowing excess liquid carrier to drain from the foam; and drying and curing the resultant impregnated open-celled foam by heating.

Claim 47

A rigid porous deformation resisting, non-resilient, inflexible, rigid plastic thermoset resin foam structure having macroscopic open cells formed by, admixing a modified polyepoxide produced by reacting a polyepoxide having a ##STR9## equivalency in the range of 175 to 210 produced by reacting bisphenol A and epichlorohydrin, a polyamide curing and hardening agent for polyepoxides produced by condensing a polybasic carboxylic acid having from 1 to 26 carbon atoms in the molecule with a polyamine formed from a polymerizable amine having from 2 to 26 carbon atoms in the molecule in an amount from 0.2 to 2 parts by weight per 100 parts by weight of said polyepoxide; said reacting being carried on at a temperature in the range of 180 degrees F. to 220 degrees F. for a period of from 1/2 to 11/2 hours; ligroine in an amount in the range of 7 to 9 parts by weight;

Claim 48

A rigid porous deformation resisting, non-resilient, inflexible, rigid plastic thermoset resin foam structure having macroscopic open cells formed by, admixing a modified polyepoxide produced by reacting a polyepoxide having a ##STR9## equivalency in the range of 175 to 210 produced by reacting bisphenol A and epichlorohydrin, a polyamide curing and hardening agent for polyepoxides produced by condensing a polybasic carboxylic acid having from 1 to 26 carbon atoms in the molecule with a polyamine formed from a polymerizable amine having from 2 to 26 carbon atoms in the molecule in an amount from 0.2 to 2 parts by weight per 100 parts by weight of said polyepoxide; said reacting being carried on at a temperature in the range of 180 degrees F. to 220 degrees F. for a period of from 1/2 to 11/2 hours; ligroine in an amount in the range of 7 to 9 parts by weight;

Claim 49

4' diamino diphenyl methane in an amount in the range of 23 to 27 parts by weight; a blowing agent mixture of a polyepoxide having a ##STR10## equivalency in the range of 175 to 210, and N,N' dimethyl N,N' dinitrosoterephthamide in an amount of 1 part by weight per 3 parts by weight of said polyepoxide, said blowing agent mixture being present in an amount in the range of 23 to 27 parts by weight; a plasticizer comprising a liquid mixture of polysulfide polymers produced by condensing an alkaline polysulfide with a dihalide in an amount in the range of 9 to 11 parts by weight; and triethylene tetramine in an amount in the range of 2 to 3 parts by weight, each per 100 parts by weight of modified polyepoxide; gelling the resulting mixture in a mold by maintaining the same at a temperature in the range of 50 degrees F. to 90 degrees F. for a period in the range of 8 to 16 hours. force foaming and partially curing the resultant gelled product by heating the same to a temperature in the range of 110 degrees F. to 130 degrees F. for an interval in the range of 3 to 5 hours; heating the mixture at a temperature in the range of 140 degrees F. to 160 degrees F. for an interval in the range of 3 to 5 hours; and subsequently heating the mixture to a temperature in the range of 190 degrees F. to 210 degrees F. for a period in the range of 50 to 70 minutes for each inch of thickness of the resulting closed-cell product; softening the product to a temperature in the range of 195 degrees F. to 205 degrees F.; compressing the closed-cell product to approximately one-half the original expanded thickness to cause the walls forming the closed cells to rupture to produce an open-celled product; reexpanding the open-celled foam material by heating to a temperature in the range of 210 degrees F. to 215 degrees F. and maintaining the temperature for an interval in the range of 10 to 30 minutes.

