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Process for preparing phenetidine and amino phenol by using mixture of nitrophenetol and nitrophenol as raw materials

A technology for nitrophenethyl ether and aminophenethyl ether, which is applied in the field of preparing aminophenethyl ether and aminophenol, can solve the problems of high energy consumption in the production process, a large amount of process waste water, material loss, etc., and achieves low equipment corrosion and process safety. , the effect of low cost

Active Publication Date: 2008-11-19
江苏仁欣化工股份有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Usually p-aminophenetole and o-aminophenetole as well as p-nitrophenol and o-nitrophenol are independent preparation processes and separation and refining processes. This traditional preparation process has the following disadvantages: due to the use of a single component as a raw material during the preparation , it is necessary to pre-treat the raw materials of the mixture in advance to obtain the required single-component raw materials. In the preparation process, pre-treatment requires a lot of equipment and unit operations, which inevitably has the disadvantages of high energy consumption and high cost in the production process, and in the pre-treatment process A large amount of process wastewater will be produced, causing serious environmental pollution and loss of materials, such as the treatment of these wastewater will greatly increase the cost

Method used

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  • Process for preparing phenetidine and amino phenol by using mixture of nitrophenetol and nitrophenol as raw materials
  • Process for preparing phenetidine and amino phenol by using mixture of nitrophenetol and nitrophenol as raw materials

Examples

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Effect test

Embodiment 1

[0023] The main process equipment is: kettle-type stirred reactor, blade-type filter device, continuous rectification tower.

[0024] A kind of technology that prepares aminophenetole and aminophenol with nitrophenetole and nitrophenol mixture as raw material, described processing step is as follows:

[0025] (1) Bulk catalytic hydrogenation reduction reaction: In the catalytic hydrogenation reduction tank type stirred reactor, the mixture of nitrophenetole and nitrophenol is used as raw material, and the nitrophenetole is p-nitrophenetole and o-nitrophenetole Nitrophenetole, the nitrophenols are o-nitrophenol and p-nitrophenol, and the percentage by weight of various components in the raw material mixture is 95.0% for nitrophenethyl ether and 5.0% for nitrophenol. Wherein the ratio between p-nitrophenetole and o-nitrophenetole is 1:1 by weight, o-nitrophenol 1.0%, p-nitrophenol 4.0%. Use Pd-C as the catalyst, the equivalent diameter of the catalyst particles is 0.01mm, the c...

Embodiment 2

[0032] The main process equipment is: kettle-type stirred reactor, blade-type filter device, batch-type rectification tower.

[0033] A kind of technology that prepares aminophenetole and aminophenol with nitrophenetole and nitrophenol mixture as raw material, described processing step is as follows:

[0034] (1) Bulk catalytic hydrogenation reduction reaction: In the catalytic hydrogenation reduction tank type stirred reactor, the mixture of nitrophenetole and nitrophenol is used as raw material, and the nitrophenetole is p-nitrophenetole and o-nitrophenetole Nitrophenetole, the nitrophenols are o-nitrophenol and p-nitrophenol, and the percentage by weight of various components in the raw material mixture is 98.5% for nitrophenethyl ether and 1.5% for nitrophenol. Wherein the ratio between p-nitrophenetole and o-nitrophenetole is 1:2 by weight, o-nitrophenol is 0.5%, and p-nitrophenol is 1.0%. Using Pt-C as the catalyst, the equivalent diameter of the catalyst particles is 1...

Embodiment 3

[0041] The main process equipment is: kettle-type stirred reactor, blade-type filter device, continuous rectification tower.

[0042] A kind of technology that prepares aminophenetole and aminophenol with nitrophenetole and nitrophenol mixture as raw material, described processing step is as follows:

[0043] (1) Bulk catalytic hydrogenation reduction reaction: In the catalytic hydrogenation reduction tank type stirred reactor, the mixture of nitrophenetole and nitrophenol is used as raw material, and the nitrophenetole is p-nitrophenetole and o-nitrophenetole Nitrophenetole, the nitrophenols are o-nitrophenol and p-nitrophenol, and the percentage by weight of various ingredients in the raw material mixture is 96.0% for nitrophenethyl ether and 4.0% for nitrophenol. Wherein the ratio between p-nitrophenetole and o-nitrophenetole is 1:1.5 by weight, o-nitrophenol is 0.8%, and p-nitrophenol is 3.2%. Using Pt-C as the catalyst, the equivalent diameter of the catalyst particles is ...

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Abstract

The invention relates to a process for preparing phenetidin and amino phenol by taking a mixture of nitrophenetol and nitrophenol as a raw material. The process comprises the following steps that: (1) a step of the catalytic hydrogenation reaction to a body, during which, the mixture of the nitrophenetol and the nitrophenol is taken as the raw material, catalyst is added, hydrogen is aerated; (2) a step of the solid-liquid separation, during which, solid and liquid in the material obtained from the step (1) after the catalytic hydrogenation reaction are separated, a liquid phase is utilized in the next step; (3) a step of the liquid-liquid separation, during which, the oil phase-water phase liquid-liquid separation is performed in the material obtained in the step (2), an oil phase is utilized in the next step; (4) a step of crystallization; (5) a step of solid-liquid separation, during which, solid and liquid of the material crystallized in the step four are separated, the solid phase is paraaminophenol and ortho-aminophenol, the phenetidine in the liquid phase is utilized in the next step; (6) a step of distillation separation, during which, the products of para aminophenyl ethyl ether and o-phenetidine are obtained. The process for preparing the aminoanisole and the aniline has the advantages that: the cost is low, the preliminary treatment step is saved, and the process is simple; and the process is clean, the energy consumption is low, and the 'three wastes' are little.

Description

technical field [0001] The invention relates to a process for preparing aminophenetole and aminophenol by using a mixture of nitrophenetole and nitrophenol as raw materials, and belongs to the technical field of fine chemicals. Background technique [0002] Both p-aminophenetole and o-aminophenetole as well as p-nitrophenol and o-nitrophenol are important organic intermediates. At present, the process adopted for the preparation of p-aminophenetole and o-aminophenetole is to use p-nitrophenetole and o-nitrophenetole as raw materials respectively, through reduction, and then separate and refine; p-aminophenol and o-aminophenetole Aminophenol is usually obtained by reducing p-nitrophenol and o-nitrophenol as raw materials, and then separating and refining. Usually p-aminophenetole and o-aminophenetole as well as p-nitrophenol and o-nitrophenol are independent preparation processes and separation and refining processes. This traditional preparation process has the following di...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C209/36C07C215/76C07C217/84
CPCY02P20/584
Inventor 段玉辉
Owner 江苏仁欣化工股份有限公司
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