CN202148299U - Volatile oil extraction oil-water separator with condensation - Google Patents
Volatile oil extraction oil-water separator with condensation Download PDFInfo
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- CN202148299U CN202148299U CN201120274241U CN201120274241U CN202148299U CN 202148299 U CN202148299 U CN 202148299U CN 201120274241 U CN201120274241 U CN 201120274241U CN 201120274241 U CN201120274241 U CN 201120274241U CN 202148299 U CN202148299 U CN 202148299U
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- oil
- water separator
- volatile oil
- condensation
- water
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Abstract
The utility model relates to a volatile oil extraction device, in particular to a volatile oil extraction oil-water separator with condensation. The volatile oil extraction oil-water separator with condensation comprises an oil-water separator, and a plug valve is arranged at the bottom of the oil-water separator. The volatile oil extraction oil-water separator with condensation is characterized in that a clamping sleeve is arranged on the oil-water separator; a condensation liquid inlet is arranged at the lower part of the clamping sleeve; a condensation liquid outlet is arranged at the upper part of the clamping sleeve; and a condenser is arranged at the top part of the oil-water separator. With the adoption of the volatile oil extraction oil-water separator with condensation, the oil-water separation can be excellently realized, and the chemical change of the volatile oil caused by high temperature for a long time can be avoided so as to obtain volatile oil with higher quality.
Description
Technical field
The utility model relates to a kind of volatile oil extractor, is a kind of volatile oil stripping oil water separator with condensation specifically.
Background technology
Volatile oil is claimed essential oil again, be one type at normal temperatures can evaporable, can be with steam distillation, with the general name of the not miscible oily liquids of water.Volatile oil is important aroma component in the common important effective constituent, particularly spice berry of natural herbal plant.It also is requisite important component in the essence and flavoring agent industry.
Volatile oil extractor mainly is made up of three parts, and the one, the water-and-oil separator that volatile oil extracts, the 2nd, condensing surface, the 3rd, extraction element.Realize that the principle that volatile oil extracts is that volatile oil steams with water vapor in extraction, the cooling back realizes that in water-and-oil separator oily water separation obtains volatile oil in condensing surface.
Volatile oil extraction system device links to each other with extraction element owing to water-and-oil separator; Because the high temperature that steam brings makes the You Heshui in the water-and-oil separator all be in the condition of high temperature; Therefore traditional volatile oil extraction system device has following disadvantage; The one, the oily water separation under the high temperature is not fine; The 2nd, the decline that change that a series of chemical transformation causes composition causes aroma quality may be because of taking place in volatile oil under the high temperature, the 3rd, be under the high temperature with water for a long time, normal make to volatilize has the boiling smell.The raising day by day of the material requisite of Along with people's, the particularly development of essence and flavoring agent industry, the volatile oil of high quality, former fragrance extracts and will more and more come into one's own.Therefore be necessary to invent a kind of volatile oil stripping oil water separator in order to improve volatile oil extraction quality with condensation.
Summary of the invention
The utility model purpose is exactly to extract the defective of equipment to existing volatile oil, and a kind of volatile oil stripping oil water separator with condensation is provided.It can realize oily water separation better, avoids volatile oil to obtain higher-quality volatile oil because of chemical transformation takes place long-time high temperature.
The technical scheme of the utility model is achieved in that it comprises water-and-oil separator; Stopcock is equipped with in the bottom of water-and-oil separator; It is characterized in that: water-and-oil separator is provided with chuck, and the bottom of chuck is provided with the phlegma import, and the top of chuck is provided with condensate outlet.The utility model technical scheme preferably is that condensing surface is equipped with at the top of described water-and-oil separator.
The utility model can be realized oily water separation better, avoids volatile oil to obtain higher-quality volatile oil because of chemical transformation takes place long-time high temperature.
Description of drawings
Fig. 1 is the structural representation of the utility model;
Fig. 2 is another embodiment synoptic diagram of the utility model;
Embodiment
Below in conjunction with accompanying drawing the utility model is done and to be further described:
As shown in Figure 1, the utility model comprises water-and-oil separator 1, and stopcock 3 is equipped with in the bottom of water-and-oil separator 1, and water-and-oil separator is provided with chuck 2, and the bottom of chuck 2 is provided with phlegma import 5, and the top of chuck is provided with condensate outlet 4.As shown in Figure 2, the utility model technical scheme preferably is that condensing surface 6 is equipped with at the top of described water-and-oil separator.
Connect extraction element by the water-and-oil separator ground during work; Condensing surface is for connecting water-and-oil separator; The loop direction of phlegma is to be flowed into by the import of oily-water seperating equipment phlegma; Flow out the back from the water-and-oil separator condensate outlet and flow into, flow out from the outlet of condenser condenses liquid at last by the import of condenser condenses liquid.
Claims (2)
1. volatile oil stripping oil water separator with condensation; It comprises water-and-oil separator, and stopcock is equipped with in the bottom of water-and-oil separator, it is characterized in that: water-and-oil separator is provided with chuck; The bottom of chuck is provided with the phlegma import, and the top of chuck is provided with condensate outlet.
2. a kind of volatile oil stripping oil water separator with condensation according to claim 1, it is characterized in that: condensing surface is equipped with at the top of described water-and-oil separator.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201120274241U CN202148299U (en) | 2011-07-29 | 2011-07-29 | Volatile oil extraction oil-water separator with condensation |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201120274241U CN202148299U (en) | 2011-07-29 | 2011-07-29 | Volatile oil extraction oil-water separator with condensation |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202148299U true CN202148299U (en) | 2012-02-22 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201120274241U Expired - Fee Related CN202148299U (en) | 2011-07-29 | 2011-07-29 | Volatile oil extraction oil-water separator with condensation |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202148299U (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107677075A (en) * | 2017-09-30 | 2018-02-09 | 吉根林 | It is a kind of that there is the High-efficiency dryer for collecting chrysanthemum steam function |
| CN108403791A (en) * | 2018-03-07 | 2018-08-17 | 浙江工业大学 | A kind of preparation method of the Cortex Moutan extract of high paeonol content |
| CN109224623A (en) * | 2018-10-23 | 2019-01-18 | 段明旭 | A kind of cutting lubricant water separating filter system |
| CN111139136A (en) * | 2018-11-05 | 2020-05-12 | 达凯股份有限公司 | Agilawood processing production line and processing technology thereof |
| CN111139132A (en) * | 2018-11-05 | 2020-05-12 | 达凯股份有限公司 | Emission-free garlic oil production line and production process thereof |
-
2011
- 2011-07-29 CN CN201120274241U patent/CN202148299U/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107677075A (en) * | 2017-09-30 | 2018-02-09 | 吉根林 | It is a kind of that there is the High-efficiency dryer for collecting chrysanthemum steam function |
| CN108403791A (en) * | 2018-03-07 | 2018-08-17 | 浙江工业大学 | A kind of preparation method of the Cortex Moutan extract of high paeonol content |
| CN108403791B (en) * | 2018-03-07 | 2021-05-11 | 浙江工业大学 | Preparation method of cortex moutan extract with high paeonol content |
| CN109224623A (en) * | 2018-10-23 | 2019-01-18 | 段明旭 | A kind of cutting lubricant water separating filter system |
| CN111139136A (en) * | 2018-11-05 | 2020-05-12 | 达凯股份有限公司 | Agilawood processing production line and processing technology thereof |
| CN111139132A (en) * | 2018-11-05 | 2020-05-12 | 达凯股份有限公司 | Emission-free garlic oil production line and production process thereof |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20120222 Termination date: 20140729 |
|
| EXPY | Termination of patent right or utility model |