CN207210364U - A kind of lossless edible oil deacidifying device - Google Patents
A kind of lossless edible oil deacidifying device Download PDFInfo
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- CN207210364U CN207210364U CN201721064293.5U CN201721064293U CN207210364U CN 207210364 U CN207210364 U CN 207210364U CN 201721064293 U CN201721064293 U CN 201721064293U CN 207210364 U CN207210364 U CN 207210364U
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- edible oil
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Abstract
A kind of lossless edible oil deacidifying device, it is related to a kind of deacidifying device of high acid value grease, the problem of lipase loss is larger, cost is higher, causes deacidifying process production cost higher be present to solve existing lipase deacidification technique.The utility model includes heating in vacuum boiling agitator tank (1), gas reservoir (2), drainer (3), vavuum pump (4), appendix (5), first connecting tube (6) and the second connecting tube (7), one end of appendix (5) is connected with gas reservoir (2), the other end of appendix (5) passes to the tank bottom of heating in vacuum boiling agitator tank (1), one end of first connecting tube (6) is connected with heating in vacuum boiling agitator tank (1), the other end of first connecting tube (6) is connected with drainer (3), one end of second connecting tube (7) is connected with drainer (3), the other end of second connecting tube (7) is connected with vavuum pump (4).The utility model is used for edible oil depickling.
Description
Technical field
It the utility model is related to a kind of deacidifying device of high acid value grease, and in particular to a kind of lossless edible oil depickling dress
Put.
Background technology
Traditional edible oil deacidification technique uses chemical alkali refining method, and a large amount of gleditsia sinensis, and alkali refining are produced due to adding highly basic
Process high temperature, the active ingredient of functional form grease is highly vulnerable to breakage, and is damaged with substantial amounts of neutral oil, sterol, vitamin E etc.
Consume, it is very inapplicable for the depickling for high-end grease.Such as the edible oil and fat that acid value is 10mg/g, by chemical alkali refining method,
Oil is more than 15% production loss.For the high acidity edible oil more than 20mg/g, loss can be bigger.It is more than for acid value
100mg/g grease can not use traditional alkali refining method depickling.
Biology enzyme resterification depickling method is using unique biological lipase, and free fatty is converted into the de- of glyceride
Sour method, suitable for the depickling of high acid value grease.The shortcomings that existing lipase deacidification technique is that lipase loss is larger, due to
Lipase cost is higher, causes deacidifying process production cost higher.
Utility model content
The utility model is that have that lipase loss is larger, cost is higher to solve existing lipase deacidification technique, is led
The problem of causing deacidifying process production cost higher, and then a kind of lossless edible oil deacidifying device is provided.
The utility model adopts the technical scheme that to solve above-mentioned technical problem：
A kind of lossless edible oil deacidifying device of the present utility model, it, which is formed, includes heating in vacuum boiling agitator tank 1, gas
Body storage tank 2, drainer 3, vavuum pump 4, appendix 5, the first connecting tube 6 and the second connecting tube 7, one end of appendix 5 and gas
Storage tank 2 connects, and the other end of appendix 5 passes to the tank bottom of heating in vacuum boiling agitator tank 1, one end of the first connecting tube 6 with it is true
Empty ebuillition of heated agitator tank 1 is connected, and the other end of the first connecting tube 6 is connected with drainer 3, one end of the second connecting tube 7 with it is cold
Solidifying tank 3 is connected, and the other end of the second connecting tube 7 is connected with vavuum pump 4.
The utility model has the advantages that compared with prior art：
1st, the utility model is inputted inert gas in heating in vacuum boiling agitator tank 1 by gas reservoir 2, and using very
Empty pump 4 and drainer 3 realize vacuum low temperature dewatering, reach the lossless depickling of edible oil.Edible oil through the utility model depickling
The technical indicators such as acid value, peroxide value, moisture effectively are greatly reduced, improve product quality, reach state food safety
Standard, extend product quality guarantee period.And without any loss, production cost is reduced, rare raw material resources is filled
Divide and utilize.
2nd, the utility model uses stirring of inert gas, avoids destruction of the mechanical agitation to lipase enzyme granule.
3rd, the utility model solves the problems, such as the lipin deacidifying that acid value is more than 100mg/g so that precious functional grease
It is developed.The utility model solves vavuum pump long-term work, and extracts vacuum caused by steam-laden gas
The problem of lubricant pollution.
4th, the utility model is seethed with excitement by inert gas and stirred, and reduces lipase mechanical damage to greatest extent, is improved
The service life of lipase, significantly reduces production cost.In deacidification, depickling grease zero is lost, while reduces
Oxidation number and moisture index, shorten refinery practice flow.
Brief description of the drawings
Fig. 1 is overall structure diagram of the present utility model.
Embodiment
Embodiment one：Illustrate present embodiment with reference to Fig. 1, present embodiment includes heating in vacuum boiling agitator tank
1st, gas reservoir 2, drainer 3, vavuum pump 4, appendix 5, the first connecting tube 6 and the second connecting tube 7, one end of appendix 5 with
Gas reservoir 2 connects, and the other end of appendix 5 passes to the tank bottom of heating in vacuum boiling agitator tank 1, one end of the first connecting tube 6
It is connected with heating in vacuum boiling agitator tank 1, the other end of the first connecting tube 6 is connected with drainer 3, one end of the second connecting tube 7
It is connected with drainer 3, the other end of the second connecting tube 7 is connected with vavuum pump 4.
