Method for preparing thermoplastic polyurethane pellets

Patent metadata

Field	Value
Publication number	US-2017291981-A1
Application number	US-201515513883-A
Country	US
Kind code	A1
Filing date	Oct 7, 2015
Priority date	Oct 9, 2014
Publication date	Oct 12, 2017
Grant date	—

Abstract

The present invention relates to a method for manufacturing thermoplastic polyurethane pellets by means of reactive extrusion of: a long macrodiol with a molecular weight of 500 to 3000 g/mol; a diisocyanate; at least one chain extender comprising a dianhydrohexitol; and a polymerization catalyst. The invention also relates to the resulting thermoplastic polyurethane pellets.

First claim

1 . A method for manufacturing thermoplastic polyurethane pellets by reactive extrusion, comprising:
introducing, into an extruder, a macrodiol (a) of molar mass from 500 to 3000 g/mol, a diisocyanate (b), at least one chain extender (c) comprising a dianhydrohexitol and a polymerization catalyst (d), said compounds (a), (b), (c) and (d) being introduced into the extruder in liquid form; mixing the compounds (a), (b), (c) and (d) and polymerizing said mixture in the extruder; and extruding and cutting said polymerized mixture to form the thermoplastic polyurethane pellets.

2 . The method as claimed in claim 1 , wherein the ratio of the number of isocyanate functions to the number of hydroxyl functions is between 0.9 and 1.1, preferably between 0.95 and 1.05, more preferentially between 0.97 and 1.02 and even more preferentially equal to 1.

3 . The method as claimed in claim 1 , wherein the content by weight of rigid segments of the thermoplastic polyurethane is from 25% to 40%.

4 . The method as claimed in claim 1 , wherein the following are introduced into the extruder:
from 60% to 75% by weight of long macrodiol (a); from 20% to 35% by weight of diisocyanate (b); and from 2% to 10% by weight of chain extender (c).

5 . The method as claimed in claim 1 , wherein the macrodiol (a) is chosen from polyether glycols, polyester glycols, polycarbonate glycols or mixtures thereof; the macrodiol (a) is preferably a polyether glycol.

6 . The method as claimed in claim 1 , wherein the dianhydrohexitol (c) is isosorbide.

7 . The method as claimed in claim 1 , wherein the reagents (a), (b), (c) and (d) are introduced simultaneously at the extruder feed end.

8 . The method as claimed in claim 1 , wherein the step of mixing and polymerizing is carried out at a temperature of between 200° C. and 250° C.

9 . The method as claimed in claim 1 , further comprising a step of drying the thermoplastic polyurethane pellets.

10 . The method as claimed in claim 1 , wherein an inert gas purge is carried out on the molten isosorbide before it is introduced into the extruder; an inert gas purge is preferably carried out on each of the reagents in the melt state.

11 . A thermoplastic polyurethane pellet obtained by the method as defined in claim 1 .

Assignees

• Roquette Freres

Inventors

• Saint-Loup René
• Gimenez Jérôme
• Sautel Henri

Classifications

• C08G18/7671 Primary

  containing only one alkylene bisphenyl group · CPC title

• C08G18/4854

  Polyethers containing oxyalkylene groups having four carbon atoms in the alkylene group · CPC title

• B29K2075/00

  Use of {PU, i.e.} polyureas or polyurethanes {or derivatives thereof}, as moulding material · CPC title

• C08G18/4238

  derived from dicarboxylic acids and dialcohols · CPC title

• B29B9/06

  in the form of filamentary material, e.g. combined with extrusion · CPC title