CN207143201U - A kind of high quality oils tea-seed oil refinement treatment system - Google Patents
A kind of high quality oils tea-seed oil refinement treatment system Download PDFInfo
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- CN207143201U CN207143201U CN201721034830.1U CN201721034830U CN207143201U CN 207143201 U CN207143201 U CN 207143201U CN 201721034830 U CN201721034830 U CN 201721034830U CN 207143201 U CN207143201 U CN 207143201U
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- pipeline
- decolouring
- degumming
- seed oil
- pond
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Abstract
The utility model discloses a kind of high quality oils tea-seed oil refinement treatment system, belong to manufacture camellia seed oil technical field, high quality oils tea-seed oil refinement treatment system, including mechanical admixture remove system, the degumming system being sequentially connected, deacidification system, decolouring system, deodorizing system and point put forward system.The utility model discloses a kind of high quality oils tea-seed oil refinement treatment system.High quality oils tea-seed oil refinement treatment system disclosure satisfy that disclosed in the utility model is handled by a series of systems, completes the process of whole tea-seed oil subtractive process, and can produce the camellia seed oil of high-quality.
Description
Technical field
It the utility model is related to manufacture camellia seed oil technical field, and in particular to a kind of high quality oils tea-seed oil refinement treatment
System.
Background technology
Camellia seed oil also known as camellia oil, it is pure natural advanced woody edible oil.Traditional production is substantially manually to press
Oil expression tea seed is made, and the traditional oil expression instrument in Chinese countryside is wooden crusher, and labor intensity is big, not only needs to consume substantial amounts of people
Power, and it is low to go out oil quality.It gradually will be replaced by hydraulic press and screw machine, but by squeezing the camellia seed oil produced
Impurity can also be contained, oily yield and quality is not high, and the large-scale production of factory also only uses big machinery, together
When substantial amounts of tea seed is squeezed, then filter etc. process, and the processing procedure of neither one system, produce oil tea
The quality of seed oil is not high.
Utility model content
The defects of in order to overcome prior art, technical problem to be solved in the utility model are to propose a kind of high-quality
Camellia seed oil refinement treatment system, it disclosure satisfy that a series of process for systematically completing camellia seed oil subtractive processes, Er Qieneng
Enough produce the camellia seed oil of high-quality.
To use following technical scheme up to this purpose, the utility model：
The utility model provides a kind of high quality oils tea-seed oil refinement treatment system, including the machinery of pipeline connection successively
Impurity removes system, degumming system, deacidification system, decolouring system, deodorizing system and point puies forward system,
The mechanical admixture, which removes system, includes filtering ponds, pressurizer and filter, and the filter is fixed on filtering
The middle part in pond, the pressurizer are arranged on above filter, by pressurizeing impurity mistakes such as some tea seed disintegrating slags in crude oil
Filter out；
The deacidification system includes depickling pipeline, depickling pump, agitator and depickling pond, and described depickling pipeline one end connects
Degumming system bottom, other end connection depickling pond top are connect, the depickling pump is set in depickling pipeline, and the agitator is arranged on
The top in depickling pond, by adding in sodium hydroxide solution and removing the acid in degumming system.
In the utility model preferably technical scheme, the degumming system includes degumming pipeline, degumming pump, degumming pond,
The bottom of degumming pipeline one end connection filtering ponds, the top in other end connection degumming pond, the degumming pump are arranged on degumming
In pipeline, the degumming bottom of pond portion is connected with depickling pipeline one end, slough phosphatide in crude oil, protein jelly mixture and
Other impurity.
In the utility model preferably technical scheme, the decolouring system include decolouring pipeline, decolouring pump, decolouring pond,
Decolouring oxidant layer and decolorizing filter, decolouring pipeline one end connection depickling bottom of pond portion, the other end connect the upper of decolouring pond
Portion, the decolouring pump are arranged in decolouring pipeline, and the decolorizing filter is arranged on decolouring pond bottom, and the decolouring oxidant layer is set
Above decolorizing filter, the pigment in crude oil is removed by decolouring oxidant layer.
