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
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
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...
PUM
Abstract
Description
Claims
Application Information
- R&D Engineer
- R&D Manager
- IP Professional
- Industry Leading Data Capabilities
- Powerful AI technology
- Patent DNA Extraction
Browse by: Latest US Patents, China's latest patents, Technical Efficacy Thesaurus, Application Domain, Technology Topic, Popular Technical Reports.
© 2024 PatSnap. All rights reserved.Legal|Privacy policy|Modern Slavery Act Transparency Statement|Sitemap|About US| Contact US: help@patsnap.com