CN204079936U - For the continous way Decolouring pot of vegetable oil refining - Google Patents
For the continous way Decolouring pot of vegetable oil refining Download PDFInfo
- Publication number
- CN204079936U CN204079936U CN201420582749.7U CN201420582749U CN204079936U CN 204079936 U CN204079936 U CN 204079936U CN 201420582749 U CN201420582749 U CN 201420582749U CN 204079936 U CN204079936 U CN 204079936U
- Authority
- CN
- China
- Prior art keywords
- decolouring pot
- pot body
- decolouring
- vegetable oil
- oil refining
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
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Abstract
The utility model relates to a kind of continous way Decolouring pot for vegetable oil refining, belong to vegetable oil refining decoloring equipment, comprise Decolouring pot body and lower Decolouring pot body, this technical essential is that Decolouring pot body and lower Decolouring pot body are welded to connect, upper Decolouring pot body is connected by oil pipe with lower decolouring pot nside, oil pipe has a Valve controlling switch, the inwall that upper Decolouring pot body contacts with lower Decolouring pot body has an overflow port, and a vacuum port is arranged at upper Decolouring pot body top.The utility model compared with prior art, has multiple function, and equipment investment cost reduces, decolorizing effect is strengthened, advantage easy and simple to handle.
Description
Technical field
The utility model relates to a kind of continous way Decolouring pot for vegetable oil refining, belongs to vegetable oil refining decoloring equipment.
Background technology
Decolouring pot is the necessaries of vegetable oil refining bleaching process, and the Decolouring pot of current high yield is all adopt steam-stirring, and it is large that steam-stirring consumes steam energy; Because bleaching process needs to run under vacuum conditions, the steam that steam-stirring sprays into need by vacuum system by its sucking-off, energy repeat consumption is caused to increase the load of vacuum system thus increase production cost, also need to be equipped with pre-mixing step, equipment investment is large and operating procedure is more complicated, steam-stirring dead angle is more simultaneously causes the quality of decolouring atlapulgite precipitation impact oil: adopt conventional mechanical stirring to be only suitable for intermittent processing, air-teturning mixed phenomenon is serious, be difficult to ensure that grease obtains the time of decolouring uniformly, be not suitable for the consecutive production of high yield.
Utility model content
The purpose of this utility model is to provide a kind of continous way Decolouring pot for vegetable oil refining, comprises Decolouring pot body and lower Decolouring pot body, and upper Decolouring pot body and lower Decolouring pot body are welded to connect, and stopping property is better.Upper Decolouring pot body is connected by oil pipe with lower decolouring pot nside, oil pipe has a Valve controlling switch, production control amount and bleaching time.The inwall that upper Decolouring pot body contacts with lower Decolouring pot body there is a ventage (ventage doubles as overflow port), avoid to the full extent because careless manipulation or other reasons cause mixing oil to occur through the situation of vacuum system sucking-off, and a vacuum port is arranged at upper Decolouring pot body top.
The external wall of described Decolouring pot has an open steam entrance, and open steam entry position, higher than lattice storehouse height, prevents grease from blowing back into steam-pipe, and lower Decolouring pot body is divided into 2-20 lattice storehouse.
The utility model compared with prior art, has following beneficial effect:
Structure is simple, reduced investment, good seal performance, be convenient to keep the vacuum tightness needed for decolouring, be convenient to control output and bleaching time by the liquid level in oil inlet quantity and equipment, easily reach best decolorizing effect, simplify decoloration process, reduce air-teturning mixed phenomenon during decolouring, grease can obtain corresponding bleaching time more uniformly.
Accompanying drawing illustrates:
Fig. 1, the utility model one implement structural representation.
In figure: 1, step-down gear, 2, manhole, 3, vacuum port, 4, oil weir, 5, upper Decolouring pot body, 6, overflow port, 7, visor, 8, Valve controlling switch, 9, visor, 10, open steam entrance, 11, oil outlet, 12, oil-in, 13, carclazyte entrance, 14, baffle plate, 15, blade, 16, lower Decolouring pot body, 17, Ge Cang, 18, feed opening.
Embodiment
Below in conjunction with embodiment, the utility model is further described:
As shown in the figure, a kind of continous way Decolouring pot for vegetable oil refining described by the utility model, after metering, grease is transported to oil-in 12 after interchanger is heated to 95-125 degree Celsius, mix with the carclazyte discoloring agent quantitatively added, in upper Decolouring pot body 5, by speed reduction unit 1, grease and carclazyte are reached mix decolouring fully, mixing oil flows into lower Decolouring pot body 16 by upper and lower two interlayer valves 8, carry out second time decolouring, open steam entrance 10 is utilized to be uniformly mixed, grease successively flows into last storehouse from first storehouse in lattice storehouse 17, the bottom of lower pot body 16 is flow into from last warehouse bottom feed opening 18, pump into decolorization filtering machine through oil outlet 11 by decolouring pump and complete whole decolorization.
In sum, the utility model simplifies decoloration process, makes decolouring easier, and reduce air-teturning mixed phenomenon during decolouring, grease can obtain corresponding bleaching time more uniformly.
Claims (3)
1. the continous way Decolouring pot for vegetable oil refining, comprise Decolouring pot body (5) and lower Decolouring pot body (16), it is characterized in that Decolouring pot body (5) and lower Decolouring pot body (16) are welded to connect, upper Decolouring pot body (5) is connected by oil pipe with lower Decolouring pot body (16) inside, oil pipe there is a Valve controlling switch (8), the inwall that upper Decolouring pot body (5) contacts with lower Decolouring pot body (16) has an overflow port (6), and a vacuum port (3) is arranged at upper Decolouring pot body top.
2. the continous way Decolouring pot for vegetable oil refining according to claim 1, is characterized in that lower Decolouring pot body (16) is divided into 2-20 lattice storehouse (17).
3. the continous way Decolouring pot for vegetable oil refining according to claim 1, is characterized in that lower Decolouring pot body (16) outer wall has an open steam entrance (10).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420582749.7U CN204079936U (en) | 2014-10-10 | 2014-10-10 | For the continous way Decolouring pot of vegetable oil refining |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420582749.7U CN204079936U (en) | 2014-10-10 | 2014-10-10 | For the continous way Decolouring pot of vegetable oil refining |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204079936U true CN204079936U (en) | 2015-01-07 |
Family
ID=52172672
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420582749.7U Expired - Fee Related CN204079936U (en) | 2014-10-10 | 2014-10-10 | For the continous way Decolouring pot of vegetable oil refining |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204079936U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107502447A (en) * | 2017-10-12 | 2017-12-22 | 太湖县纯野生态茶油有限责任公司 | Continuous operating camellia oil is segmented decoloration device and its application method |
-
2014
- 2014-10-10 CN CN201420582749.7U patent/CN204079936U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107502447A (en) * | 2017-10-12 | 2017-12-22 | 太湖县纯野生态茶油有限责任公司 | Continuous operating camellia oil is segmented decoloration device and its application method |
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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: 20150107 Termination date: 20151010 |
|
| EXPY | Termination of patent right or utility model |