Melt spun thermoplastic polyurethanes useful as textile fibers
OwnerW. Kenneth Wilkinsoninventor
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Abstract
Melt spun thermoplastic polyurethane polymers useful as textile fibers and having good tenacity and recovery and substantially no gelation are disclosed. The polymers are prepared by a three-step polymerization process including: preparation of “hard” segment oligomer, preparation of “soft” segment oligomer and final reaction of “hard” segment with “soft” segment in a twin-screw reaction extruder to obtain a final polyurethane product having relatively uniform distances between the “hard” segments. The “soft” segment oligomer comprises blocks of polymeric glycol (poly) urethanes end capped with isocyanate groups. The “hard” segment oligomer comprises blocks of low molecular weight C2-C6 glycol (poly) urethanes.
Claims29
1) A melt spinnable composition useful in preparing textile fibers comprising a high molecular weight polyurethane polymer prepared from at least one diisocyanate monomer and at least two diol monomers, a first diol monomer of relatively high molecular weight and a second diol monomer of low molecular weight, said polyurethane having a molecular weight above about 200,000, a tenacity above about 0.6 gm/denier, and an elongation above about 400%, wherein said first and second diol monomers are always reacted separately during preparation of the polyurethane polymer.
10) A process of preparing a polyurethane polymer fiber precursor, the process comprising the steps of:
- a) obtaining a polyol prepolymer which is a member selected from the group consisting of hydroxyl terminated polyester glycols, hydroxyl terminated polyether/polyester glycols, and mixtures thereof;
- b) adding a first organic diisocyanate to the polyol prepolymer wherein the mole ratio of diisocyanate to prepolymer is about 1.2 to 1:1.1 to obtain a first mixture;
- c) reacting the first mixture of first organic diisocyanate and polyol prepolymer at a temperature of about 60° C. to about 100° C. and at atmospheric pressure for a time of about 20 minutes to about 100 minutes to obtain a first “soft” polymer having a viscosity of about 50-800 poises;
- d) obtaining a low molecular weight glycol having terminal hydroxyl groups;
- e) adding a second organic diisocyanate to the glycol wherein the mole ratio of isocyanate to hydroxyl is about 1.2 to about 1:1.2 to obtain a second mixture;
- f) reacting the second mixture of second organic diisocyanate and low molecular weight glycol at a temperature of about 50° C. to about 70° C. and at atmospheric pressure for a time of about 2 minutes to about 10 minutes to obtain a second “hard” polymer;
- g) combining the first “soft” polymer from (c) with the second “hard” polymer from (f) in an extruder to obtain a combination of polymers wherein the mole ratio of isocyanate functionality to hydroxyl functionality in the combination is about 0.98:1 to about 1.2:1;
- h) reacting the combination of polymers in the extruder under polymerization and high mixing conditions and at a temperature of about 125° C. to about 260° C. for a time of about 2 minutes to about 8 minutes and at atmospheric pressure to obtain a final polyurethane polymer;
- and
- j) extruding the final polyurethane polymer to obtain a solid product of polyurethane polymer fiber precursor.
20) A process for preparing a polyurethane polymer fiber precursor, the process comprising the steps of:
- (a) obtaining a polyol prepolymer which is a member selected from the group consisting of hydroxyl terminated polyester glycols, hydroxyl terminated polyether/polyester glycols, and mixtures thereof;
- (b) adding an organic diisocyanate to the polyol prepolymer wherein the mole ratio of isocyanate to hydroxyl is about 1:2 to about 1:1.1 to obtain a first mixture;
- (c) reacting a first mixture of organic diisocyanate and polyol prepolymer at a temperature of about 60° C. to about 100° C. and at atmospheric pressure for a time of about 20 minutes to about 100 minutes to obtain a first “soft” polymer and unreacted diisocyanate;
- (d) obtaining a low molecular weight glycol having terminal hydroxyl groups;
- (e) adding the first polymer and the unreacted diisocyanate from step (c) to the low molecular weight glycol in a reaction extruder to obtain a second mixture wherein the mole ratio of isocyanate group to hydroxyl group approaches 1.000;
- (f) reacting the second mixture of first “soft” polymer, unreacted diisocyanate and low molecular weight glycol in a reaction extruder under polymerization and high mixing conditions and at a temperature of about 125° C. to about 260° C. for a time of about 2 minutes to about 8 minutes and at atmospheric pressure to obtain a final polyurethane polymer;
- and
- (g) extruding the final polyurethane polymer to obtain a solid product of polyurethane polymer fiber precursor.
26) A spandex-like polyurethane polymer fiber having a minor amount of urea functionality prepared according to the process of 25.
Dependencies are inferred from the claim text.