Multistage process for producing thermoplastic polyurethane elastomers

Claim 2

A multistage process for the continuous production of thermoplastically processable polyurethane elastomers comprising: A) continuously mixing one or more substantially linear polyols having molecular weights of 500 to 5000 with a diisocyanate corresponding to the formula OCN--Z--NCO, in which Z is a difunctional organic radical, B) continuously reacting the mixture prepared in stage A) completely in a reactor at temperatures of from 100° C. to 250° C. to form a prepolymer, wherein stage A) and stage B) are carried out together in an intensively stirred tube reactor having length-to-diameter ratio of 4:1 to 15:1, C) continuously mixing the prepolymer prepared in stage B) with low molecular weight diol chain extenders and, optionally, triol and/or diamine chain extenders, said chain extenders having molecular weights of 62 to 500, wherein triol is present in an amount of up to 15 percent relative to the weight of said diol chain extender, the amounts of components being such that the total NCO:active H ratio for all the components used in stages A), B) and C) is from 0.9 to 1.2:1, D) applying the reaction mixture prepared in stage C) directly and continuously onto a conveyor belt, upon which said reaction mixture is allowed to react until it has solidified, and E) optionally, continuously melting the solidified reaction mixture prepared in stage D)in an extruder and with auxiliaries and/or other components being incorporated therein.

Claim 3

The process of claim 1, wherein i) said polyols are selected from the group consisting of polyester diols, polyether diols, polycarbonate diols and mixtures thereof, ii) said diisocyanate is selected from the group consisting of dicyclohexyl methane diisocyanate, isophorone diisocyanate, hexamethylene diisocyanate, naphthylene diisocyanate, 4,4-diphenylmethane diisocyanate, diphenylmethane diisocyanate isomer mixtures containing more than 96% by weight of 4,4'-diphenylmethane diisocyanate and mixtures thereof.

Claim 4

The process of claim 1, wherein a member selected from the group consisting of thermoplastics, reinforcing materials, plasticizers and mixtures thereof is introduced into the extruder as a further component in stage E.

Claim 5

Thermoplastically processable polyurethane elastomers produced by the process of claim 1.

Claim 6

A multistage process for the continuous production of thermoplastically processable polyurethane elastomers comprising: A) in a high-shear mixing unit, continuously mixing one or more substantially linear polyols having molecular weights of 500 to 5000 with a diisocyanate corresponding to the formula OCN--Z--NCO, in which Z is a difunctional organic radical, B) continuously reacting the mixture prepared in stage A) completely in a tube reactor having a length-to-diameter ratio of from 2:1 to 20:1 at temperatures of from 100° C. to 250° C. to form a prepolymer, C) in a high shear mixing unit, continuously mixing the prepolymer prepared in stage B) with low molecular weight diol chain extenders and, optionally, triol and/or diamine chain extenders, said chain extenders having molecular weights of 62 to 500, wherein triol is present in an amount of up to 15 percent relative to the weight of said diol chain extender, the amounts of components being such that the total NCO:active H ratio for all the components used in stages A), B) and C) is from 0.9:1 to 1.2:1, D) applying the reaction mixture prepared in stage C) directly and continuously onto a conveyor belt, and guiding said reaction mixture through a zone heated to a temperature of >110° C. until said reaction mixture has solidified, and E) optionally, continuously melting the solidified reaction mixture prepared in stage D) in an extruder and with auxiliaries and/or other components being incorporated therein.

Claim 7

A multistage process for the continuous production of thermoplastically processable polyurethane elastomers comprising: A) in a high-shear mixing unit, continuously mixing one or more substantially linear polyols having molecular weights of 500 to 5000 with a diisocyanate corresponding to the formula OCN--Z--NCO, in which Z is a difunctional organic radical, B) continuously reacting the mixture prepared in stage A) completely in a tube reactor having a length-to-diameter ratio of from 2:1 to 20:1 at temperatures of from 100° C. to 250° C. to form a prepolymer, C) in a high shear mixing unit, continuously mixing the prepolymer prepared in stage B) with low molecular weight diol chain extenders and, optionally, triol and/or diamine chain extenders, said chain extenders having molecular weights of 62 to 500, wherein triol is present in an amount of up to 15 percent relative to the weight of said diol chain extender, the amounts of components being such that the total NCO:active H ratio for all the components used in stages A), B) and C) is from 0.9:1 to 1.2:1, D) applying the reaction mixture prepared in stage C) directly and continuously onto a conveyor belt, and guiding said reaction mixture through a zone heated to a temperature of >110° C. until said reaction mixture has solidified, and E) optionally, continuously melting the solidified reaction mixture prepared in stage D) in an extruder and with auxiliaries and/or other components being incorporated therein.

Claim 8

The process of claim 5, wherein i) said polyols are selected from the group consisting of polyester diols, polyether diols, polycarbonate diols and mixtures thereof, ii) said diisocyanate is selected from the group consisting of dicyclohexyl methane diisocyanate, isophorone diisocyanate, hexamethylene diisocyanate, naphthylene diisocyanate, 4,4'-diphenylmethane diisocyanate, diphenylmethane diisocyanate isomer mixtures containing more than 96% by weight of 4,4'-diphenylmethane diisocyanate and mixtures thereof.