| PATENT NUMBER | This data is not available for free |
| PATENT GRANT DATE | May 8, 1984 |
| PATENT TITLE | Polyurethane |
| PATENT ABSTRACT | A polyurethane comprises (a) organic diisocyanate units and (b) polycaprolactone polyol units having a narrow molecular weight distribution in which a ratio of the weight average molecular weight to the number average molecular weight is in the range of from 1.1 to 2.0 and the average molecular weight is 500 to 5,000, the units (a) and (b) being connected linearly through urethane linkages |
| PATENT INVENTORS | This data is not available for free |
| PATENT ASSIGNEE | This data is not available for free |
| PATENT FILE DATE | February 23, 1982 |
| PATENT FOREIGN APPLICATION PRIORITY DATA | This data is not available for free |
| PATENT CLAIMS |
The embodiments of the invention of which an exclusive privilege and property is claimed are defined as follows: 1. A process for the preparation of polyurethanes which comprises reacting an organic diisocyanate with a polycaprolactone polyol having a narrow molecular weight distribution in which the ratio of the weight average molecular weight to the number average molecular weight is in the range of from 1.1 to 2.0 and the average molecular weight is 500 to 5,000, said polycaprolactone polyol having been prepared by subjecting a lactone to ring-opening polymerization in the presence of 0.1 to 50 ppm of stannous halide selected from the group consisting of stannous chloride, stannous bromide and stannous iodide, as a catalyst, and at a temperature of from 100.degree. to 230.degree. C. 2. A process claimed in claim 1 in which said lactone is epsilon-caprolactone. 3. A polyurethane prepared by the process of claim 1. -------------------------------------------------------------------------------- |
| PATENT DESCRIPTION |
The present invention relates to a lactone polymer, especially a lactone polymer having a narrow molecular weight distribution, and a process for the preparation thereof. Moreover, the invention relates to a polyurethane and a process for the preparation thereof. More particularly, the invention relates to a polyurethane which is excellent in the elastic recovery and has a very good operation adaptability because of a low viscosity thereof and a process for the preparation thereof. The polyurethane is obtained from diisocyanate and the before mentioned lactone polymer. The lactone polymer having a molecular weight of 500 to 5,000 is very valuable as a starting material to be used for manufacture of polyurethanes, paints and the like. Conventional lactone polymers having a molecular weight of 500 to 5,000, however, have a broad molecular weight distribution and the ratio of the weight average molecular weight to the number average molecular weight is in the range of from 2.5 to 3.5. When such polymers are actually used, various problems are caused by this broad molecular weight distribution. We made researches on molecular weight distributions of conventional lactone polymers by gel permeation chromatography (hereinafter referred to as "GPC"), and found that if the molecular weight distribution is appropriately adjusted, lactone polymers giving practically very excellent characteristics can be obtained. We have now completed the present invention based on this finding. More specifically, in accordance with the present invention, there are provided a lactone polymer having a narrow molecular weight distribution, which is characterized in that the ratio of the weight average molecular weight to the number average molecular weight is in the range of from 1.1 to 2.0 and the molecular weight is 500 to 5,000, and a process for the preparation of such lactone polymer. By the term "lactone polymer" used in the present invention is meant a polymer obtained by subjecting .epsilon.-caprolactone to ring-opening polymerization in the presence of an initiator containing an active hydrogen atom. As the initiator, there can be used polyhydric alcohols such as diols and triols and polyvalent amines. As the diol, there can be mentioned ethylene glycol, propylene glycol, diethylene glycol, 1,4-butylene glycol, 1,6-hexane diol and neopentyl glycol. As the triol, there can be listed glycerin and trimethylol-propane. Other polyhydric alcohols include pentaerythritol, acrylic polyols, styrene/allyl alcohol copolymers and polymeric resins having hydroxyl groups such as polyester-polyols, epoxy resins, polyether polyols and cellulose derivatives. The polyvalent amine include ethylene diamine, diethylene triamine and ethanol amine. Moreover aromatic polyamines may be used here. By the term "molecular weight" used in the present invention is meant a value calculated from the hydroxyl value of the lactone polymer according to the following formula: ##EQU1## The hydroxyl value is determined according to the method of JIS K-1557 6.4. In the above formula, N represents the number of functional groups of the initiator. The molecular weight of the lactone polymer of the present invention is 500 to 5,000. As is apparent from the foregoing description, the amount of the polymerization initiator necessary for obtaining a predetermined molecular weight can be defined according to the above calculation formula. The ratio of the weight-average molecular weight Mw to the number-average molecular weight Mn, that is, the molecular weight distribution, is determined by GPC. Apparatus: Model LC-3A manufactured by Shimazu Seisakusho Solvent: tetrahydrofuran, 1 ml/min Temperature: room temperature Columns: HSG-PRE (one), HSG-20 (one), HSG-15 (three) and HSG-10 (one) (each being supplied by Shimazu Seisakusho) Detector: Shodex RI SE-11 (supplied by Showa Denko) The ratio of the weight average molecular weight to the number average molecular weight is in the range of from 1.1 to 2.0. The process for the preparation of the polymer of the present invention will now be described. In the preparation process according to the present invention, a stannous halide such as stannous chloride, stannous bromide or stannous iodide is used as a catalyst. The amount used of the catalyst is 0.1 to 50 ppm based on the total weight of .epsilon.