Process for the production of polyurethane products

Claim 2

The process for the production of polyurethane products by mixing and reacting the following components: A: 1 to 200 parts by weight of a lignin-cellulose polyepoxy resin which is produced by mixing and reacting 10 to 200 parts by weight of a polyfunctional epoxide compound and 50 parts by weight of broken-down alkali metal plant polymer; B: 50 to 100 parts by weight of a polyisocyanate or polyisothiocyanate.

Claim 3

The process of claim 1 wherein the polyfunctional epoxide compound is an epihalohydrin.

Claim 4

The process of claim 1 wherein the broken-down alkali metal plant polymer is produced by heating 1 to 3 parts by weight of alkali metal hydroxide with 2 parts by weight of plant particles while agitating at temperatures between 150° C. and 220° C. for 5 to 60 minutes.

Claim 5

The process of claim 1 wherein the polyisocyanate is selected from the group consisting of arylene polyisocyanates, alkylene polyisocyanates, phosgenation product of aniline-formaldehyde condensation and mixtures thereof.

Claim 6

The process of claim 1 wherein the polyisocyanate is selected from the group consisting of tolylene diisocyanate, phosgenation product of aniline-formaldehyde condensation and mixtures thereof.

Claim 7

The process of claim 1 wherein a polyol in the amount of up to 100 parts by weight is added with the lignin-cellulose polyepoxy resin.

Claim 8

The process of claim 1 wherein from up to 50% by weight, based on the reaction mixture, of a chemically inert blowing agent, boiling within the range of from -25° C. to 80° C., is added to the lignin-cellulose polyepoxy resin and/or polyisocyanate.

Claim 9

The process of claim 1 wherein up to 200 parts by weight of a curing agent are added with the lignin-cellulose polyepoxy resin and selected from the group consisting of water, water containing 10% to 70% by weight of an alkali metal silicate, water containing 20% to 70% by weight of silica sol, water containing 5% to 40% by weight of magnesium oxide in the form of a colloidal dispersion, alkali metal silicate selected from the group consisting of sodium silicate, potassium silicate and lithium silicate, water containing up to 70% hydraulic cement and mixtures thereof.

Claim 10

The process of claim 1 wherein up to 10 percent of a catalyst, percentage based on reactive mixture, selected from the group consisting of an amine, organic tin compound, silaamines, alkali metal alcoholates and mixtures thereof, is added with the lignin-cellulose polyepoxy resin.

Claim 11

The process of claim 1, wherein up to 20% by weight, based on the reaction mixture, of an emulsifying agent is added with the lignin-cellulose polyepoxy resin.

Claim 12

The process of claim 1, wherein up to 20% by weight, based on the reaction mixture, of a foam stabilizer is added with the lignin-cellulose polyepoxy resin.

Claim 13

The process of claim 1, wherein organic or inorganic particulate or pulverulent materials are added to the lignin-cellulose polyepoxy resin and/or polyisocyanate.

Claim 14

The product produced by the process of claim 1.

Claim 15

The product produced by the process of claim 5.

Claim 16

The process of claim 1 wherein up to 100 parts by weight of an organic compound, consisting of aldehyde, alkene halohydrin, phenol, mono-epoxy, amine, organic polyepoxy compound, organic polyhydroxy compound and mixtures thereof, are added with the broken-down alkali metal plant polymer when reacted with a polyfunctional epoxide compound to produce the lignin-cellulose polyepoxy resin.

Claim 17

The process of claim 15 wherein the aldehyde is selected from the group consisting of formaldehyde, acetoaldehyde, furfural, benzaldehyde, crotonaldehyde, acrolein, chloral, butylaldehyde and mixtures thereof.

Claim 18

The process of claim 15 wherein the alkene halohydrin has the general formula of: ##STR10## wherein R is an alkene.

Claim 19

The process of claim 15, wherein the phenol is selected from the group consisting of phenol, cresols, cresylic acid, creosote, xylenols, cashew nut shell liquid, anacordol, p-tert-butyl phenol, p-tert-amyl-phenol, phenolic acids produced from bark and mixtures thereof.

Claim 20

The process of claim 15 wherein the amine is a tertiary amine.

Claim 21

The process of claim 16 wherein the mono-epoxy compound is selected from the group consisting of ethylene oxide, propylene oxide, butylene oxide, tetrahydrofuran, styrene oxide and mixtures thereof, and is added at a pressure wherein the mono-epoxide compound is in a liquid state.

Claim 22

The process of claim 15 wherein the organic polyepoxy is a glycidyl polyether of 2,2'-bis(4-hydroxy phenyl) propane, containing at least 2 epoxy radicals per molecule.

Claim 23

The process of claim 1 wherein up to 50 parts by weight of a polyhydroxyl compound, selected from the group consisting of di(monohydroxy) alkanes, di(monohydroxyaryl) alkanes, resorcinol, hydroquinones glycols, glycerol, trimethylol propane, polyesters with 2 or more hydroxyl groups per molecule, polyamides with 2 or more hydroxyl groups per molecule and mixtures thereof, are added with the lignin-cellulose polyepoxy resin.

Claim 24

The product produced by the process of claim 15.

Claim 25

The process of claim 1 wherein the organic polyisocyanate is reacted with a polyol to produce a liquid isocyanate-terminated polyurethane prepolymer and the polyol is added, in the ratio of 1 to 50 mols, to 50 to 99 mols of the polyisocyanate, then reacted with the lignin-cellulose polyepoxy resin.

Claim 26

The product produced by the process of claim 24.

Claim 27

The process of claim 1 wherein up to 200 parts by weight of a water-binding agent are added with the lignin-cellulose epoxy resin and/or polyisocyanate and are selected from the group consisting of hydraulic cement, burnt lime, gypsum or synthetic anhydrites, thereby producing an inorganicorganic plastic product.

Claim 28

The product produced by the process of claim 26.

Claim 29

The process of claim 1 wherein up to 20%, percentage based on the reaction mixture, of a fire-retardant agent is added to the organic polyisocyanate and/or the lignin-cellulose polyepoxy resin.

Claim 30

The process of claim 1 wherein up to 50 parts by weight of an oxidated silicon compound, selected from the group consisting of hydrated silica, silicoformic acid, alkali metal silicates and mixtures thereof, are mixed with the polyisocyanate, then heated to between 30° C. and 40° C. while agitating for 10 to 30 minutes, thereby producing an isocyanate-terminated polyisocyanate silicate prepolymer, which is then mixed and allowed to react with the lignin-cellulose polyepoxy resin, thereby producing a polyurethane silicate product.

Claim 31

The product produced by the process of claim 28.

Claim 32

The process of claim 2 wherein the epihalohydrin is epichlorohydrin.