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Method for producing adipic acid by utilizing air oxidation of cyclohexane based on gas-liquid-solid heterogeneous reaction separation synchronous reactor

A technology of heterogeneous reaction and air oxidation, which is used in the preparation of carboxylic acid by oxidation, chemical instruments and methods, separation/purification of carboxylic acid compounds, etc. Reduce selectivity and yield, increase the residence time of reaction products, etc., achieve high-selectivity continuous production, prevent off-site overreaction, and solve the effects of complex equipment structure

Active Publication Date: 2015-08-19
蚌埠启邦科技信息咨询有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The continuous process of insoluble products can be realized by adding solvents; however, the addition of solvents makes the chemical production process complicated, and also increases the corresponding equipment investment and energy consumption, material consumption and environmental pollution by solvents; another One option is to use interstitial operations to produce
In the above two schemes, the residence time of the reaction product in the reaction system will be increased, and under the reaction operating conditions, the reaction product will be decomposed or deeply reacted, resulting in a decrease in the selectivity and yield of the reaction product

Method used

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  • Method for producing adipic acid by utilizing air oxidation of cyclohexane based on gas-liquid-solid heterogeneous reaction separation synchronous reactor
  • Method for producing adipic acid by utilizing air oxidation of cyclohexane based on gas-liquid-solid heterogeneous reaction separation synchronous reactor
  • Method for producing adipic acid by utilizing air oxidation of cyclohexane based on gas-liquid-solid heterogeneous reaction separation synchronous reactor

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0035] Attached figure 1 The shown gas-liquid-solid multiphase reaction separation synchronous reactor carries out the air oxidation of cyclohexane to prepare adipic acid products; wherein, the diameter-to-height ratio of the bubbling gravity reaction tower is 1:35; the ratio of the length of the gravity settling plate to the diameter of the tower is 1 : 1.2; the included angle of the gravity settling plate along the tower axis is 55°; there are two constant temperature settling towers, the constant temperature settling tower I and the constant temperature settling tower II; the outlet of the reaction liquid is 3 / 7 away from the height of the tower body .

[0036] Copper tetraphenylporphyrin (concentration: 30ppm) is added to the cyclohexane raw material as a catalyst, and the mixed solution enters the constant temperature settling tower I and the bubbling gravity reaction tower from the upper reaction material inlet of the constant temperature settling tower I, and is filled ...

Embodiment 2

[0040] Attached figure 1 The gas-liquid-solid multiphase reaction separation synchronous reactor is used to prepare adipic acid products by air oxidation of cyclohexane; wherein, the diameter-to-height ratio of the bubbling gravity reaction tower is 1:25; the ratio of the length of the gravity settling plate to the diameter of the tower is 1 : 1.1; the included angle of the gravity settling plate inclined along the tower axis is 65°; there are two constant temperature settling towers, the constant temperature settling tower Ⅰ and the constant temperature settling tower Ⅱ; .

[0041] Tetraphenylporphyrin iron μ-dimer (concentration: 20ppm) is added to the cyclohexane raw material as a catalyst, and the mixed solution enters the constant temperature settling tower I and the bubbling gravity reaction tower from the upper reaction material inlet of the constant temperature settling tower I, and is filled with In the oxidation zone of the constant temperature settling tower Ⅰ and ...

Embodiment 3

[0046] Attached figure 1 The gas-liquid-solid multiphase reaction separation synchronous reactor is used to prepare adipic acid products by air oxidation of cyclohexane; wherein, the diameter-to-height ratio of the bubbling gravity reaction tower is 1:32; the ratio of the length of the gravity settling plate to the diameter of the tower is 1 : 0.9; The included angle of the gravity settling plate along the tower axis is 50°; there are two constant temperature settling towers, the constant temperature settling tower I and the constant temperature settling tower II; .

[0047] Cobalt naphthenate (concentration: 100ppm) is added to the cyclohexane raw material as a catalyst, and the mixed liquid enters the constant temperature settling tower I and the bubbling gravity reaction tower from the upper reaction material inlet of the constant temperature settling tower I, and is filled with the constant temperature settling tower I and the bubbling gravity reaction tower. In the oxida...

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Abstract

The invention discloses a method for producing adipic acid by oxidizing cyclohexane by utilizing air based on a gas-liquid-solid multiphase reaction and separation synchronization reactor. The method is characterized by adding cyclohexane to the gas-liquid-solid multiphase reaction and separation synchronization reactor, wherein the reactor comprises a reaction tower and at least two constant temperature settling towers communicated with the bottom of the reaction tower, and the reaction tower is internally provided with a gas phase zone, an oxidation zone and a gas outlet; during reaction, filling the oxidation zone and constant temperature settling towers with cyclohexane, continuously pumping air from the bottom of the oxidation zone to come into contact with cyclohexane to carry out oxidation reaction, simultaneously enabling generated adipic acid solid to enter the constant temperature settling towers through settling, at the moment, enabling cyclohexane in the constant temperature settling towers to enter the oxidation zone via an external circulation system so that reaction is continuously carried out, enabling adipic acid to continuously settle in the constant temperature settling towers until the constant temperature settling towers are filled with the adipic acid phase, and switching a reaction tower to be communicated with the other constant temperature settling tower filled with cyclohexane, thus alternating the steps to carry out continuous production. The method can be used for continuously producing adipic acid with high conversion rate and high yield, and has the effects of improving the production efficiency and reducing the production cost.

Description

technical field [0001] The invention relates to a process for producing adipic acid by oxidizing cyclohexane with air. Background technique [0002] Adipic acid is the basic chemical raw material of Nylon 66. Industrially, the liquid-phase nitric acid oxidation of cyclohexanone is the main method for preparing adipic acid. The process of preparing adipic acid from cyclohexanone with nitric acid uses high-cost cyclohexanone as a raw material, and nitric acid will corrode equipment and have problems of environmental pollution. In recent years, some patents have disclosed the process of preparing adipic acid through the biomimetic catalytic air oxidation of cyclohexane by metalloporphyrins. Patent CN1850756A and patent CN1530358A disclose the process and equipment for the preparation of adipic acid by low-concentration metalloporphyrin biomimetic catalytic air oxidation of cyclohexane, but the product obtained by this technology is a mixture of cyclohexanol, cyclohexanone and...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C07C51/31C07C51/42C07C55/14B01J8/10B01J8/12
CPCB01J8/007B01J8/10B01J8/125C07C51/313C07C51/42C07C55/14
Inventor 郭灿城郭欣
Owner 蚌埠启邦科技信息咨询有限公司
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