-caprolactone. If the amount used of the catalyst is smaller than 0.1 ppm, polymerization is not advanced, and if the amount used of the catalyst is larger than 50 ppm, it becomes difficult to obtain a polymer having a narrow molecular weight. The reaction temperature is ordinarily 100.degree. to 230.degree. C. and preferably 120.degree. to 190.degree. C. Since a known catalyst, TBT (tetrabutyl titanate), contributes not only to ring-opening polymerization but also to ester exchange reaction, use of this catalyst results in production of a polymer having a broad molecular weight distribution. The lactone polymer of the present invention has a narrower molecular weight distribution than the conventional lactone polymer and also has a lower viscosity and a slightly lower melting point than those of the conventional polymer. Since the molecular distribution of the lactone polymer of the present invention is narrow, it is very valuable as a starting material to be used for manufacture of urethane elastomers, urethane adhesives, urethane paints and polyurethanes. For example, when the polymer of the present invention is used in the field of spandex fibers, there can be provided products excellent in the elastic recovery characteristics. Furthermore, there can be provided a high-solid paint as a polyol component of a two-pack type urethane paint. Polyurethanes having a linear structure have heretofore been synthesized by reacting a polyol having hydroxyl groups on both the molecule ends, an organic diisocyanate and a chain extender having a relatively low molecular weight such as a diol or diamine. As the polyol having hydroxyl groups on both the molecule ends, there are used polyester type polyols and polyether type polyols. As the polyester type polyol, there are ordinarily used a polyester polyol synthesized from ethylene glycol or 1,4-butylene glycol and adipic acid and a polycaprolactone polyol prepared from .epsilon.-caprolactone. The conventional polycaprolactone polyol is defective in that it is inferior to polyether type polyols, especially polytetramethylene glycol (PTMG), in the elastic recovery. Accordingly, the conventional polycaprolactone polyol cannot be used in the fields where a high elastic recovery is required. When polyester type polyols are used for the synthesis of urethane prepolymers to be used for casting or urethane type adhesives, their operation adaptability is bad because of a high viscosity, and if the viscosity is reduced so as to improve the operation adaptability, the characteristics of the resulting polyurethanes are degraded. We made researches with a view to eliminating these defects of conventional polycaprolactone type polyurethanes, and we found that a polyurethane prepared by using a polycaprolactone polyol having a narrow molecular weight distribution has an excellent elastic recovery not observed in the conventional products and it has a lower viscosity than those of the conventional products and a highly improved operation adaptability in the synthesis of prepolymers and urethane type adhesives. We have now completed the present invention based on this finding. More specifically, the present invention relates a polyurethane prepared by reacting an organic diisocyanate with a compound containing at least two active hydrogen atoms in the molecule, wherein a polycaprolactone polyol having a narrow molecular weight distribution in which the ratio of the weight average molecular weight to the number average molecular weight is in the range of from 1.1 to 2.0 and the average molecular weight is 500 to 5,000, is used as the active hydrogen atom-containing compound, and a process for the preparation thereof. As the organic diisocyanate that is used in the present invention, there can be mentioned, for example, 2,4-tolylene diisocyanate, 2,6-tolylene diisocyanate, 4,4'-diphenylmethane diisocyanate, tolidine diisocyanate, hexamethylene diisocyanate, isophorone diisocyanate and 1,5-naphthalene diisocyanate. As the chain extender that is used in carrying out the present invention, there are preferably used ethylene glycol, propylene glycol, 1,4-butylene glycol and 1,6-hexamethylene diol. Furthermore, there can be used ethylene diamine, propylene diamine and hydrazine. For preparing the polyurethane of the present invention, there is preferably adopted a prepolymer process comprising reacting a polyol with an excessive amount of an organic isocyanate to form an isocyanate-terminated prepolymer and then reacting the formed prepolymer with a chain extender such as a diol or diamine. As the solvent to be used for the preparation of a solution type polyurethane, such as a urethane adhesive, there can be used ordinary solvents such as toluene, ethyl acetate, methylethyl ketone and dimethylformamide. The polycaprolactone type polyurethane of the present invention is excellent over the conventional products in the elastic recovery and has a low viscosity and a good operation adaptability. This is due to the fact that the molecular distribution of the polycaprolactone polyol is narrow and in the range of from 1.1 to 2.0. The polyurethane of the present invention can be used very advantageously for manufacture of a spandex products, adhesives, artificial leathers and paints. |
| PATENT EXAMPLES | available on request |
| PATENT PHOTOCOPY | available on request |
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