Polyurethane foams and elastomers based on modified polyether polyols

Claim 2

A process for the preparation of modified polyether polyols comprising polymerizing of from 1 to 50 parts by weight of a mixture of 20 to 100% by weight (based on the total quantity of monomers) of acrylonitrile and 0 to 80% by weight of styrene in 50 to 99 parts by weight of the polyether polyol in the presence of a polymerization initiator which yields radicals, wherein said polymerization is carried out in the presence of from 0.1 to 1.5% by weight, based on the total quantity of monomers put into the process, of a compound of the formula: A=CH--X--R wherein A represents a divalent group ##STR8## R represents a C 1-18 alkyl, C 1-10 cycloalkyl, or substituted or unsubstituted benzyl group, R' represents C 1-8 alkyl group, n represents 0, 1 or 2 and X represents oxygen or sulfur.

Claim 3

The process of claim 1, wherein the temperature during said polymerization is in the range of 100° C. to 140° C.

Claim 4

The process of claim 1, wherein N=0 or 1, R represents a methyl group and R' represents a C 1 -C 6 alkyl group, a benzyl group or a cyclohexyl group.

Claim 5

The process of claim 1, wherein 10 to 40 parts by weight of the monomer mixture is used.

Claim 6

The process of claim 1, wherein 40 to 80% by weight of the total monomer mixture is acrylonitrile.

Claim 7

The process of claim 1, wherein 20 to 60% by weight of the total monomer mixture is styrene.

Claim 8

The process of claim 1, wherein 50 to 99 parts by weight of said polyether polyol is used.

Claim 9

The process of claim 1, wherein R is a C 1-8 alkyl, cyclohexyl, cyclohexylmethyl or benzyl group.

Claim 10

The process of claim 1, wherein R' is a methyl group.

Claim 11

The process of claim 1, wherein said compound of the formula: A=CH--X--R is present in a quantity of 0.5 to 1.2% by weight based on the total quantity of monomers used.

Claim 12

The process of claim 1, wherein said polymerization initiator is selected from the group consisting of organic peroxides, percarboxylic acid esters, and aliphatic azo compounds and is used in a quantity of from 0.3 to 2% by weight based on the total quantity of monomer.

Claim 13

The process of claim 1, wherein said compound of the formula A=CH--X--R is ##STR9##

Claim 14

The process of claim 1, wherein said compound of the formula A=CH--X--R is ##STR10##

Claim 15

The product of claim 1.

Claim 16

In a process for the preparation of a cellular or non-cellular polyurethane resin comprising reacting (A) a polyisocyanate with (B) a polyether polyol modified by graft polymerization and optionally (C) other higher molecular and/or low molecular compounds containing isocyanate reactive hydrogen atoms, optionally in the presence of (D) blowing agents, catalysts and other known additives, the improvement comprising employing a modified polyether polyol prepared by a process comprising polymerizing from 1 to 50 parts by weight of a mixture of 20 to 100% by weight (based on the total quantity of monomers) of acrylonitrile and 0 to 80% by weight of styrene in 50 to 99 parts by weight of the polyether polyol in the presence of a polymerization initiator which yields free radicals, wherein said polymerization is carried out in the presence of from 0.1 to 1.5% by weight, based on the total quantity of monomers put into the process, of a compound of the formula: A=CH--X--R wherein A represents a divalent group ##STR11## R represents a C 1-18 alkyl, C 1-10 cycloalkyl, or substituted or unsubstituted benzyl group, R' represents C 1-8 alkyl group, n represents 0, 1 or 2 and X represents oxygen or sulfur.

Claim 17

In a process for the preparation of a cellular or non-cellular polyurethane resin comprising reacting (A) a polyisocyanate with (B) a polyether polyol modified by graft polymerization and optionally (C) other higher molecular and/or low molecular compounds containing isocyanate reactive hydrogen atoms, optionally in the presence of (D) blowing agents, catalysts and other known additives, the improvement comprising employing a modified polyether polyol prepared by a process comprising polymerizing from 1 to 50 parts by weight of a mixture of 20 to 100% by weight (based on the total quantity of monomers) of acrylonitrile and 0 to 80% by weight of styrene in 50 to 99 parts by weight of the polyether polyol in the presence of a polymerization initiator which yields free radicals, wherein said polymerization is carried out in the presence of from 0.1 to 1.5% by weight, based on the total quantity of monomers put into the process, of a compound of the formula: A=CH--X--R wherein A represents a divalent group ##STR11## R represents a C 1-18 alkyl, C 1-10 cycloalkyl, or substituted or unsubstituted benzyl group, R' represents C 1-8 alkyl group, n represents 0, 1 or 2 and X represents oxygen or sulfur.