Production of polyalkylene glycol ethers from formose and use thereof in the preparation of polyurethane resins

Claim 2

A process for the production of polyether polyols having an average molecular weight of from 200 to 10,000 and an average hydroxyl functionality of from 2.0 to 7.0, comprising reacting one or more cyclic ethers, optionally successively, with a starter comprising: (A) formose which is optionally α-aldolized; or (B) liquid mixtures of: (a) high molecular weight and/or low molecular weight polyhydroxyl compounds and/or mono- or di-saccharides and/or natural or synthetic invert sugars; and (b) formose which is optionally α-aldolized in the presence of an acid catalyst.

Claim 3

The process of claim 1 wherein from 20 to 80% by weight of solutions of crystalline mono- or di-saccharides and/or natural or synthetic invert sugars in formose are used as starter.

Claim 4

The process of claim 2 wherein from 30 to 70% by weight solutions of crystalline mono- or di-saccharides and/or natural or artificial invert sugars in formose are used as starter.

Claim 5

The process of claim 1 wherein the starter contains from 2 to 100% by weight based on the total starter mixture, of dihydric or polyhydric alcohols having a molecular weight of from 62 to 300 and/or polyether, polyester, polyacetal and/or polycarbonate polyols having a molecular weight of from 300 to 4000.

Claim 6

The process of claim 1 wherein formoses having a molecular weight of from 92 to 360 are used.

Claim 7

The process of claim 1 wherein formoses having a content of reducing compounds, expressed as glucose, of from 4 to 85% by weight are used.

Claim 8

The process of claim 1 wherein ethylene oxide and/or propylene oxide are used as cyclic ethers.

Claim 9

The process of claim 1 wherein an adduct of a carboxylic acid or carboxylic acid anhydride with boron trifluoride is used as the acid catalyst.

Claim 10

The process of claim 8, wherein the starter contains from 0.5 to 20% by weight of water.

Claim 11

The process of claim 1 wherein the starter contains from 0.5 to 4% by weight of water.

Claim 12

In a process for the production of optionally cellular polyurethane plastics by reacting: (a) polyisocyanates; with (b) relatively high molecular weight compounds containing isocyanate-reactive hydrogen atoms; and optionally, (c) chain-extenders; optionally in the presence of (d) blowing agents, catalysts and other known additives; the improvement which comprises using the polyether polyols as component (b) which are produced by a process comprising reacting one or more cyclic ethers, optionally successively, with a starter comprising: (A) formose which is optionally α-aldolized; or (B) liquid mixtures of: (a) high molecular weight and/or low molecular weight polyhydroxyl compounds and/or mono- or di-saccharides and/or natural or synthetic invert sugars; and (b) formose which is optionally α-aldolized in the presence of an acid catalyst.

Claim 13

In a process for the production of optionally cellular polyurethane plastics by reacting: (a) polyisocyanates; with (b) relatively high molecular weight compounds containing isocyanate-reactive hydrogen atoms; and optionally, (c) chain-extenders; optionally in the presence of (d) blowing agents, catalysts and other known additives; the improvement which comprises using the polyether polyols as component (b) which are produced by a process comprising reacting one or more cyclic ethers, optionally successively, with a starter comprising: (A) formose which is optionally α-aldolized; or (B) liquid mixtures of: (a) high molecular weight and/or low molecular weight polyhydroxyl compounds and/or mono- or di-saccharides and/or natural or synthetic invert sugars; and (b) formose which is optionally α-aldolized in the presence of an acid catalyst.