In the utility model preferably technical scheme, the decolouring oxidant layer is active carbon layer or albic horizon.
In the utility model preferably technical scheme, the deodorizing system include deodorization pipeline, deodorization valve, destilling tower,
And heater, the deodorization pipeline connection destilling tower and decolouring pond bottom, the deodorization valve is arranged on deodorization pipeline, described
Heater is fixed on distillation tower bottom, removes some and causes low grade aldehyde, ketone, free fatty of grease stink etc..
In the utility model preferably technical scheme, described point carry system include point carrying pipeline, point carry pump, cooling bay,
Cooler, cooling filter and outlet, described point carries pipeline one end and is connected to destilling tower close to the side of bottom, the other end
Connect cooling bay top, described point carries pump and be arranged on and point carry in pipeline, and the cooler is fixed on cooling bay top, the cooling
Filter is fixed on cooling bay bottom, and the outlet is arranged on cooling bay bottom, by grease solid and liquid separation, then by filtering
To high quality oils tea-seed oil.
In the utility model preferably technical scheme, the cooler is water cooled condenser.
The beneficial effects of the utility model are：
High quality oils tea-seed oil refinement treatment system provided by the utility model, it disclosure satisfy that by a series of systems
Reason, system is removed by mechanical admixture, pressurizes and the contaminant filters such as some tea seed disintegrating slags in crude oil is removed；Pass through degumming system
System, sloughs phosphatide in crude oil, the mixture of protein jelly and other impurity；By deacidification system, neutralize and remove degumming system
Acid in system；Pigment in crude oil is removed by the decolouring oxidant layer in decolouring system；By deodorizing system, remove some and cause oil
The low grade aldehyde of fat stink, ketone, free fatty etc.；System is put forward by point, sloughs the mixing of phosphatide in crude oil, protein jelly
Thing and other impurity take off；The process for completing whole tea-seed oil subtractive process, sloughs various impurity, so as to produce high-quality
Camellia seed oil.
Brief description of the drawings
Fig. 1 is the structural representation for the high quality oils tea-seed oil refinement treatment system that the utility model embodiment provides
Figure.
In figure：
11st, pressurizer；12nd, filter；13rd, filtering ponds；21st, degumming pump；22nd, degumming pipeline；23rd, degumming pond；31st, depickling
Pump；32nd, depickling pipeline；33rd, depickling pond；34th, agitator；41st, decolouring pump；42nd, decolouring pipeline；43rd, decolouring pond；44th, decolorising agent
Layer；45th, decolorizing filter；51st, it is deodorized pipeline；511st, it is deodorized valve；52nd, destilling tower；53rd, heater；61st, divide and carry pipeline；62、
Divide and carry pump；63rd, cooling bay；64th, cooling filter；65th, cooler；66th, export.
Embodiment
Further illustrate the technical solution of the utility model below in conjunction with the accompanying drawings and by embodiment.