Claim 50

4' diamino diphenyl methane in an amount in the range of 23 to 27 parts by weight; a blowing agent mixture of a polyepoxide having a ##STR10## equivalency in the range of 175 to 210, and N,N' dimethyl N,N' dinitrosoterephthamide in an amount of 1 part by weight per 3 parts by weight of said polyepoxide, said blowing agent mixture being present in an amount in the range of 23 to 27 parts by weight; a plasticizer comprising a liquid mixture of polysulfide polymers produced by condensing an alkaline polysulfide with a dihalide in an amount in the range of 9 to 11 parts by weight; and triethylene tetramine in an amount in the range of 2 to 3 parts by weight, each per 100 parts by weight of modified polyepoxide; gelling the resulting mixture in a mold by maintaining the same at a temperature in the range of 50 degrees F. to 90 degrees F. for a period in the range of 8 to 16 hours. force foaming and partially curing the resultant gelled product by heating the same to a temperature in the range of 110 degrees F. to 130 degrees F. for an interval in the range of 3 to 5 hours; heating the mixture at a temperature in the range of 140 degrees F. to 160 degrees F. for an interval in the range of 3 to 5 hours; and subsequently heating the mixture to a temperature in the range of 190 degrees F. to 210 degrees F. for a period in the range of 50 to 70 minutes for each inch of thickness of the resulting closed-cell product; softening the product to a temperature in the range of 195 degrees F. to 205 degrees F.; compressing the closed-cell product to approximately one-half the original expanded thickness to cause the walls forming the closed cells to rupture to produce an open-celled product; reexpanding the open-celled foam material by heating to a temperature in the range of 210 degrees F. to 215 degrees F. and maintaining the temperature for an interval in the range of 10 to 30 minutes.

Claim 51

A rigid foam according to claim 40 including: soaking the open-celled foam in a dispersion produced by mixing toluene, phenolic spar varnish in an amount in the range of 17 to 20 parts by weight, carbon black an amount in the range of 3 to 4 parts by weight, and calcium titanite an amount in the range of 1.5 to 2 parts by weight, each per 100 parts by weight of said toluene, whereby the foam is impregnated with carbon black and calcium titanite; removing the resulting open-celled foam product from the dispersion; allowing excess toluene to drain from the foam product; and drying and curing the resultant impregnated open-celled foam by heating at a temperature in the range of 140 degrees F. to 160 degrees F. until dried.

Claim 52

A rigid foam according to claim 41 including: finally curing the reexpanded foam by heating to a temperature in the range of 240 degrees F. to 270 degrees F. for a period of from 50 to 70 minutes per inch of thickness of the product.

Claim 53

A rigid foam according to claim 42 including impregnating the finally cured open-celled foam: soaking the open-celled foam in a dispersion produced by mixing toluene, phenolic spar varnish in an amount in the range of 17 to 20 parts by weight, carbon black in an amount in the range of 3 to 4 parts by weight, and calcium titanite in an amount in the range of 1.5 to 2 parts by weight, each per 100 parts by weight of said toluene; allowing the excess toluene to dry from the foam product; and drying the resultant cured impregnated open-celled foam material by heating at a temperature in the range of 140 degrees F. to 160 degrees F. until dry.

Claim 56

4' diamino diphenyl methane in an amount in the range of 23 to 27 parts by weight; a decomposable activated blowing agent adapted to produce N 2 , CO 2 , and NH 3 (trace) gases, said blowing agent mixture being present in an amount in the range of 23 to 27 parts by weight; a plasticizer comprising a liquid mixture of polysulfide polymers produced by condensing an alkaline polysulfide with a dihalide in an amount in the range of 9 to 11 parts by weight; and triethylene tetramine in an amount in the range of 2 to 3 parts by weight, each per 100 parts by weight of modified polyepoxide; gelling the resulting mixture in a mold by maintaining the same at a temperature in the range of 50 degrees F. to 90 degrees F. for a period in the range of 8 to 16 hours; force foaming and partially curing the resultant gelled produced by heating the same to a temperature in the range of 110 degrees F. to 130 degrees F. for an interval in the range of 3 to 6 hours; heating the mixture at a temperature in the range of 140 degrees F. to 160 degrees F. for an interval in the range of 2 to 5 hours; and subsequently heating the mixture to a temperature in the range of 190 degrees F. to 210 degrees F. for a period in the range of 50 to 70 minutes for each inch of thickness of the resulting closed-cell product; softening the product at a temperature in the range of 280 degrees F. to 300 degrees F.; compressing the closed-cell product to approximately one-half the original expanded thickness to cause the walls forming the closed cells to rupture to produce an open-celled product; reexpanding the open-celled foam material to its original thickness by heating to a temperature in the range of 280 degrees F. to 300 degrees F. and maintaining the temperature for an interval in the range of 10 to 30 minutes.

