Equipment and production process for producing camphor by continuous gas phase dehydrogenation of isoborneol

A gas-phase dehydrogenation and isoborneol technology, which is applied in the direction of dehydrogenation preparation, carbon-based compound preparation, organic compound preparation, etc., can solve the problems of catalyst erosion and affecting the service life of catalysts, etc.

Active Publication Date: 2021-04-27
福建南平青松化工有限公司
View PDF7 Cites 0 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] In order to overcome the shortcomings of the existing isoborneol continuous dehydrogenation method for preparing camphor when the liquid phase enters the fixed bed reactor, which may cause erosion of the catalyst and affect the service life of the catalyst, the invention provides a method for preparing camphor by continuous gas phase dehydrogenation of isoborneol Equipment and production process, it conducts dehydrogenation reaction by vaporizing isoborneol raw material and specially designs a heat-exchanging radial flow dehydrogenation reactor suitable for it, which can carry out continuous production, has little impact on the service life of the catalyst, and reacts The material is more reasonably distributed, which can greatly improve the production efficiency of the catalyst.

Method used

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
View more

Image

Smart Image Click on the blue labels to locate them in the text.
Viewing Examples
Smart Image
  • Equipment and production process for producing camphor by continuous gas phase dehydrogenation of isoborneol
  • Equipment and production process for producing camphor by continuous gas phase dehydrogenation of isoborneol
  • Equipment and production process for producing camphor by continuous gas phase dehydrogenation of isoborneol

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0056] Such as figure 1 , 3 As shown, a kind of camphor equipment of continuous gas-phase dehydrogenation of isoborneol according to the present invention comprises feeding pump 2, vaporizer 3, heat exchange type radial flow dehydrogenation reactor 4, continuous rectification tower 5, sublimation Kettle 6 and desublimation chamber 7; the feeding pump 2 is connected with the liquid storage tank 1 containing the isoborneol organic solvent solution after the hydrolysis reaction, and between the feeding pump 2 and the liquid storage tank 1 The connecting pipeline is provided with a first control valve 8; the feed port of the vaporizer 3 is connected with the feeding pump 2 for inputting the isoborneol organic solvent solution after the hydrolysis reaction pumped through the feeding pump 2 into the vaporizer 3 for vaporization;

[0057] The heat exchange type radial flow dehydrogenation reactor 4 includes a dehydrogenation reaction chamber 4-1 for carrying out a dehydrogenation r...

Embodiment 2

[0073] Such as Figure 2-3 As shown, a kind of camphor equipment of continuous gas-phase dehydrogenation of isoborneol according to the present invention comprises feeding pump 2, vaporizer 3, heat exchange type radial flow dehydrogenation reactor 4, continuous rectification tower 5, sublimation Kettle 6 and desublimation chamber 7; the feeding pump 2 is connected with the liquid storage tank 1 containing the isoborneol organic solvent solution after the hydrolysis reaction, and between the feeding pump 2 and the liquid storage tank 1 The connecting pipeline is provided with a first control valve 8; the feed port of the vaporizer 3 is connected with the feeding pump 2 for inputting the isoborneol organic solvent solution after the hydrolysis reaction pumped through the feeding pump 2 into the vaporizer 3 for vaporization;

[0074] The heat exchange type radial flow dehydrogenation reactor 4 includes a dehydrogenation reaction chamber 4-1 for carrying out a dehydrogenation rea...

Embodiment 3

[0096] Such as Figure 2-3 As shown, a kind of camphor equipment of continuous gas-phase dehydrogenation of isoborneol according to the present invention comprises feeding pump 2, vaporizer 3, heat exchange type radial flow dehydrogenation reactor 4, continuous rectification tower 5, sublimation Kettle 6 and desublimation chamber 7; the feeding pump 2 is connected with the liquid storage tank 1 containing the isoborneol organic solvent solution after the hydrolysis reaction, and between the feeding pump 2 and the liquid storage tank 1 The connecting pipeline is provided with a first control valve 8; the feed port of the vaporizer 3 is connected with the feeding pump 2 for inputting the isoborneol organic solvent solution after the hydrolysis reaction pumped through the feeding pump 2 into the vaporizer 3 for vaporization;

[0097] The heat exchange type radial flow dehydrogenation reactor 4 includes a dehydrogenation reaction chamber 4-1 for carrying out a dehydrogenation rea...

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to view more

PUM

No PUM Login to view more

Abstract

The invention relates to a device for producing camphor through continuous gas-phase dehydrogenation of isoborneol, comprising a feeding pump, a vaporizer, a heat-exchanging radial flow dehydrogenation reactor, a continuous rectification tower, a sublimation kettle and a desublimation chamber; The feed pump is connected to a liquid storage tank containing the hydrolyzed isoborneol organic solvent solution, and a first control valve is provided on the connecting pipeline between the feed pump and the liquid storage tank. This invention overcomes the shortcomings of the existing isoborneol continuous dehydrogenation method that when the liquid phase enters the fixed bed reactor to prepare camphor, it may cause erosion of the catalyst and affect the service life of the catalyst. It performs dehydrogenation reaction by vaporizing the isoborneol raw material and especially A heat-exchanging radial flow dehydrogenation reactor adapted to it is designed, which has the advantages of continuous production, little impact on the service life of the catalyst, more reasonable distribution of reaction materials, and can greatly improve the production efficiency of the catalyst.

Description

technical field [0001] The invention relates to equipment and a production process for preparing camphor through continuous gas-phase dehydrogenation of isoborneol, which is applied in the field of camphor preparation. Background technique [0002] Camphor is a white crystalline powder with a strong cooling sensation and aromatic smell. It is widely used as pharmaceutical intermediates, environment-friendly anti-moth agents, spices, incense, and industrial raw materials. [0003] Camphor is divided into natural camphor and synthetic camphor, wherein natural camphor is far from meeting the market demand due to lack of resources and small output. Therefore, the process of synthesizing camphor with turpentine as raw material has been greatly developed. The synthesis of camphor takes turpentine as the starting material, and obtains isoborneol through isomerization, esterification and hydrolysis, and then dehydrogenates the isoborneol to finally obtain camphor. At present, ther...

Claims

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to view more

Application Information

Patent Timeline
no application Login to view more
Patent Type & Authority Patents(China)
IPC IPC(8): C07C45/00C07C45/81C07C45/82C07C49/437B01J8/06
CPCB01J8/025B01J8/0278B01J8/06B01J8/067B01J2208/00026C07C45/002C07C45/81C07C45/82C07C49/437
Inventor 江承艳
Owner 福建南平青松化工有限公司
Who we serve
  • R&D Engineer
  • R&D Manager
  • IP Professional
Why Eureka
  • Industry Leading Data Capabilities
  • Powerful AI technology
  • Patent DNA Extraction
Social media
Try Eureka
PatSnap group products