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Method of controlling the amount of used catalyst to be recycled to a hydrogenation reactor, used to produce fatty alcohols from fatty acids, or their derivatives

机译:控制要循环到氢化反应器中,用于由脂肪酸或其衍生物生产脂肪醇的催化剂用量的方法

摘要

Fatty acids and/or fatty acid derivatives as well as hydrogen, fresh catalyst and a dispersion which contains used catalyst are supplied to the hydrogenating means, which are operated at temperatures in the range from 100 DEG to 400 DEG C. and under pressures in the range from 20 to 400 bars to produce a product stream, which contains fatty alcohols and used catalyst. A part of the product stream is circulated. A first partial stream Is withdrawn at a controllable rate from the circulating stream and is passed through a separator. A product which is rich in fatty alcohol and a dispersion which contains used catalyst are separately delivered by the separator. The dispersion is recycled to the hydrogenating means. A second partial stream is withdrawn at a controllable rate from the circulating product stream. Used catalyst is separated from the second partial stream and is removed from the process. The rate at which used catalyst is fed to the hydrogenating means can be increased in that the rate of the second partial stream is decreased.
机译:脂肪酸和/或脂肪酸衍生物以及氢气,新鲜催化剂和包含用过的催化剂的分散体被提供给加氢装置,所述加氢装置在100℃至400℃的温度范围内和在200℃的压力下操作。范围从20到400巴,以产生包含脂肪醇和用过的催化剂的产物流。一部分产品流被循环。第一部分流以可控制的速率从循环流中抽出并通过分离器。富含脂肪醇的产物和包含用过的催化剂的分散体通过分离器分别输送。将分散体再循环到氢化装置。从循环产物流中以可控制的速率抽出第二部分流。从第二部分流中分离出用过的催化剂,并将其从工艺中除去。可以增加用过的催化剂进料到氢化装置中的速率,因为降低了第二部分物流的速率。

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