As shown in figure 1, a kind of high quality oils tea-seed oil refinement treatment system is provided in embodiment, including pipeline connects successively
The mechanical admixture that connects removes system, degumming system, deacidification system, decolouring system, deodorizing system and point puies forward system,
Mechanical admixture, which removes system, includes filtering ponds 13, pressurizer 11 and filter 12, and the filter 12 is fixed
At the middle part of filtering ponds 13, the pressurizer 11 is arranged on the top of filter 12；
Degumming system includes degumming pipeline 22, degumming pump 21, degumming pond 23, the one end of degumming pipeline 22 connection filtering ponds 13
Bottom, the top in other end connection degumming pond 23, degumming pump 21 are arranged in degumming pipeline 22, the bottom of degumming pond 23 and depickling
The one end of pipeline 32 is connected, and degumming system is used to carry out degumming process to camellia seed oil；
Deacidification system includes depickling pipeline 32, depickling pump 31, agitator 34 and depickling pond 33, the one end of depickling pipeline 32
Degumming system bottom, the top of other end connection depickling pond 33 are connected, depickling pump 31 is set in depickling pipeline 32, and agitator 34 is set
At the top in depickling pond 33；
Decolouring system includes decolouring pipeline 42, decolouring pump 41, decolouring pond 43, decolouring oxidant layer 44 and decolorizing filter 45,
The bottom of the one end of decolouring pipeline 42 connection depickling pond 33, the other end connect the top of decolouring pond 43, and decolouring pump 41 is arranged on decolouring pipe
In road 42, decolorizing filter 45 is arranged on the bottom of decolouring pond 43, and decolouring oxidant layer 44 is arranged on the top of decolorizing filter 45, decolorising agent
Layer 44 is active carbon layer, albic horizon or is the decolouring oxidant layer 44 that identical decolorization can be played to camellia seed oil, the present embodiment
In using active carbon layer, decolouring system is used to slough the pigment in camellia seed oil；
Deodorizing system includes deodorization pipeline 51, deodorization valve 511, destilling tower 52 and heater 53, and deodorization pipeline 51 connects
Destilling tower 52 and the bottom of decolouring pond 43, the deodorization valve 511 are arranged on deodorization pipeline 51, and heater 53 is fixed on destilling tower
52 bottoms, deodorizing system are used for except the middle stink impurity that deoils；
Point putting forward system includes point carrying pipeline 61, point carries pump 62, cooling bay 63, cooler 65, cooling filter 64 and go out
Mouthfuls 66, point carry the one end of pipeline 61 and be connected to destilling tower 52 close to the side of bottom, other end connection cooling bay 63 top, point carry pump
62 are arranged on and point carry in pipeline 61, and cooler 65 is water cooled condenser, and cooler 65 is fixed on the top of cooling bay 63, cooled
Filter 64 is fixed on the bottom of cooling bay 63, and outlet 66 is arranged on the bottom of cooling bay 63, divides and puies forward system to improve oleic acid in product
Deng the content of unrighted acid, saturated fatty acid especially hard fatty acids content is reduced.
Camellia seed oil refinement treatment process of the present utility model is as follows：
1. the crude oil that tea seed handles to obtain by squeezing enters from the filtering ponds 13 in mechanical admixture removal system, pass through
Pressurizer 11 is pressurizeed, and accelerates crude oil to pass through filter 12, and the impurity such as some tea seed disintegrating slags in crude oil are removed；
2. the crude oil by filtering enters degumming pipeline 22, by degumming pump 21, crude oil is transported on degumming pond 23
Portion, then toward adding citric acid in degumming pond 23, wherein, crude oil and citric acid are by weight being 1：0.03-0.05, it is fully mixed
After conjunction, slough phosphatide in crude oil, the mixture of protein jelly and other impurity, degummed oil and flow to depickling pipeline 32；
3. degummed oil is transported to the top of depickling pond 33 by depickling pump 31, then toward adding 10% sodium hydroxide in depickling pond 33
Solution, wherein, degummed oil and 10% sodium hydroxide are 1 by weight:0.3-0.5, start agitator 34 and be stirred, neutralization removes
Acid, then depickling oil stream is to decolouring pipeline 42；
4. depickling oil is transported to the top of decolouring pond 43 by decolouring pump 41, depickling oil fully connects with activated carbon decolorizing oxidant layer 44
Stay after touch to decolorizing filter 45, slough pigment, subsequent bleached oil flow direction deodorization pipeline 51；
5. deodorization valve 511 is opened, bleached oil flows into destilling tower 52, the heater of the bottom of destilling tower 52 by being deodorized pipeline 51
53 are begun to warm up, and bleached oil is distilled, and are removed some and are caused low grade aldehyde, ketone, free fatty of grease stink etc., pass through
Arrange the stink substance that can not only remove in deoiling, moreover it is possible to improve oil and fat smoke point, the deodorised oil after distillation, which enters, point to be carried
Pipeline 61；
6. deodorised oil carries pump 62 by dividing, the top of cooling bay 63 is flowed into, cooler 65 starts to cool down deodorised oil
Processing, is cooled to subzero 5 degrees Celsius, grease solid and liquid separation, then obtains high quality oils tea-seed oil by cooling filter 64, high
Quality camellia seed oil flows out from outlet.
