CN202322775U - Camellia oil purification system - Google Patents
Camellia oil purification system Download PDFInfo
- Publication number
- CN202322775U CN202322775U CN2011203936373U CN201120393637U CN202322775U CN 202322775 U CN202322775 U CN 202322775U CN 2011203936373 U CN2011203936373 U CN 2011203936373U CN 201120393637 U CN201120393637 U CN 201120393637U CN 202322775 U CN202322775 U CN 202322775U
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- China
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- tea oil
- purification system
- camellia oil
- reaction device
- oil
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Abstract
The utility model provides a camellia oil purification system and adopts the technical scheme that the camellia oil purification system is characterized by comprising a crude camellia oil pre-filtering device, a dephosphorization reactor and a salt water feeder, wherein the outlets of both the crude camellia oil pre-filtering device and the salt water feeder face to the inlet of the dephosphorization reactor. According to the technical scheme, large dregs in crude camellia oil are filtered out through pre-filtering treatment, then the crude camellia oil enters the dephosphorization reactor, and at the moment, salt water is fed into the dephosphorization reactor for reaction so as to remove phospholipid, protein and sticky matter in the crude camellia oil; then the crude camellia oil stands for a span, and an oil layer and a water layer are separated after oil-water separation; and finally, the oil layer is sent to a refining workshop, so as to obtain refined camellia oil product. The camellia oil purification system can effectively purify the crude camellia oil, so that the quality, the purity and the transparency of the refined camellia oil product are greatly improved.
Description
Technical field
The utility model relates to a kind of purification system of tea oil.
Background technology
Tea oil is obtained through squeezing processing by tea seed, wherein also contains a large amount of slags in the thick tea oil after the squeezing processing, need do the filtration pre-treatment to it, so that follow-up process operation.Generally only thick tea oil is done simple filtering in the tradition workshop and handle, also contain a large amount of suspended substances in its product in fact, this has not only influenced the quality of product, has also influenced product gas purity and brightness.
Summary of the invention
The purpose of the utility model provides a kind of purification system of tea oil.
To achieve these goals; The technical scheme that the utility model adopted is: a kind of purification system of tea oil; It is characterized in that: described purification system comprises thick tea oil pre-filtrating equipment, dephosphorisation reaction device, salt solution feeder, and the outlet of said thick tea oil pre-filtrating equipment and salt solution feeder is all towards the import of dephosphorisation reaction device.
Can be known by above-mentioned technical scheme: thick tea oil is handled through pre-filtering big slag is wherein removed by filter; Get into the dephosphorisation reaction device then, the salt solution feeder joined salt solution in the dephosphorisation reaction device and reacted this moment, was stained with material with phosphatide, protein, the glue removed wherein; Then leave standstill for some time; After the profit layering, oil reservoir and water layer are separated, last oil reservoir arrives refining workshop and obtains finished product tea oil.This purification system can be carried out purifying treatment to thick tea oil effectively, and this has improved the quality of tea oil finished product greatly, and its purity and transparency have also obtained very big improvement simultaneously.
Description of drawings
Fig. 1 is the utility model synoptic diagram.
Embodiment
A kind of purification system of tea oil, as shown in Figure 1: described purification system comprises thick tea oil pre-filtrating equipment, dephosphorisation reaction device 20, salt solution feeder 30, the outlet of said thick tea oil pre-filtrating equipment and salt solution feeder 20 is all towards the import of dephosphorisation reaction device 30.Thick tea oil is added in the pre-filtrating equipment in the thick tea oil storage tank 14, handles that through pre-filtering big slag is wherein removed by filter, and gets into dephosphorisation reaction device 20 then; Salt solution feeder 30 joined salt solution in the dephosphorisation reaction device 20 and reacted this moment; Phosphatide, protein, glue to remove wherein are stained with material, then leave standstill for some time, after the profit layering; Oil reservoir and water layer are separated, and last oil reservoir arrives refining workshop and obtains finished product tea oil.This purification system can be carried out purifying treatment to thick tea oil effectively, and this has improved the quality of tea oil finished product greatly, and its purity and transparency have also obtained very big improvement simultaneously.
Described dephosphorisation reaction device 20 bottoms are connected with export pipeline 22, and said export pipeline 22 is provided with the take-off pipe 23 and first valve 24, and described take-off pipe 23 is provided with second valve 25 and described take-off pipe 23 is nearest from dephosphorisation reaction device 20.Reaction is left standstill for some time after finishing in the dephosphorisation reaction device 20, closes second valve 25 then, opens first valve 24; The water layer that is positioned at dephosphorisation reaction device 20 bottoms just gets into export pipeline 22 by outlet 21, is discharged from and is collected by holding tank 28, then closes first valve 24; Open second valve 25; Superposed tea oil layer just gets into export pipeline 22 by outlet 21, and gets into oil outlet pipe 23 arrival storage tank 27, obtains finished product tea oil at last by the processing of refining workshop.