Claim 57

4' diamino diphenyl methane in an amount in the range of 23 to 27 parts by weight; a decomposable activated blowing agent adapted to produce N 2 , CO 2 , and NH 3 (trace) gases, said blowing agent mixture being present in an amount in the range of 23 to 27 parts by weight; a plasticizer comprising a liquid mixture of polysulfide polymers produced by condensing an alkaline polysulfide with a dihalide in an amount in the range of 9 to 11 parts by weight; and triethylene tetramine in an amount in the range of 2 to 3 parts by weight, each per 100 parts by weight of modified polyepoxide; gelling the resulting mixture in a mold by maintaining the same at a temperature in the range of 50 degrees F. to 90 degrees F. for a period in the range of 8 to 16 hours; force foaming and partially curing the resultant gelled produced by heating the same to a temperature in the range of 110 degrees F. to 130 degrees F. for an interval in the range of 3 to 6 hours; heating the mixture at a temperature in the range of 140 degrees F. to 160 degrees F. for an interval in the range of 2 to 5 hours; and subsequently heating the mixture to a temperature in the range of 190 degrees F. to 210 degrees F. for a period in the range of 50 to 70 minutes for each inch of thickness of the resulting closed-cell product; softening the product at a temperature in the range of 280 degrees F. to 300 degrees F.; compressing the closed-cell product to approximately one-half the original expanded thickness to cause the walls forming the closed cells to rupture to produce an open-celled product; reexpanding the open-celled foam material to its original thickness by heating to a temperature in the range of 280 degrees F. to 300 degrees F. and maintaining the temperature for an interval in the range of 10 to 30 minutes.

Claim 58

A method according to claim 40 including: soaking the open-celled foam in a dispersion produced by mixing toluene, phenolic spar varnish in an amount in the range of 17 to 20 parts by weight, carbon black in an amount in the range of 3 to 4 parts by weight, and calcium titanite an amount in the range of 1.5 to 2 parts by weight, each per 100 parts by weight of said toluene, whereby the foam is impregnated with carbon black and calcium titanite; removing the resulting open-celled foam product from the dispersion; allowing excess toluene to drain from the foam product; and drying and curing the resultant impregnated open-celled foam by heating at a temperature in the range of 140 degrees F. to 160 degrees F. until dried.

Claim 59

A method according to claim 44 including: finally curing the reexpanded foam by heating to a temperature in the range of 280 degrees F. to 300 degrees F. for a period of from 50 to 70 minutes per inch of thickness of the product.

Claim 60

A method according to claim 46 including impregnating the finally cured open-celled foam: soaking the open-celled foam in a dispersion produced by mixing toluene, phenolic spar varnish in an amount in the range of 17 to 20 parts by weight, carbon black in an amount in the range of 3 to 4 parts by weight, and calcium titanite in an amount in the range of 1.5 to 2 parts by weight, each per 100 parts by weight of said toluene; allowing the excess toluene to dry from the foam product; and drying the resultant cured impregnated open-celled foam material by heating at a temperature in the range of 140 degrees F. to 160 degrees F. until dry.

Claim 61

A rigid porous deformation resisting, non-resilient, inflexible, rigid plastic thermoset resin foam structure having macroscopic open cells formed by, admixing a modified polyepoxide produced by reacting a polyepoxide having a ##STR12## equivalency in the range of 175 to 210 produced by reacting bisphenol A and epichlorohydrin, a polyamide curing and hardening agent for polyepoxides produced by condensing a polybasic carboxylic acid having from 1 to 26 carbon atoms in the molecule with a polyamine formed from a polymerizable amine having from 2 to 26 carbon atoms in the molecule in an amount from 0.2 to 2 parts by weight per 100 parts by weight of said polyepoxide; said reacting being carried on at a temperature in the range of 180 degrees F. to 220 degrees F. for a period of from 1/2 to 11/2 hours; ligroine in an amount in the range of 7 to 9 parts by weight;

