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New method for producing dihydromyrcene

A technology of dihydromyrcene and pyrolysis products, which is applied in the field of chemical technology, can solve the problems of increased system operating costs, waste of energy, and the need for cooling media, and achieve low production energy consumption and cost, reduced production costs, and full utilization of heat energy Effect

Active Publication Date: 2012-12-26
FUZHOU UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Hydrogenate α-pinene to produce α-pinene, and then undergo thermal isomerization to obtain dihydromyrcene, but the isomerization product of α-pinene is a mixture of various terpenes, and its boiling point difference is very small , and there are unreacted cis-pinane and trans-pinane, because the boiling points of pinane and dihydromyrcene are very close, it is difficult to separate by rectification
If in order to improve the conversion rate of pinane, then the selectivity of generating dihydromyrcene is reduced again, causing the separation difficulty of by-product and dihydromyrcene
The high temperature reaction product from the cracking furnace must be cooled and condensed into the refining tower. If this part of heat is directly exchanged with the cooling medium, it will not only waste energy but also require cooling medium, which will increase the operating cost of the system.

Method used

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  • New method for producing dihydromyrcene

Examples

Experimental program
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Effect test

Embodiment 1

[0016] The cracking furnace temperature is controlled at 500°C, the raw material pinane is mixed with the pinane recycled from the refining tower, and then it is preheated to 450°C and then enters the cracking furnace with a space velocity of 0.1 mol·ml-1·h-1, the single-pass conversion of pinane cracking The rate is 35%, the total conversion rate is 100%, and the selectivity of generating diclear myrcene is 83%. The pressure of the two-purity myrcene refining tower is controlled at 2-10kPa, and the concentration of dihydromyrcene obtained at the top of the tower can reach more than 85%. Using pyrolysis products to exchange heat with raw materials can save heat. The remaining steps are as described in the detailed description.

Embodiment 2

[0018] The cracking furnace temperature is controlled at 500°C, the raw material pinane is mixed with the pinane recycled from the refining tower, and then it is preheated to 450°C and then enters the cracking furnace with a space velocity of 0.128mol·ml-1·h-1, the single-pass conversion of pinane cracking The rate is 55%, the total conversion rate is 100%, and the selectivity of generating diclear myrcene is 83%. The pressure of the two-purity myrcene refining tower is controlled at 2-10kPa, and the concentration of dihydromyrcene obtained at the top of the tower can reach more than 85%. The remaining steps are as described in the detailed description.

Embodiment 3

[0020] The cracking furnace temperature is controlled at 520°C, the raw material pinane is mixed with the pinane recycled from the refining tower, and then it is preheated to 450°C and then enters the cracking furnace with a space velocity of 0.1mol·ml-1·h-1, the single-pass conversion of pinane cracking The rate is 65%, the total conversion rate is 100%, and the selectivity of generating diclear myrcene is 80%. The pressure of the two-purity myrcene refining tower is controlled at 2-10kPa, and the concentration of dihydromyrcene obtained at the top of the tower can reach more than 85%. The remaining steps are as described in the detailed description.

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Abstract

The invention discloses a new method for producing dihydromyrcene through partial thermal isomerization of pinane, which mainly comprises the following steps of: performing partial thermal isomerization on the pinane in a cracking furnace to generate the dihydromyrcene, performing heat exchange between the dihydromyrcene, unreacted pinane and a reaction byproduct out of the cracking furnace and a raw material pinane entering the cracking furnace, and making the dihydromyrcene, unreacted pinane and the reaction byproduct enter a rectifying tower for rectification; and after the rectification of the rectifying tower, obtaining the pure dihydromyrcene on the tower top, obtaining heavy components on the bottom of the tower, extracting pinane-containing streams with high concentration from the side of the rectifying tower and returning the pinane-containing streams serving as a raw material for thermal isomerization. The method has the advantages that: a partial cracking-rectifying separation process is adopted to improve the selectivity (over 80 percent ) of generating the dihydromyrcene, which is improved by about 10 percent than that under the condition of single-pass overall conversion; meanwhile, the high-temperature materials at the outlet of the cracking furnace exchange heat with the raw material pinane, the heat of the system is fully utilized, and the energy consumption of the whole system is reduced.

Description

technical field [0001] The invention belongs to the field of chemical technology, and in particular relates to a method for producing dihydromyrcene by using pinane as a raw material. Background technique [0002] Pinane (2,6,6-trimethylbicyclo[3.1.1]heptane) is a monoterpene compound, which is obtained by hydrogenation of pinene in turpentine oil, and the main product di Hydrogen myrcene (Dihydromene, also known as dihydromyrcene) is a good intermediate for the synthesis of fragrances and medicines. It is of great significance to study the synthesis of its downstream products from dihydromyrcene, the main product of pinane cracking, for the comprehensive utilization of my country's rich turpentine resources. Hydrogenate α-pinene to produce α-pinene, and then undergo thermal isomerization to obtain dihydromyrcene, but the isomerization product of α-pinene is a mixture of various terpenes, and its boiling point difference is very small , and there are unreacted cis-pinane a...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C07C11/12C07C5/31C07C7/04
Inventor 郑辉东吴燕翔邱挺黄智贤李玲
Owner FUZHOU UNIV
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