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Litsea cubeba oil distillation separation equipment and technology

A technology for separation and distillation of Radix japonica oil, applied in the directions of essential oils/spices, fat production, etc., can solve the problems of affecting yield and quality, simple distillation kettle, boiler heat loss, etc., to improve oil yield and distillation speed. , avoid scalding the operator, improve the effect of thermal energy utilization

Inactive Publication Date: 2017-01-25
YONGZHOU SAMSHIANG FLAVOURS & FRAGRANCES CORP
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, the quality and color of litsea cubeba crude oil vary greatly from place to place, and the content of citral in it ranges from 58-75%, which increases the process and difficulty of subsequent finishing
[0004] The difference in the quality of litsea cubeba crude oil is mainly due to the simplicity and backwardness of the distillation equipment for the primary processing of litsea cubeba oil. The main problems are as follows: (1) poor equipment, defects in equipment structure, safety, etc. , pressure and other parameters to adjust the process in time and standardize the operation process, resulting in the lag of adjustment affecting the yield and quality; (2) most of the distillation equipment is made of carbon steel, which is easy to rust, which not only affects the production The color and quality of Litsea Cubeba Oil have a negative impact, and the thinning of distillation equipment and pipelines due to corrosion is likely to cause serious safety accidents; (3) there is a large loss and waste of heat generated by the boiler, and the waste water produced by the process is relatively large. Many; (4) The oil-water separation equipment is currently in the shape of a cuboid, and the oil-water boundary cannot be seen, and the oil layer cannot be effectively collected, and more water and other impurities are collected, which reduces the efficiency and increases the subsequent dehydration and impurity removal process; (5) The distillation kettle is simple and poor in terms of sealing and safety. Especially when many oil farmers use boilers of 1 steam ton, 2 steam tons, and 4 steam tons to supply heat, higher requirements are put forward for distillation equipment and safe operation. requirements
[0005] Due to the uneven technical level of various oil farmers, non-standard operating processes, and insufficient equipment management and safety management, the oil yield and quality are unstable, which not only affects the benefits of oil farmers, but also improves the follow-up quality of litsea cubeba oil. processing cost
With the changes in the industry, small-scale oil farmers have decreased, and large-scale processing households have gradually formed. However, equipment, technology, and safety have not been followed up in time, which is very unfavorable for the healthy development of the litsea cubeba oil industry.

Method used

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  • Litsea cubeba oil distillation separation equipment and technology
  • Litsea cubeba oil distillation separation equipment and technology

Examples

Experimental program
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Effect test

Embodiment

[0054] see figure 1 , a Litsea cubeba oil distillation and separation process in the illustration is a preferred embodiment of the present invention, specifically including a distillation kettle 1, an air guide channel 2, a condenser 3, a primary oil-water separator 41 and a secondary oil-water separator in series in sequence. Separator 42.

[0055] The heating method of the still 1 includes two kinds of external heating and internal direct heating. A jacket 11 is wrapped around the body of the still 1. The jacket 11 is an inner hollow channel wrapped on the outer surface of the still. At the bottom of the jacket 11 A jacket inlet 111 is provided, and a jacket outlet 112 is provided on the top of the jacket 11 for circulating heating medium into the inner cavity of the jacket.

[0056] The heating medium includes heat transfer oil and steam, and a steam safety valve 113 is provided on the jacket 11 for pressure protection when steam is introduced into the jacket.

[0057] Th...

Embodiment 2

[0073] The present embodiment adopts the litsea cubeba oil distillation and separation equipment in embodiment 1 to carry out the processing of litsea cubeba oil, and its technology includes following three kinds according to the difference of distillation mode:

[0074] 1. Direct steam-water distillation

[0075] Put the picked litsea cubeba in a cool place, if it cannot be distilled in time, it can be impregnated with 20% salt and stored in a cool airtight container.

[0076] (1) First put fresh or salt-impregnated Litsea cubeba into the distillation still in Example 1, and add pure water, the weight ratio of Litsea cubeba raw material to pure water is 1: 1-2.

[0077] (2) Open the steam pipe in the kettle of the still to feed steam, and open the condenser at the same time. Since the high-temperature steam directly introduced will partly turn into water, observe the liquid level in the kettle through the pressure-resistant sight glass of the kettle body, and pay attention t...

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Abstract

The invention discloses litsea cubeba oil distillation separation equipment and a technology. The litsea cubeba oil distillation separation equipment comprises a distillation still, a condenser and oil-water separators, wherein the distillation still, the condenser and the oil-water separators are connected in series; a jacket covers the outside of the distillation still; heating media are introduced into the jacket; the inside of the distillation still is also connected with a steam pipeline in the distillation still, and external normal pressure heating distillation and internal pressurization heating distillation can be respectively realized; the top of the distillation still is provided with a distillation column section, and the distillation column section is connected with the inlet of the condenser through an inclined air duct; the oil-water separators are in two-stage serial connection, wherein the oil-water feeding hole of the first-stage oil-water separator is connected with the outlet of the condenser, the oil-water feeding hole of the second-stage oil-water separator is connected with the water outlet of the first-stage oil-water separator, and the water outlet of the second-stage oil-water separator is connected with a storage tank through a pump. According to different specification requirements of litsea cubeba essential oil, underwater distillation and overwater distillation are realized, pressurization distillation also can be realized, heat energy use ratio is high, energy consumption is lowered by 5-10%, a wastewater quantity is reduced by 10-30%, and the oil extraction rate and the quality of the litsea cubeba essential oil can be improved.

Description

technical field [0001] The invention relates to litsea cubeba oil distillation and separation equipment and technology, which belongs to oil distillation production technology. Background technique [0002] The main ingredient in litsea cubeba oil is citral, which is used to formulate natural citrus and lemon flavors. The annual output of litsea cubeba oil is about 800-1000 tons, and a large amount of litsea cubeba oil and natural citral are exported in my country every year. [0003] The traditional litsea cubeba oil processing method is to obtain the litsea cubeba fruit through steam distillation, such as the technical scheme recorded in the Chinese patent application document with the publication number CN104120036A, the oil farmer concentrates the litsea cubeba crude oil obtained by distillation It is sold to a large-scale Litsea cubeba oil fine processing company to refine natural citral and standardized Litsea cubeba essential oil. However, the quality and color of l...

Claims

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Application Information

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IPC IPC(8): C11B9/02
CPCC11B9/027C11B9/022
Inventor 薛金春李维虎余杰坤张宁
Owner YONGZHOU SAMSHIANG FLAVOURS & FRAGRANCES CORP
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