Myrcene production system

A production system, myrcene technology, applied in distillation separation, organic chemistry, organic chemical methods, etc., can solve the problems of high energy consumption, low output, high production cost, etc., and achieve the goal of improving fractionation effect, reducing cost, and reducing energy consumption Effect

Active Publication Date: 2016-09-28
江西省吉水县兴华天然香料有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

In recent years, researchers have done more research on myrcene production methods, but less research on its production equipment
In the device for cracking β-pinene to produce myrcene, there are still problems such as high energy consumption, high production cost, uneven heating, low output, and long reaction time.

Method used

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Experimental program
Comparison scheme
Effect test

Embodiment 1

[0024] refer to figure 1 The production system of a kind of myrcene shown comprises successively connected α-pinene fractionation tower 6, β-pinene fractionation tower 9, preheater 1, cracker 2, cooler 3, vacuum buffer tank 4, vacuum Receiving tank 5, vacuum gas storage tank 8 and vacuum pump 7, the feed port of described β-pinene fractionation tower 9 is connected with the β-pinene mother liquor outlet of described α-pinene fractionation tower 6, and described pre- The feed port 103 of the heater 1 is connected with the β-pinene discharge port 904 of the β-pinene fractionation tower 9, and the feed port 104 of the preheater 1 is connected with the feed port of the cracker 2 201 is connected through a first pipeline 203, the outlet 202 of the cracker 2 is connected with the feed inlet 303 of the cooler 3 through a second pipeline 204, and the first pipeline 203 and the second pipeline 204 are jointly wrapped with Insulation layer 205.

[0025]The α-pinene fractionation tower...

Embodiment 2

[0029] refer to figure 1 The production system of a kind of myrcene shown comprises successively connected α-pinene fractionation tower 6, β-pinene fractionation tower 9, preheater 1, cracker 2, cooler 3, vacuum buffer tank 4, vacuum Receiving tank 5, vacuum gas storage tank 8 and vacuum pump 7, the feed port of described β-pinene fractionation tower 9 is connected with the β-pinene mother liquor outlet of described α-pinene fractionation tower 6, and described pre- The feed port 103 of the heater 1 is connected with the β-pinene discharge port 904 of the α-pinene fractionation tower 9, and the feed port 104 of the preheater 1 is connected with the feed port of the cracker 2 201 is connected through the first pipeline 203, the outlet 202 of the cracker 2 is connected with the feed inlet 303 of the cooler 3 through the second pipeline 204, and the first pipeline 203 and the second pipeline 204 are jointly wrapped with Insulation layer 205.

[0030] The α-pinene fractionation ...

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PUM

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Abstract

The invention discloses a myrcene production system, comprising an alpha-pinene fractionator, a beta-pinene fractionator, a preheater, a pyrolytic device, a cooler, a vacuum buffer tank, a vacuum receiving tank, a vacuum gas storage tank and a vacuum pump; a feed port of the beta-pinene fractionator is connected with a beta-pinene mother liquid outlet of the alpha-pinene fractionator, a feed port of the preheater is connected with a beta-pinene discharge port of the beta-pinene fractionator, a discharge port of the preheater is connected with a feed port of the pyrolytic device through a first pipeline, a discharge port of the pyrolytic device is connected with a feed port of the cooler through a second pipeline, and the first pipeline and the second pipeline are jointly covered with an insulation layer. The multistage fractionators used herein cooperate with reflux action of a reflow pipe by means of multistage spraying, providing greatly improved fractionating effect, improving the purity of beta-pinene obtained by isolating and therefore ensuring the purity of finally isolated myrcene.

Description

technical field [0001] The invention relates to a production device in the field of fine chemical industry, in particular to a production system of myrcene. Background technique [0002] Myrcene is also known as myrcene, 7-methyl-3-methylene-1,6-octadiene, etc. Its molecular formula is: C10H16, its molecular weight is 136.23, and there are two conjugated double bonds and one single A double bond is an important chemical raw material and intermediate in the fragrance industry, such as the synthesis of mint, citral, citronellol, geraniol, nerol and linalool. Myrcene is a colorless or light yellow oily liquid at room temperature, soluble in organic solvents such as ethanol, ether, and chloroform, and miscible with most spice intermediates. Myrcene has a strong fruity, floral, green, woody and lemony aroma. Because of its unique aroma quality, it is widely used in medicine, tobacco, food ingredients, perfume, cosmetics, soap, detergent and other fields. There are two ways to o...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C13/40C07C13/42C07C7/04C07C11/21C07C5/31B01D3/14B01D3/32
CPCB01D3/143B01D3/32C07B2200/09C07C5/31C07C7/04C07C13/40C07C13/42C07C11/21
Inventor 张亲春
Owner 江西省吉水县兴华天然香料有限公司
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