Claim 62

A rigid porous deformation resisting, non-resilient, inflexible, rigid plastic thermoset resin foam structure having macroscopic open cells formed by, admixing a modified polyepoxide produced by reacting a polyepoxide having a ##STR12## equivalency in the range of 175 to 210 produced by reacting bisphenol A and epichlorohydrin, a polyamide curing and hardening agent for polyepoxides produced by condensing a polybasic carboxylic acid having from 1 to 26 carbon atoms in the molecule with a polyamine formed from a polymerizable amine having from 2 to 26 carbon atoms in the molecule in an amount from 0.2 to 2 parts by weight per 100 parts by weight of said polyepoxide; said reacting being carried on at a temperature in the range of 180 degrees F. to 220 degrees F. for a period of from 1/2 to 11/2 hours; ligroine in an amount in the range of 7 to 9 parts by weight;

Claim 63

4' diamino diphenyl methane in an amount in the range of 23 to 27 parts by weight; a decomposable activated blowing agent adapted to produce N 2 , CO 2 , and NH 3 (trace) gases, said blowing agent mixture being present in an amount in the range of 23 to 27 parts by weight; a plasticizer comprising a liquid mixture of polysulfide polymers produced by condensing an alkaline polysulfide with a dihalide in an amount in the range of 9 to 11 parts by weight; and triethylene tetramine in an amount in the range of 2 to 3 parts by weight, each per 100 parts by weight of modified polyepoxide; gelling the resulting mixture in a mold by maintaining the same at a temperature in the range of 50 degrees F. to 90 degrees F. for a period in the range of 8 to 16 hours; force foaming and partially curing the resultant gelled product by heating the same to a temperature in the range of 110 degrees F. to 130 degrees F. for an interval in the range of 3 to 6 hours; heating the mixture at a temperature in the range of 140 degrees F. to 160 degrees F. for an interval in the range of 2 to 5 hours; and subsequently heating the mixture to a temperature in the range of 190 degrees F. to 210 degrees F. for a period in the range of 50 to 70 minutes for each inch of thickness of the resulting closed-cell product; softening the product to a temperature in the range of 280 degrees F. to 300 degrees F.; compressing the closed-cell product to approximately one-half the original expanded thickness to cause the walls forming the closed cells to rupture to produce an open-celled product; reexpanding the open-celled foam material to its original thickness by heating to a temperature in the range of 280 degrees F. to 300 degrees F. and maintaining the temperature for an interval in the range of 10 to 30 minutes.

Claim 64

4' diamino diphenyl methane in an amount in the range of 23 to 27 parts by weight; a decomposable activated blowing agent adapted to produce N 2 , CO 2 , and NH 3 (trace) gases, said blowing agent mixture being present in an amount in the range of 23 to 27 parts by weight; a plasticizer comprising a liquid mixture of polysulfide polymers produced by condensing an alkaline polysulfide with a dihalide in an amount in the range of 9 to 11 parts by weight; and triethylene tetramine in an amount in the range of 2 to 3 parts by weight, each per 100 parts by weight of modified polyepoxide; gelling the resulting mixture in a mold by maintaining the same at a temperature in the range of 50 degrees F. to 90 degrees F. for a period in the range of 8 to 16 hours; force foaming and partially curing the resultant gelled product by heating the same to a temperature in the range of 110 degrees F. to 130 degrees F. for an interval in the range of 3 to 6 hours; heating the mixture at a temperature in the range of 140 degrees F. to 160 degrees F. for an interval in the range of 2 to 5 hours; and subsequently heating the mixture to a temperature in the range of 190 degrees F. to 210 degrees F. for a period in the range of 50 to 70 minutes for each inch of thickness of the resulting closed-cell product; softening the product to a temperature in the range of 280 degrees F. to 300 degrees F.; compressing the closed-cell product to approximately one-half the original expanded thickness to cause the walls forming the closed cells to rupture to produce an open-celled product; reexpanding the open-celled foam material to its original thickness by heating to a temperature in the range of 280 degrees F. to 300 degrees F. and maintaining the temperature for an interval in the range of 10 to 30 minutes.