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    • 3. 发明授权
    • Process for the continuous production of monoisocyanates
    • 连续生产单异氰酸酯的方法
    • US4195031A
    • 1980-03-25
    • US965648
    • 1978-12-20
    • Wolfgang ReichmannKlaus KonigJohannes Koster
    • Wolfgang ReichmannKlaus KonigJohannes Koster
    • C07C265/02C07C20060101C07C67/00C07C241/00C07C263/04C07C265/04C07C118/00
    • C07C263/04
    • The instant invention relates to an improved process for the continuous production of an aliphatic monoisocyanate from the corresponding N-alkyl carbamic acid aryl ester. More particularly, the invention is directed to a process for the continuous production of monoisocyanates corresponding to the formulaR--NCOin whichR represents an aliphatic hydrocarbon radical containing 1 to 3 carbon atoms comprising thermally decomposing the corresponding N-alkylcarbamic acid aryl esters corresponding to the formulaR--NH--CO--O--R'in whichR has the meaning above andR' represents a radical of the type obtained by removing the hydroxyl group from a monophenol having a boiling point below 250.degree. C. at normal pressure, and separating the decomposition products by decomposition, further characterized in that(a) a solution of the N-alkylcarbamic acid aryl ester in an organic solvent, which solvent is inert under the reaction conditions and has a boiling point lying at least 20.degree. C. above the boiling point of the monoisocyanate to be formed, is heated to a temperature of from 160.degree. C. to 250.degree. C. at normal pressure or at slightly reduced pressure within the range of 200 to 1013 mbar, thereby resulting in the decomposition of the ester into the corresponding monoisocyanate and the corresponding phenol, as well as the evaporation of the solvent and the decomposition products, and(b) the vapors formed are fed into a distillation column with the monoisocyanate obtained at the head of the column and with the phenol and at least a major portion of the solvent obtained from a side stream or from several side streams.
    • 本发明涉及从相应的N-烷基氨基甲酸芳基酯连续制备脂族单异氰酸酯的改进方法。 更具体地说,本发明涉及连续制备相应于式R-NCO的单异氰酸酯的方法,其中R代表含有1至3个碳原子的脂族烃基,包括热分解相应的N-烷基氨基甲酸芳基酯 式R-NH-CO-OR'其中R具有上述含义,R'表示通过在常压下从沸点低于250℃的单酚除去羟基得到的类型的基团,并且分离 分解产物,其特征还在于(a)N-烷基氨基甲酸芳基酯在有机溶剂中的溶液,该溶剂在反应条件下是惰性的,并且沸点至少在20℃以上 要形成的单异氰酸酯的沸点在常压或稍微减压的范围内加热到160℃至250℃的温度 e为200至1013毫巴,从而导致酯分解成相应的单异氰酸酯和相应的苯酚,以及溶剂和分解产物的蒸发,和(b)所形成的蒸气进料到蒸馏塔 与在柱的头部和苯酚获得的单异氰酸酯以及从侧流或从多个侧流获得的至少大部分溶剂。