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    • 1. 发明授权
    • Continuous process for thermal splitting of carbamic acid esters
    • 氨基甲酸酯热分解的连续工艺
    • US4692550A
    • 1987-09-08
    • US485347
    • 1983-04-15
    • Theodor EngbertGunter HammenHartmut KnofelKlaus Konig
    • Theodor EngbertGunter HammenHartmut KnofelKlaus Konig
    • C07C263/04C07C27/00C07C31/02C07C31/125C07C67/00C07C241/00C07C265/00C07C265/04C07C265/12C07C118/00
    • C07C263/04
    • N-monosubstituted carbamic acid esters are thermally split on a continuous basis in a tube reactor. The carbamic acid ester which is flowed down or passed over the inner wall of a tube reactor is thermally split at a temperature of from 150.degree. to 450.degree. C. and under a pressure of from 0.001 to 20 bar into at least two fractions. One fraction is predominantly isocyanate and a second fraction is predominantly hydroxyl compound. These fractions may be separated by removing one as a gaseous fraction formed under the splitting conditions from the head of the reactor and collecting the second fraction as a liquid which accumulates at the base of the reactor. If both fractions are gaseous under the splitting conditions, they are both removed from the head of the reactor and subsequently separated by fractionating columns for example. This process is particularly advantageous in that isocyanate and hydroxyl fractions are obtained in high yield without using a solvent.
    • N-单取代氨基甲酸酯在管式反应器中以连续的方式热分解。 流过或流过管式反应器内壁的氨基甲酸酯在150℃至450℃的温度和0.001至20巴的压力下热分解成至少两个馏分。 一个部分主要是异氰酸酯,第二部分主要是羟基化合物。 这些级分可以通过除去在分离条件下从反应器的头部形成的气态馏分来分离,并将第二馏分作为积聚在反应器底部的液体进行收集。 如果两个馏分在分解条件下都是气态的,则它们都从反应器的头部移出,并随后通过分馏塔例如分离。 该方法特别有利的是在不使用溶剂的情况下以高产率获得异氰酸酯和羟基部分。
    • 2. 发明授权
    • Isocyanato-isocyanurate derivatives
    • 异氰酸酯 - 异氰脲酸酯衍生物
    • US4698424A
    • 1987-10-06
    • US666586
    • 1984-10-31
    • Theodor EngbertHartmut KnofelGerhard Wegener
    • Theodor EngbertHartmut KnofelGerhard Wegener
    • C07D251/34C08G18/00C08G18/79C09D175/00
    • C07D251/34C08G18/791
    • The present invention relates to isocyanato-isocyanurates corresponding to the formula ##STR1## in which X.sub.1, X.sub.2 and X.sub.3 may be the same or different and represent radicals corresponding to the formula ##STR2## wherein R.sup.1 and R.sup.2 may be the same or different and represent hydrogen or C.sub.1 -C.sub.12 alkyl groups, and p is a whole or (on a statistical average) fractional number of from 1 to 5.The present invention also relates to a process for producing these isocyanato-isocyanurates and additionally relates to the use of the new isocyanato-isocyanurates, optionally blocked by blocking agents for isocyanate groups, as the isocyanate component in the produciton of isocyanate polyaddition products, preferably polyurethane lacquers.
    • 本发明涉及对应于式(I)的异氰酸根合 - 异氰脲酸酯,其中X 1,X 2和X 3可以相同或不同,并且表示与式(II)相应的基团,其中R 1和R 2可以是 相同或不同,表示氢或C 1 -C 12烷基,p是1至5的整数或(统计平均)分数。本发明还涉及一种制备这些异氰酸根合异氰脲酸酯的方法,另外 涉及在异氰酸酯加成产物(优选聚氨酯漆)的生产中使用新的异氰酸根合异氰脲酸酯,其任选被封闭剂用于异氰酸酯基团封端,作为异氰酸酯组分。
    • 4. 发明授权
    • Process for the preparation of polyisocyanates
    • 制备多异氰酸酯的方法
    • US5043471A
    • 1991-08-27
    • US519190
    • 1990-05-04
    • Gunter HammenHartmut KnofelWolfgang Friederichs
    • Gunter HammenHartmut KnofelWolfgang Friederichs
    • C07C263/04C07C263/20C07C265/14
    • C07C263/20C07C263/04
    • The present invention relates to a process for the preparation of a polyisocyanate comprising(a) thermally decomposing in a tube reactor a solution of an N-substituted carbamic acid ester corresponding to said polyisocyanate in a solvent used as decompositoin medium, wherein said solvent (i) is capable of dissolving the carbamic acid ester, (ii) is stable at the decomposition temperature and chemically inert towards the carbamic acid esters and the polyisocyanate product, (iii) can be distilled without decomposing under the conditions of decomposition of carbamic acid estes, and (iv) has at least one miscibility gap with an extracting agent used according to the extraction step (c), said solutions being carried along the internal wall of reactor;(b) separating the gaseous materials formed in the tube reactor by fractional condensation into a fraction I comprised mainly of the alcohol by-product and a fraction II comprised mainly of polyisocyanates, isocyanatourethanes, unreacted carbamic acid ester, and the solvent used in step (a);(c) extracting the polyisocyanate from said fraction II with an extracting agent that is at least partly immiscible with the decomposition medium and is a solvent for the polyisocyanate, and optionally distilling the resultant solution of the polyisocyanate in the extracting agent; and(d) recycling the portion of fraction II remaining after the polyisocyanate is extracted.