The utility model is described with reference to the preferred embodiments, and those skilled in the art know, is not departing from this reality
In the case of with new spirit and scope, various changes or equivalence replacement can be carried out to these features and embodiment.This reality
It is not limited to the particular embodiment disclosed with new, other embodiments fallen into claims hereof all belong to
In the scope of the utility model protection.
Claims (7)
- A kind of 1. high quality oils tea-seed oil refinement treatment system, it is characterised in that：Including pipeline successively connection mechanical admixture remove system, degumming system, deacidification system, decolouring system, deodorizing system, with And divide and put forward system,The mechanical admixture, which removes system, includes filtering ponds, pressurizer and filter, and the filter is fixed on filtering ponds Middle part, the pressurizer are arranged on above filter；The deacidification system includes depickling pipeline, depickling pump, agitator and depickling pond, and depickling pipeline one end connection is de- Colloid system bottom, other end connection depickling pond top, the depickling pump are set in depickling pipeline, and the agitator is arranged on depickling The top in pond.
- 2. high quality oils tea-seed oil refinement treatment system according to claim 1, it is characterised in that：The degumming system bag Degumming pipeline, degumming pump, degumming pond, the bottom of degumming pipeline one end connection filtering ponds are included, the other end connects degumming pond Top, the degumming pump are arranged in degumming pipeline, and the degumming bottom of pond portion is connected with depickling pipeline one end.
- 3. high quality oils tea-seed oil refinement treatment system according to claim 1, it is characterised in that：The decolouring system bag Decolouring pipeline, decolouring pump, decolouring pond, decolouring oxidant layer and decolorizing filter are included, described decolouring pipeline one end connects depickling bottom of pond Portion, the other end connect the top of decolouring pond, and the decolouring pump is arranged in decolouring pipeline, and the decolorizing filter is arranged on decolouring Pond bottom, the decolouring oxidant layer are arranged on above decolorizing filter.
- 4. high quality oils tea-seed oil refinement treatment system according to claim 3, it is characterised in that：The decolouring oxidant layer is Active carbon layer or albic horizon.
- 5. high quality oils tea-seed oil refinement treatment system according to claim 1, it is characterised in that：The deodorizing system bag Deodorization pipeline, deodorization valve, destilling tower and heater, the deodorization pipeline connection destilling tower and decolouring pond bottom are included, it is described de- Smelly valve is arranged on deodorization pipeline, and the heater is fixed on distillation tower bottom.
- 6. high quality oils tea-seed oil refinement treatment system according to claim 1, it is characterised in that：Described point carries system bag Include and point carry pipeline, point propose pump, cooling bay, cooler, cooling filter and outlet, described point carries pipeline one end and be connected to steaming Tower is evaporated close to bottom sides, other end connection cooling bay top, and described point carries pump and be arranged on and point carry in pipeline, and the cooler is consolidated Cooling bay top is scheduled on, the cooling filter is fixed on cooling bay bottom, and the outlet is arranged on cooling bay bottom.
- 7. high quality oils tea-seed oil refinement treatment system according to claim 6, it is characterised in that：The cooler is water Air-cooled condenser.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721034830.1U CN207143201U (en) | 2017-08-17 | 2017-08-17 | A kind of high quality oils tea-seed oil refinement treatment system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721034830.1U CN207143201U (en) | 2017-08-17 | 2017-08-17 | A kind of high quality oils tea-seed oil refinement treatment system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207143201U true CN207143201U (en) | 2018-03-27 |
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ID=61665782
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721034830.1U Expired - Fee Related CN207143201U (en) | 2017-08-17 | 2017-08-17 | A kind of high quality oils tea-seed oil refinement treatment system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207143201U (en) |
-
2017
- 2017-08-17 CN CN201721034830.1U patent/CN207143201U/en not_active Expired - Fee Related
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| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20180327 Termination date: 20190817 |
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| CF01 | Termination of patent right due to non-payment of annual fee |