Process for the production of broken down cellulose copolymers

Claim 2

The process for the production of broken down cellulose copolymer by mixing and reacting the following components: Component (a) broken down alkali metal cellulose polymer produced by mixing 2 to 5 parts by weight of an alkali metal hydroxide selected from the group consisting of sodium hydroxide, potassium hydroxide and mixtures thereof with 3 parts by weight of a cellulose-containing plant particle then heating the mixture at 150° C. to 220° C. while agitating for 5 to 60 minutes Component (b) a substituted organic compound having at least two carbon atoms, each of which is attached to a substituent which will split off during the reaction, to said broken down alkali metal cellulose polymer in the amount wherein the mols of the substituted radicals are about equal to the mols of the alkali radicals in the mixture.

Claim 3

The process of claim 1 wherein the substituted organic compound is selected from the group consisting of, α,α' disubstituted ethyl ether; ββ' disubstituted ethyl ether; disubstituted methyl ether, disubstituted ethoxy ethyl ether; disubstituted thio ethyl ether; disubstituted 1,3 methoxy 2,2 dimethyl propane; disubstituted dipropyl formal; disubstituted diethyl formal; disubstituted para diethoxy benzene; disubstituted dimethoxy ethane; disubstituted diethyl carbonate; disubstituted glycol diacetate; pp' disubstituted diphenyl ether, disubstituted dibenzyl ether; disubstituted diethyl sulphone; αα' disubstituted propyl ether; para disubstituted benzene; disubstituted para Xylene; pp' disubstituted dibenzyl; disubstituted para hexyl propyl benzene; disubstituted 3-toyl propene-2; ethylene dichloride; ethylene dibromide; propylene dichloride; dihalides of unsaturated hydrocarbon gases derived from pressure-cracking processes and material gas-cracking processes and material gas-cracking processes; 1,1,2-trichloroethane; 1,2,4-trichlorobutane; trichloromesetylene, and mixtures thereof.

Claim 4

The process of claim 2 wherein the substituted organic compound contains at least two substituents, selected from the group consisting of acid sulfate, nitrate, acid phosphate, bicarbonate, formate acetate, propionate, laurate, oleate, stearate, oxalate, acid malonate, acid tartrate, acid citrate, halogens, and mixtures thereof.

Claim 5

The process of claim 1 wherein an emulsifying or dispersing agent selected from the group consisting of lignin sulfonates alkyl aryl sulfonates, aryl alkyl sulfonates, sorbitan monolaurates, alkyl aryl sulfates, methyl cellulose, sulfonated petroleum fractions, polymerized alkyl aryl sulfonates, polymerized aryl alkyl sulfonates, soybean lecithin and mixtures thereof in an aqueous solution is added to the unreacted mixture.

Claim 6

The process of claim 1 wherein lignin sulfonate in an aqueous solution is added to the unreacted mixture as an emulsifying or dispersing agent.

Claim 7

The process of claim 1 wherein the substituted organic compound is ethylene dichloride.

Claim 8

The product produced by the process of claim 1.

Claim 9

The process of claim 1 wherein an additional step is taken wherein a water soluble polysulfide in an aqueous solution is added with the broken down alkali metal cellulose polymer, thereby producing a polysulfide-broken down cellulose condensation product.

Claim 10

The product produced by the process of claim 8.

Claim 11

The process according to claim 8 wherein the water soluble polysulfide is selected from the group consisting of alkali metal polysulfide, alkaline earth metal polysulfide, ammonium polysulfide, polysulfides of ethanolamine, and mixtures thereof and added in the ratio of 1 to 20 parts by weight of the water soluble polysulfide to 10 parts by weight of the broken down alkali metal cellulose.

Claim 12

The process of claim 1 wherein an additional step is taken wherein a water soluble alkali-sulfur-silicate condensation product is added in an aqueous solution up to an amount equal to the broken down alkali metal cellulose polymer, with the broken down alkali metal cellulose polymer, thereby producing a polysulfide-silicate-broken-down cellulose condensation product.

Claim 13

The product produced by the process of claim 11.

