Process for producing polyurethane polyacetal elastomers and the product so produced

Claim 2

A process for producing a polyurethane polyacetal elastomer comprising: (a) reacting a dihydroxy-terminated polyacetal homopolymer with an alkylene diisocyanate in the presence of a urethane-forming catalyst in a reaction to produce an isocyanate-terminated prepolymer, said homopolymer having a weight average molecular weight of between about 20,000 and about 50,000 as measured against a polystyrene standard by gel permeation chromatography and being produced by polymerizing-a 4-lower alkyl substituted-1,3-dioxolane, said reaction employing between about 55 mole percent and about 70 mole percent of said alkylene diisocyanate based upon the total amount of said alkylene diisocyanate and said homopolymer employed, and (b) reacting said isocyanate-terminated prepolymer with a dihydroxy-terminated polyacetal copolymer in the presence of a solvent and a urethane-forming catalyst to provide said elastomer, said copolymer having a weight average molecular weight of between about 100,000 and about 200,000 as measured against a polystyrene standard by gel permeation chromatography and being the reaction product of a formaldehyde-providing compound and 1,3-dioxolane, said copolymer being employed in an amount of between about 30 and about 50 mole percent based upon the total amount of said copolymer and said isocyanate-termninated prepolymer employed.

Claim 3

The process of claim 1 wherein said formaldehyde-providing compound is selected from the group consisting of trioxane, formaldehyde, para-formaldehyde and combinations thereof.

Claim 4

The process of claim 1 wherein said solvent is a halohydrocarbon.

Claim 5

The process of claim 3 wherein said halohydrocarbon is selected from the group consisting of tetrachloroethane, chloroform, trichloroethane, and mixtures thereof.

Claim 6

The process of claim 1 wherein the reaction of step (a) additionally employs a solvent.

Claim 7

The process of claim 5 wherein said solvent is a halohydrocarbon.

Claim 8

The process of claim 6 wherein said halohydrocarbon is selected from the group consisting of tetrachloroethane, chloroform, trichloroethane, and mixtures thereof.

Claim 9

The process of claim 1 wherein said urethane catalyst is dibutyltin dilaurate.

Claim 10

The process of claim 1 wherein said urethane catalyst is employed in an amount of between about 0.1 weight percent and about 5 weight percent, based on the total amount of said polyacetal homopolymer or polyacetal copolymer employed.

Claim 11

The process of claim 1 wherein the reactions of step (a) and step (b) are individually selected within a temperature range of between 25° C. and 90° C.

Claim 12

The process of claim 1 wherein said alkylene diisocyanate is hexamethylene diisocyanate.

Claim 13

The elastomer produced by the process of claim 1.

Claim 14

The elastomer produced by the process of claim 2.

Claim 15

The elastomer produced by the process of claim 3.

Claim 16

The elastomer produced by the process of claim 4.

Claim 17

The elastomer produced by the process of claim 5.

Claim 18

The elastomer produced by the process of claim 6.

Claim 19

The elastomer produced by the process of claim 7.

Claim 20

The elastomer produced by the process of claim 8.

Claim 21

The elastomer produced by the process of claim 9.

Claim 22

The elastomer produced by the process of claim 10.

Claim 23

The elastomer produced by the process of claim 11.

Claim 24

A process for producing a polyurethane polyacetal elastomer comprising: (a) reacting a dihydroxy-terminated polyacetal copolymer with an alkylene diisocyanate in the presence of a urethane-forming catalyst in a reaction to produce an isocyanate-terminated prepolymer, said copolymer having a weight average molecular weight of between about 100,000 and about 200,000 as measured against a polystyrene standard by gel permeation chromatography and being the reaction product of a formaldehyde-providing compound and 1,3-dioxolane, said reaction employing between about 55 mole percent and about 70 mole percent of said alkylene diisocyanate based upon the total amount of said alkylene diisocyanate and said copolymer employed, and (b) reacting said isocyanate-terminated prepolymer with a dihydroxy-terminated polyacetal homopolymer in the presence of a solvent and a urethane-forming catalyst to provide said elastomer, said homopolymer having a weight average molecular weight of between about 20,000 and about 50,000, as measured against a polystyrene standard by gel permeation chromatography and being produced by polymerizing a 4-lower alkyl substituted-1,3-dioxolane, said homopolymer being employed in an amount of between about 30 and about 50 mole percent based upon the total amount of said homopolymer and said isocyanate-terminated prepolymer employed.

Claim 25

A process for producing a polyurethane polyacetal elastomer comprising: (a) reacting a dihydroxy-terminated polyacetal copolymer with an alkylene diisocyanate in the presence of a urethane-forming catalyst in a reaction to produce an isocyanate-terminated prepolymer, said copolymer having a weight average molecular weight of between about 100,000 and about 200,000 as measured against a polystyrene standard by gel permeation chromatography and being the reaction product of a formaldehyde-providing compound and 1,3-dioxolane, said reaction employing between about 55 mole percent and about 70 mole percent of said alkylene diisocyanate based upon the total amount of said alkylene diisocyanate and said copolymer employed, and (b) reacting said isocyanate-terminated prepolymer with a dihydroxy-terminated polyacetal homopolymer in the presence of a solvent and a urethane-forming catalyst to provide said elastomer, said homopolymer having a weight average molecular weight of between about 20,000 and about 50,000, as measured against a polystyrene standard by gel permeation chromatography and being produced by polymerizing a 4-lower alkyl substituted-1,3-dioxolane, said homopolymer being employed in an amount of between about 30 and about 50 mole percent based upon the total amount of said homopolymer and said isocyanate-terminated prepolymer employed.

Claim 26

The elastomer produced by the process of claim 23.