Low density carbonized composite foams

Claim 2

A process for preparing a carbonized polystyrene based low density foam which comprises: (A) preparing an inverse emulsion of a styrene monomer in water; (B) polymerizing said styrene monomer to produce a foam; (C) filling said foam with an aqueous resorcinol-formaldehyde solution whereby said resorcinol-formaldehyde solution occupies the cells of said foam; (D) curing said resorcinol-formaldehyde solution to form a gel; and (E) heating said resorcinol-formaldehyde gel filled polystyrene foam to a temperature sufficient to carbonize said foam.

Claim 3

The process of claim 1 wherein said resorcinol-formaldehyde solution is prepared by mixing resorcinol and formaldehyde in about a 1:2 molar ratio in the presence of sodium carbonate.

Claim 4

The process of claim 2 wherein the ratio of resorcinol to sodium carbonate by weight ranges from 35 to 300, and said sodium carbonate is present in an amount sufficient to provide an aqueous solution having a pH ranging from about 6 to about 7.

Claim 5

The process of claim 1 wherein said styrene monomer is polymerized in step (B) by heating said emulsion to a temperature of about 50° C.

Claim 6

The process of claim 1 wherein said resorcinol-formaldehyde solution is cured in step (D) at a temperature of about 90° C.

Claim 7

The process of claim 1 wherein said resorcinol-formaldehyde gel filled polystyrene foam is heated to a temperature of at least about 1050° C., for a period of time sufficient to carbonize it.

Claim 8

The process of claim 1 wherein said inverse emulsion of a styrene monomer in water is prepared by intimately mixing an oil phase of styrene, divinylbenzene and an oil soluble surfactant, with an aqueous phase of sodium persulfate in water, wherein the aqueous phase comprises from about 92 to about 95 percent of the total emulsion.

Claim 9

A process for preparing a carbonized polymer based low density foam which comprises: (A) preparing an inverse emulsion of a foam forming monomer selected from the group consisting of styrene monomers and alkyl acrylate monomers in water; (B) polymerizing said monomer to produce a foam; (C) filling said foam with a high-carbon-yield foam forming prepolymer selected from the group consisting of phenol aldehyde, acrylonitrile, furfuryl alcohol, and vinyl alcohol whereby said prepolymer occupies the cells of said foam; (D) curing said prepolymer to form a polymer; and (E) heating said polymer filled foam to a temperature sufficient to carbonize said foam.

Claim 10

A process for preparing a carbonized polymer based low density foam which comprises: (A) preparing an inverse emulsion of a foam forming monomer selected from the group consisting of styrene monomers and alkyl acrylate monomers in water; (B) polymerizing said monomer to produce a foam; (C) filling said foam with a high-carbon-yield foam forming prepolymer selected from the group consisting of phenol aldehyde, acrylonitrile, furfuryl alcohol, and vinyl alcohol whereby said prepolymer occupies the cells of said foam; (D) curing said prepolymer to form a polymer; and (E) heating said polymer filled foam to a temperature sufficient to carbonize said foam.

Claim 11

The process of claim 8 wherein said high-carbon-yield foam forming prepolymer is a resorcinol-formaldehyde solution prepared by mixing resorcinol and formaldehyde in about a 1:2 molar ratio in the presence of sodium carbonate.

Claim 12

The process of claim 8 wherein said high-carbon-yield prepolymer is selected from the group consisting of acrylonitrile, furfuryl alcohol, and vinyl alcohol.

Claim 13

The process of claim 1 which includes the further step of supercritically drying said foam after step (D) and prior to step (E).

Claim 14

The process of claim 11 wherein said supercritical drying comprises replacing entrapped water in the foam with an organic solvent, replacing the organic solvent with liquid carbon dioxide, then heating the foam under pressure to a temperature sufficient to vaporize the liquid carbon dioxide.

Claim 15

The process of claim 8 which includes the further step of supercritically drying said foam after step (D) and prior to step (E).

Claim 16

The process of claim 13 wherein said supercritical drying comprises replacing entrapped water in the foam with an organic solvent, replacing the organic solvent with liquid carbon dioxide, then heating the foam under pressure to a temperature sufficient to vaporize the liquid carbon dioxide.

Claim 17

The process of claim 8 wherein said foam forming monomer is selected from the group consisting of styrene, butylstyrene, butyl methacrylate and ethyl methacrylate.

Claim 18

The process of claim 8 wherein said high-carbon-yield prepolymer is a phenol aldehyde.

Claim 19

The process of claim 16 wherein said phenol is selected from the group consisting of resorcinol, monohydric phenols, polyhydric phenols, pyrocatechol, hydroquinone and alkyl substituted phenols and said aldehyde is selected from the group consisting of formaldehyde, meta-aldehyde, para-aldehyde, acetaldehyde and benzaldehyde.