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Adiabatic process for making mononitrobenzene

一种二硝基苯、工艺的技术,应用在制备单硝基苯的改进工艺领域,能够解决移除和处理运行成本和资金投资巨大等问题

Active Publication Date: 2015-04-15
NORAM INT LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The operating costs and capital investment required to remove and dispose of these by-products are significant

Method used

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  • Adiabatic process for making mononitrobenzene
  • Adiabatic process for making mononitrobenzene

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Embodiment

[0022] Eight batch nitrations were performed in an adiabatic continuously stirred reactor. From the perspective of chemical reactor theory, the reaction time in a batch stirred reactor is approximately equivalent to the reaction distance in an ideal continuous mixing plug flow reactor. Therefore, the results from these batch stirred reactor experiments will more closely represent those of an ideal plug flow nitration reactor than the CSTR reactor. In all experiments performed, the concentration of nitric acid in the mixed acid was the same, which was less than 3% by weight nitric acid, and the strength of sulfuric acid in the mixed acid was the same. Only the initial mixed acid temperature (ie, the temperature before the nitration reaction starts) differs, resulting in different average reaction temperatures. At the beginning of each experiment, the sulfuric and nitric acids were thoroughly mixed in the reactor at a controlled initial temperature. An appropriate amount of be...

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Abstract

An adiabatic process for making mononitrobenzene by the nitration of benzene which minimizes the formation of nitrophenols and dinitrobenzene by-products. The process uses a mixed acid having less than 3 wt % nitric acid, 55 to 80 wt % sulfuric acid, and water. The initial temperature of the mixed acid is in the range of 60 to 96° C. The nitration reaction is complete in about 300 seconds and produces less than 1,200 ppm nitrophenols and less than about 80 ppm dinitrobenzene. The reaction can be carried out in a plug-flow or a stirred pot reactor, or a combination of such reactors.

Description

technical field [0001] The present invention relates to an improved process for preparing mononitrobenzene. More specifically, it relates to an adiabatic nitration process that will minimize the formation of undesired by-products. Background of the invention [0002] Industrially, mononitrobenzene is produced by several adiabatic nitration techniques. Adiabatic nitrification was first introduced by Castner as described in US 2,256,999. The adiabatic nitration of benzene has replaced the previously used energy-intensive isothermal nitration process. [0003] In the late 1970s, Alexanderson et al. proposed varying the composition and temperature limits of Castner's adiabatic nitration process, resulting in a commercially useful process, as described in US 4,021,498 and US 4,091,042. US 4,021,498 describes a process for the preparation of mononitrobenzene using a mixed acid with a strength of nitric acid of 5-8.5% by weight, a strength of sulfuric acid of 60-70% by weight an...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C07C201/08
CPCC07C201/08C07C205/06B01J19/18
Inventor 塞尔吉奥·贝雷塔
Owner NORAM INT LTD
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