    • 本发明涉及一种制备多异氰酸酯的方法,其包含(a)在管式反应器中将在所述多异氰酸酯中的N-取代氨基甲酸酯的溶液在用作分解介质的溶剂中热分解,其中所述溶剂(i )能够溶解氨基甲酸酯,(ii)在分解温度下稳定并对氨基甲酸酯和多异氰酸酯产物具有化学惰性,(iii)可以在氨基甲酸酯分解条件下不分解而蒸馏, 和(iv)与根据提取步骤(c)使用的萃取剂具有至少一个混溶性间隙,所述溶液沿反应器内壁运送; (b)通过分级冷凝将形成在管式反应器中的气态物质分离成主要由醇副产物组成的馏分I和主要由多异氰酸酯,异氰酸酯基氨基甲酸酯,未反应的氨基甲酸酯和步骤( 一个); (c)使用与分解介质至少部分不混溶并且是多异氰酸酯的溶剂的提取剂从所述级分II中提取多异氰酸酯,并且任选地将得到的多异氰酸酯溶液蒸馏在萃取剂中; 和(d)回收在提取多异氰酸酯之后残留的馏分II的部分。
    • 9. 发明授权
    • Diamines and a process for their production
    • 二胺及其生产工艺
    • US4720582A
    • 1988-01-19
    • US523211
    • 1983-08-15
    • Hartmut KnofelMichael BrockeltStefan Penninger
    • Hartmut KnofelMichael BrockeltStefan Penninger
    • C07B61/00B01J23/00C07C67/00C07C209/00C07C209/36C07C209/72C07C211/49C08G18/32C07C87/52
    • C08G18/3234
    • Diamines corresponding to the general formula ##STR1## wherein R.sup.1, R.sup.2 and R.sup.3 may be identical or different and represent hydrogen or straight- or branched-chain C.sub.1 -C.sub.12 alkyl groups, provided that two of the radicals,R.sup.1, R.sup.2 and R.sup.3, represent hydrogen, m and n each represent 0 or 1, provided that m+n=1; where m or n=0, the free valence is saturated by hydrogen, optionally in the form of isomeric mixtures, and optionally containing up to 35%, by weight, of the corresponding perhydrogenated diamines, and up to 10%, by weight, of the corresponding unhydrogenated aromatic diamines.Also, a process for preparing these diamines by catalytically-hydrogenating the corresponding aromatic diamines with 3 moles of hydrogen per mole of diamine, or catalytically-hydrogenating the corresponding dinitro compounds with 9 moles of hydrogen per mole of dinitro compound.
    • 对应于通式“IMAGE”的二胺,其中R 1,R 2和R 3可以相同或不同,表示氢或直链或支链C 1 -C 12烷基,条件是基团R 1,R 2和R 3中的两个表示 氢,m和n各自表示0或1,条件是m + n = 1; 其中m或n = 0,任选地以异构混合物形式的氢饱和,并且任选地含有至多35重量%的相应的过氢化二胺,以及至多10重量%的 相应的未氢化芳族二胺。 另外,通过用相对于每摩尔二胺的3摩尔氢催化氢化相应的芳族二胺或每摩尔二硝基化合物以9摩尔氢催化氢化相应的二硝基化合物来制备这些二胺的方法。