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Co-production of an aromatic monoamine and an aromatic diamine directly from benzene or a benzene derivative through controlled nitration

机译:通过控制硝化作用直接从苯或苯衍生物联合生产芳族单胺和芳族二胺

摘要

A two-stage process for the co-production of aniline and m-phenylenediamine where, in the first stage, benzene, nitric acid, and sulfuric acid are reacted in a liquid phase to produce in greater amounts nitrobenzene (approximately 70%) and m-dinitrobenzene (approximately 30%), and in lesser or trace amounts o-dinitrobenzene and p-dinitrobenzene, and water; and in the second stage the products of the first stage are reacted with hydrogen in the gas phase to produce aniline (approximately 70%) and m-phenylenediamine (approximately 30%) in greater amounts, and o-phenylenediamine and p-phenylenediamine in lesser amounts, and water. The reaction products are separated by distillation. The first stage of a preferred embodiment of the process is characterized in that a concentrated mixture of nitric acid and sulfuric acid are fed along with mononitrobenzene to a first reactor for producing dinitrobenzene, and then the dilute acid mixture recovered from this first reactor is fed along with benzene to a second reactor for producing the mononitrobenzene used as a reactant in the first reactor. The second stage, which provides the aniline and m-phenylenediamine in major amounts, is characterized in that the hydrogenation is carried out in the gas phase with product aniline serving as a diluent. The process is applicable to the co-production of other aromatic mono- and diamines.
机译:联产苯胺和间苯二胺的两步法,在第一步中,苯,硝酸和硫酸在液相中反应生成大量的硝基苯(约70%)和-二硝基苯(约30%),以及少量或痕量的邻二硝基苯和对二硝基苯以及水;在第二阶段中,第一阶段的产物与气相中的氢气反应生成大量的苯胺(约70%)和间苯二胺(约30%),而邻苯二胺和对苯二胺的数量较少量和水。反应产物通过蒸馏分离。该方法的一个优选实施方案的第一阶段的特征在于,将硝酸和硫酸的浓混合物与一硝基苯一起进料到用于生产二硝基苯的第一反应器中,然后将从该第一反应器中回收的稀酸混合物一起进料。将苯与苯一起送入第二反应器,以生产在第一反应器中用作反应物的一硝基苯。第二阶段主要提供苯胺和间苯二胺,其特征在于氢化在气相中以产物苯胺作为稀释剂进行。该方法适用于其他芳族单胺和二胺的联产。

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