This invention relates to novel polyurethanes, more particularly thermoplastic polyurethanes, and to their use. Polyurethanes and also thermoplastic polyurethanes are already long known and have come to be widely used. For instance, polyurethanes are used in the footwear and automotive industries, for self-supporting films/sheets, cable sheathing or in leisure articles, and also variously as a blend component.
Commercially, there is increasing demand for polyurethane products where all or some of the petrochemical raw materials are replaced by raw materials from renewable sources. Sebacic acid is a renewable raw material obtained from vegetable oil (castor oil) for example. However, sebacic esters tend to crystallize, which is undesirable for many applications and so rules them out of many applications. U.S. Pat. No. 5,695,884 discloses the use of polyester polyols based on sebacic acid for thermoplastic polyurethanes of high crystallinity. US 2006/0141883 A1 and US 2006/0121812 also describe the use of polyester polyols based on sebacic acid for polyurethanes for fibers having a high melting point. WO 00/51660 A1 describes polyurethanes for heart catheters which can utilize polyester polyols based on sebacic acid; again, sufficient hardness is required. US 2007/0161731 A1 and U.S. Pat. No. 6,395,833 B1 further disclose using sebacic acid to produce polyester polyols for use in polyurethane chemistry.
It is an object of the present invention to provide polyester diols that are distinctly less prone to crystallize. More particularly, they should be useful for preparing transparent thermoplastic polyurethanes.
We have found that this object is achieved by polyurethanes based on
To determine the number of carbon atoms, count only the carbon atoms directly between the carboxyl groups of the dicarboxylic acid and only the carbon atoms directly between the OH groups of the diols and not the carbon atoms in branches.
In a preferred embodiment, the dicarboxylic acid conforms to the following formula:
where
The polyurethanes of the present invention surprisingly display reduced crystallization and improved transparency, while branched diols also contribute to a distinct suppression of so-called soft phase crystallization. Unbranched diols are particularly preferred. In another preferred embodiment, branched diols are used as a portion together with unbranched diols, although generally more than 50 mol % of unbranched diols are used, based on the totality of diols.
In a further preferred embodiment, the polyurethane of the present invention comprises a thermoplastic polyurethane.
In a further preferred embodiment, the polyurethanes obtained are transparent.
In a further preferred embodiment, the glass transition temperature of the polyurethane of the present invention, determined via dynamic mechanical analysis (DMA), is smaller than that of a comparably obtained polyurethane having whichever is the next higher even diol and/or dd dicarboxylic acid in said polyester diol B.
In one preferred embodiment, the molecular weight of the polyester diol is between 500 to 4000 g/mol, more preferably between 800 and 2500 g/mol and even more preferably between 1000 and 2000 g/mol (corresponding to an OH number of 28 to 224 and preferably 112 to 56 mg KOH/g). In a further preferred embodiment, the dicarboxylic acid underlying the polyester diol B is sebacic acid. In a further preferred embodiment, the diol is 1,3-propanediol. In a particularly preferred embodiment, the polyester diol B is a propanediol sebacate.
Processes for preparing polyester diols by polycondensation of the corresponding diols with at least one dicarboxylic acid preferably at elevated temperature and reduced pressure preferably in the presence of known catalysts are common knowledge and have been extensively described.
Processes for preparing polyurethanes are likewise common knowledge. For example, thermoplastic polyurethanes are obtainable by reaction of (a) isocyanates with (b) isocyanate-reactive compounds having a molecular weight of 500 to 10 000 g/mol and optionally (c) chain-extending agents having a molecular weight of 50 to 499 g/mol optionally in the presence of (d) catalysts and/or (e) customary assistants.
According to the present invention, the preferred thermoplastic polyurethanes are prepared by reaction of isocyanate A with polyester diol B and optionally further isocyanate-reactive compounds and optionally chain-extending agents C optionally in the presence of catalysts D and/or customary assistants E, wherein sebacic acid propanediol is used with particular preference.
The polyurethane of the present invention can also be obtained via the intermediate stage of prepolymers. Only incomplete chains of the polymer are initially prepared in order that the end-user may have the benefit of simpler processing, particularly of the isocyanate component. The incompletely reacted starting materials thus provided are also referred to as the system, which are very important in the manufacture of shoe soles for example.
The components A, B, C and also optionally D and/or E customarily used in the manufacture of polyurethanes will now be described by way of example:
Further details about the abovementioned auxiliary and added substances are discernible from the technical literature, for example from Plastics Additive Handbook, 5th edition, H. Zweifel, ed, Hanser Publishers, Munich, 2001. All molecular weights mentioned in this reference have the unit [g/mol].
In a further preferred embodiment, the dicarboxylic acid and/or the diol of said polyester diol B and/or said chain extender C are of nonfossil origin.
The preparation of the polyurethanes can be carried out according to the known processes as a batch operation or as a continuous operation, for example using reactive extruders or the belt process by the one shot or the prepolymers process, preferably by the one shot process. In these processes, the reactant components A, B and optionally C, D and/or E can be mixed in succession or at the same time, and the reaction ensues immediately. In the extruder process, the structural components A, B and also optionally C, D and/or E are introduced into the extruder individually or as a mixture, reacted at temperatures of 100 to 280° C. and preferably 140 to 250° C., for example, and the polyurethane obtained is extruded, cooled down and pelletized.
The processing of the polyurethanes of the present invention, which are typically in the form of pellets or powders, to form the desired self-supporting films/sheets, molded parts, rollers, fibers, linings in automobiles, hoses, cable plugs, bellows, drag cables, cable sheathing, gaskets, belts or shock-absorbing elements is effected according to customary processes, for example injection molding, calendering or extrusion. The thermoplastic polyurethanes obtainable by the processes of the present invention, preferably coatings, cables, floors for buildings and transportations, plug connectors, solar modules, self-supporting films/sheets, molded parts, shoe soles and shoe parts, rollers, fibers, linings in automobiles, profiles, laminates and wiper blades, hoses, cable plugs, bellows, drag cables, cable sheathing, gaskets, nonwoven fabrics, belts or shock-absorbing elements have the advantages described at the beginning.
The dicarboxylic acids and diols apparent from Table 1 were reacted in vacuum in a dicarboxylic acid/diol ratio of about 1/1. Next this polyester diol was admixed with butanediol chain extender while stirring. Following subsequent heating of the solution to 80° C., methylenediphenyl diisocyanate (MDI) was added and stirred in until the solution was homogeneous.
The crystallization temperatures of the polyurethane obtained were determined as follows:
The glass transition temperature Tg of the soft phase was determined by dynamic mechanical analysis (DMA). Here the maximum of tan 8 corresponds to the glass transition temperature Tg. The DMA measurement was carried out on an instrument from Rheometric Scientific (ARES). The measurements were carried out as per DIN EN ISO 6721.
The values apparent from Table 1 below were obtained:
Implications are as follows:
Number | Date | Country | Kind |
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08164554.1 | Sep 2008 | EP | regional |
Filing Document | Filing Date | Country | Kind | 371c Date |
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PCT/EP2009/062019 | 9/16/2009 | WO | 00 | 3/14/2011 |