首页> 外国专利> Process for the preparation of complexes of one mol of dimerized or low- oligodimerized 4,4'-diisocyanatodiphenylmethane and two to three mol of 4, 4'-diisocyanatodiphenylmethane, corresponding complexes, and their use for polyurethane production

Process for the preparation of complexes of one mol of dimerized or low- oligodimerized 4,4'-diisocyanatodiphenylmethane and two to three mol of 4, 4'-diisocyanatodiphenylmethane, corresponding complexes, and their use for polyurethane production

机译:一摩尔二聚或低聚的4,4'-二异氰酸根合二苯基甲烷与两至三摩尔4,4'-二异氰酸根合二苯基甲烷的配合物的制备方法,相应的配合物及其在聚氨酯生产中的用途

摘要

The present invention relates to a process for the dimerization of 4, 4'-diisocyanatodiphenylmethane from emulsion in apolar solvents with the formation of complexes and to the complexes obtainable for the first time by this process. The complexes consist of one mol of low molecular weight 4,4'-diisocyanato-diphenylmethane-uretdione or its low oligomers corresponding to the idealized formula (I) ##STR1## (n=0 to 0.5, where n is the average degree of oligomerization of the dimer) and 2 to 3 mol of 4,4'-diisocyanatodiphenylmethane (MDI) ##STR2## In the process according to the invention, 4,4'-diisocyanatodiphenylmethane (II) in the molten form is emulsified in apolar solvents. Dimerization is started in the presence of conventional dimerization catalysts at temperatures above the melting point of MDI, preferably up to an upper temperature limit of 50. degree. to 60 C. The temperature is then lowered to 40. degree. C. If desired, dimerization can be stopped when an isocyanate content of from 22.4 to 26.9% has been reached. The product is then worked up at low temperatures, preferably at 0 to 25 C. The complex obtained is claimed as a new substance. The use of the complex for the production of polyurethanes is also claimed.
机译:本发明涉及在非极性溶剂中使乳液中的4,4′-二异氰酸根合二苯基甲烷二聚而形成络合物的方法,以及涉及该方法首次获得的络合物。配合物由一摩尔的低分子量4,4'-二异氰酸根合-二苯甲烷-脲二酮或其低聚物组成,对应于理想化的式(I)## STR1 ##(n = 0至0.5,其中n为平均度(二聚物的低聚)和2至3摩尔的4,4'-二异氰酸根合二苯基甲烷(MDI)## STR2 ##在本发明的方法中,将熔融形式的4,4'-二异氰酸根合二苯基甲烷(II)乳化在非极性溶剂。在常规二聚催化剂的存在下,在高于MDI熔点的温度下,优选最高温度上限为50℃,开始二聚反应。至60℃。然后将温度降低至<40℃。 C.如果需要,当异氰酸酯含量达到22.4%至26.9%时,可以停止二聚。然后将产物在低温下,优选在0至25℃下进行后处理。获得的复合物被要求为新物质。还要求保护该配合物用于生产聚氨酯。

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