Described thick tea oil pre-filtrating equipment comprises two filtering units 10 at least, and described filtering unit 10 comprises the wire netting 15 and filter cloth 11 that is positioned at its inside and is arranged in parallel, and described wire netting 15 is arranged on the top of filter cloth 11.Be the wire netting 15 that is provided with in the filtering unit 10, can slag in the coarse tea oil be held back that the filter cloth 11 that further via hole diameter is small then filters, tea oil has basically just obtained good pre-filtering processing like this, and gets into next operation via pipeline 13.
The outlet of described thick tea oil pre-filtrating equipment and salt solution feeder 30 is communicated with the import of dephosphorisation reaction device 20.
Described salt solution feeder 30 is provided with first liquidometer 32 and TM 31.So just can control the brinish addition and control its temperature, the phosphatide in the tea oil, protein, glue are stained with material remove effect completely to reach.
Described dephosphorisation reaction device 20 was communicated with the pipe that can monitor its inner liquid level 29.Profit just can be monitored through the pipe 29 pairs of thick dephosphorisation reaction devices 20 interior materials that are communicated with dephosphorisation reaction device 20, and measure the height of its liquid level when being separated like this, is beneficial to control oily water separation operation.
Described dephosphorisation reaction device 20 is provided with second liquidometer 26 with export pipeline 22 junctions.Second liquidometer 26 can be convenient to the workman and observe the liquid level in the dephosphorisation reaction device 20, is beneficial to the process operation that adds material or blowing.
Described filtering unit 10 is 2.Satisfied so on the one hand and improved the requirement that tea oil filters the operating speed of processing, also be convenient on the other hand fast filter cake disposed to carry out filter operation next time.
Described dephosphorisation reaction device 20 bottoms are cone structure.Such structure is according to hydrodynamic characteristic design, and outlet is the closing in shape, and profit can be easily be separated the water layer bottom being positioned at after layering like this, has also avoided oil reservoir to sneak in the water layer again and separated together.
Claims (9)
1. the purification system of a tea oil; It is characterized in that: described purification system comprises thick tea oil pre-filtrating equipment, dephosphorisation reaction device (20), salt solution feeder (30), and the outlet of said thick tea oil pre-filtrating equipment and salt solution feeder (20) is all towards the import of dephosphorisation reaction device (30).
2. the purification system of a kind of tea oil according to claim 1; It is characterized in that: described dephosphorisation reaction device (20) bottom is connected with export pipeline (22); Said export pipeline (22) is provided with take-off pipe (23) and first valve (24), and described take-off pipe (23) is provided with second valve (25) and described take-off pipe (23) is nearest from dephosphorisation reaction device (20).
3. the purification system of a kind of tea oil according to claim 1; It is characterized in that: described thick tea oil pre-filtrating equipment comprises two filtering units (10) at least; Described filtering unit (10) comprises wire netting (15) and the filter cloth (11) that is positioned at its inside and is arranged in parallel, and described wire netting (15) is arranged on the top of filter cloth (11).
4. the purification system of a kind of tea oil according to claim 1, it is characterized in that: the outlet of described thick tea oil pre-filtrating equipment and salt solution feeder (30) is communicated with the import of dephosphorisation reaction device (20).
5. the purification system of a kind of tea oil according to claim 1 is characterized in that: described salt solution feeder (30) is provided with first liquidometer (32) and TM (31).
6. the purification system of a kind of tea oil according to claim 1, it is characterized in that: described dephosphorisation reaction device (20) was communicated with the pipe that can monitor its inner liquid level (29).
7. the purification system of a kind of tea oil according to claim 1 and 2 is characterized in that: described dephosphorisation reaction device (20) is provided with second liquidometer (26) with export pipeline (22) junction.
8. the purification system of a kind of tea oil according to claim 3, it is characterized in that: described filtering unit (10) is 2.
9. according to the purification system of claim 1 or 4 described a kind of tea oil, it is characterized in that: described dephosphorisation reaction device (20) bottom is cone structure.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011203936373U CN202322775U (en) | 2011-10-17 | 2011-10-17 | Camellia oil purification system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011203936373U CN202322775U (en) | 2011-10-17 | 2011-10-17 | Camellia oil purification system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202322775U true CN202322775U (en) | 2012-07-11 |
Family
ID=46434762
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011203936373U Expired - Fee Related CN202322775U (en) | 2011-10-17 | 2011-10-17 | Camellia oil purification system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202322775U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106433968A (en) * | 2016-11-24 | 2017-02-22 | 耒阳市金鑫农业科技发展有限公司 | Camellia oil purifying system |
-
2011
- 2011-10-17 CN CN2011203936373U patent/CN202322775U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106433968A (en) * | 2016-11-24 | 2017-02-22 | 耒阳市金鑫农业科技发展有限公司 | Camellia oil purifying system |
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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: 20120711 Termination date: 20141017 |
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| EXPY | Termination of patent right or utility model |