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Two-Step System And Method For The Production Of Methyl Isobutyl Ketone

机译:两步法生产甲基异丁基酮的系统和方法

摘要

Embodiments of the present invention describe systems and methods for production of methyl isobutyl ketone (MIBK) from acetone and hydrogen in a two-step process. In a first step, acetone is converted to a product stream containing mesityl oxide (MO) at a temperature in the range of about 0-120° C. and a pressure in the range of about 1-3 atm. The composition of the product stream from the first reaction step is adjusted so that the resulting stream can undergo a favorable liquid-liquid separation in a decanter, and an MO rich product stream can be recovered. The composition of the feed to the decanter is controlled by choosing the number of reactor stages for the first reaction step and their operating temperatures, and/or by recycling some MIBK to the decanter feed. The method does not require a substantially complete conversion of acetone in the first reaction step, nor does it require a removal of DAA from the product of the first reaction step by separation.
机译:本发明的实施方案描述了在两步法中由丙酮和氢生产甲基异丁基酮(MIBK)的系统和方法。在第一步中,将丙酮在约0-120℃范围内的温度和约1-3atm范围内的压力下转化成含有异丁烯二氧化物(MO)的产物流。调节来自第一反应步骤的产物流的组成,使得所得的流可以在倾析器中进行良好的液-液分离,并且可以回收富含MO的产物流。通过选择用于第一反应步骤的反应器级数和它们的操作温度,和/或通过将一些MIBK再循环到to析器进料中,来控制to析器进料的组成。该方法不需要在第一反应步骤中丙酮的基本完全转化,也不需要通过分离从第一反应步骤的产物中除去DAA。

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