Claim 14

The process of claim 11 wherein the water soluble alkali-sulfur-silicate condensation product is produced by mixing 2 parts by weight of an alkali metal hydroxide selected from the group consisting of sodium hydroxide and potassium hydroxide, 1 to 4 parts by weight of sulfur and 1 to 2 parts by weight of an oxidated silicon compound selected from the group consisting of silica, alkali metal silicate, alkaline earth metal silicates, natural oxidated silicon compounds containing free silicic acid and/or oxide groups and mixtures thereof, then heating the mixture to just above the melting temperature of sulfur while agitating for 10 to 30 minutes thereby producing an alkali-sulfur-silicate condensation product.

Claim 15

The process of claim 1 wherein the broken down alkali metal cellulose polymer is first added to a solvent selected from the group consisting of water, methanol, ethanol, isopropyl alcohol, ethylene glycol, propylene glycol, glycerol, furfuryl alcohol, polyester polymer with 2 or more hydroxyl groups, sucrose amine polymer with 2 or more hydroxyl groups, polyether polymers with 2 or more hydroxyl groups and mixtures thereof.

Claim 16

The process of claim 1 wherein the broken down alkali metal cellulose polymer is first reacted with an aldehyde selected from the group consisting of formaldehyde, acetaldehyde, propionic aldehyde, furfural, crotonaldehyde, acrolein, butyl aldehyde, paraformaldehyde, pentanals, hexanals, heptanals and mixtures thereof in the ratio of 1 to 5 parts by weight of the aldehyde to 2 parts by weight of the broken down alkali metal cellulose polymer and then reacted with the substituted organic compound thereby producing an aldehyde broken down cellulose organic copolymer.

Claim 17

The product produced by the process of claim 15.

Claim 18

The process of claim 1 wherein an additional step is taken where in 1 to 95 parts by weight of the broken down cellulose copolymer and 50 parts by weight of a polyisocyanate or a polyisothiocyanate are mixed and reacted to produce a polyurethane product.

Claim 19

The process of claim 17 wherein the polyisocyanate is selected from the group consisting of aliphatic, cycloaliphatic, araliphatic, aromatic and hetrocyclic polyisocyanates and mixtures thereof.

Claim 20

The process of claim 17 wherein the polyisocyanate is a phosgenation product of aniline- formaldehyde condensation.

Claim 21

The process of claim 17 wherein the polyisocyanate is accompanied by foaming.

Claim 22

The product produced by the process of claim 17.

Claim 23

The process of claim 1 wherein an additional step is taken wherein 1 to 95 parts by weight of the broken down cellulose copolymer, 1 to 95 parts by weight of a polyol, 50 parts by weight of an organic polyisocyanate, up to 20% by weight of a foam stabilizer, up to 50% by weight of a chemically-inert blowing agent, boiling within the range of from -25° C. to 80° C., up to 10% by weight of an activator, up to 50% by weight of a curing agent, and up to 200 parts by weight of a water-binding agent, percentages based on the weight of the reactants, are mixed and allowed to react, thereby producing a polyurethane foam.

Claim 24

The process of claim 22 wherein the organic polyisocyanate is selected from the group consisting of tolylene diisocyanate, phosgenation product of aniline-formaldehyde condensation and mixtures thereof.

Claim 25

The process of claim 22 wherein the polyol is selected from the group consisting of polyether glycols, polyhydric alcohols, castor oil, and polyesters, polyamides, polyacetals and polycarbonates which contain 2 or more hydroxyl groups per molecule and mixtures thereof.

Claim 26

The product produced by the process of claim 22.

Claim 27

The process of claim 22 wherein the water-binding agent is selected from the group consisting of hydraulic cement, synthetic anhydride, gypsum and burnt lime.

Claim 28

The process of claim 1 wherein an additional step is taken wherein 1 to 95 parts by weight of the broken down cellulose copolymer, up to 20% by weight of a foam stabilizer, up to 20% by weight of a curing agent, up to 50% by weight of a chemically-inert blowing agent, boiling within the range of from -25° C. to 80° C., up to 10% by weight of an activator, percentage based on the weight of the reactants, and 50 parts by weight of an isocyanate-terminated polyurethane prepolymer are mixed and allowed to react, thereby producing a polyurethane resinous product.

Claim 29

The process of claim 27 wherein the isocyanate-terminated polyurethane prepolymer is selected from the group consisting of an isocyanate-terminated polyester, isocyanate-termined polyether, isocyanate-terminated polybutadiene, isocyanate-terminated polysulfide and mixtures thereof.

Claim 30

The process of claim 27 wherein the process is accompanied by foaming.

Claim 31

The product produced by the process of claim 27.