Embodiment two：Illustrate present embodiment with reference to Fig. 1, present embodiment is different from embodiment one
It is that it also includes air inlet pressure regulator valve 11, the air inlet pressure regulator valve 11 is arranged on appendix 5.Air inlet pressure regulator valve 11 can be adjusted in real time
Save the pressure in heating in vacuum boiling agitator tank 1.Other compositions and annexation are identical with embodiment one.
Embodiment three：Illustrate present embodiment with reference to Fig. 1, present embodiment and embodiment one or two are not
Same is that it also includes check valve 10, and check valve 10 is arranged on appendix 5.Other compositions and annexation and specific embodiment party
Formula one or two is identical.
Embodiment four：Illustrate present embodiment with reference to Fig. 1, present embodiment is different from embodiment three
It is that it also includes thermometer 8, thermometer 8 is arranged on the tank body of heating in vacuum boiling agitator tank 1.Other compositions and annexation
It is identical with embodiment three.
Embodiment five：Illustrate present embodiment with reference to Fig. 1, present embodiment and embodiment one, two or
It also includes pressure vacuum gauge 9 unlike four, and the pressure vacuum gauge 9 is arranged on the tank body of heating in vacuum boiling agitator tank 1
On.Pressure vacuum gauge 9 can monitor the vacuum in heating in vacuum boiling agitator tank 1 in real time.It is other composition and annexation with
Embodiment one, two or four are identical.
Embodiment six：Illustrate present embodiment with reference to Fig. 1, present embodiment is different from embodiment five
It is that it also includes the first valve 12, first valve 12 is arranged in the first connecting tube 6.Other compositions and annexation and tool
Body embodiment five is identical.
Embodiment seven：Illustrate present embodiment with reference to Fig. 1, present embodiment is different from embodiment six
It is that it also includes the second valve 13, second valve 13 is arranged in the second connecting tube 7.Other compositions and annexation and tool
Body embodiment six is identical.
The course of work of the present utility model：
Treat that depickling grease is poured into heating in vacuum boiling agitator tank 1 by a number of, addition grease weight 5% is consolidated
State Grainy fat tissue enzyme, tank body is heated to 60 DEG C, is passed through inert gas, it is seethed and is uniformly mixed grease.Stop into
Gas is simultaneously static 10 minutes, sampling detection acid value.According to acid value of lipids, required glycerine quantity is calculated.Air inlet pressure regulator valve 11 is opened,
Inert gas is passed through, while the glycerine of requirement is poured into heating in vacuum boiling agitator tank 1, is then sealed, and open true
The water pump of empty pump 4 and drainer 3.Air inlet pressure regulator valve 11 is adjusted, makes grease and lipase entirety tumble mixed uniform, and vacuumize
To 0.08MPa.Process operation is opened closure, sampling detection, after reaching edible oil acid value standard, can stopped to setting time
And release oil, so far, complete whole deacidification.
The utility model solves the production technology problem of high added value feature animals and plants extract, realizes raising extraction
The yield of produce product is taken, extracted products quality is greatly improved, reduces production cost, waste material fills after enabling raw material and extraction
Divide and utilize.
The utility model is greatly improved to technology old than ever from production effect, product quality：
Table one：The technical solution of the utility model and old technology contrast table
It can be seen that, device of the present utility model is an innovation that really may apply in actual production from upper table
High-performance bio extracts process technology.Following key technical index is up in actual applications exemplified by producing forest frog's egg fat:
Table two：The utility model actually reaches key technical index by taking forest frog's egg fat as an example
| Project | Original alkali refining technology | New technology | New and old technology contrast |
| Acid value is in terms of KOH, mg/g | ≤2.0 | ≤2.0 | Reach depickling purpose |
| Peroxide value, mmol/kg | ≤10 | ≤6 | The range of decrease is 40% |
| Oil loss after depickling | 80% | 0% | New technology is without any loss |
Claims (7)
- A kind of 1. lossless edible oil deacidifying device, it is characterised in that：Described device include heating in vacuum boiling agitator tank (1), Gas reservoir (2), drainer (3), vavuum pump (4), appendix (5), the first connecting tube (6) and the second connecting tube (7), appendix (5) one end is connected with gas reservoir (2), and the other end of appendix (5) passes to the tank bottom of heating in vacuum boiling agitator tank (1), One end of first connecting tube (6) is connected with heating in vacuum boiling agitator tank (1), the other end and drainer of the first connecting tube (6) (3) connect, one end of the second connecting tube (7) is connected with drainer (3), and the other end and the vavuum pump (4) of the second connecting tube (7) connect Connect.
- A kind of 2. lossless edible oil deacidifying device according to claim 1, it is characterised in that：Described device also include into Controlled atmosphere pressure valve (11), the air inlet pressure regulator valve (11) are arranged on appendix (5).
- A kind of 3. lossless edible oil deacidifying device according to claim 1 or 2, it is characterised in that：Described device is also wrapped Check valve (10) is included, the check valve (10) is arranged on appendix (5).
- A kind of 4. lossless edible oil deacidifying device according to claim 3, it is characterised in that：Described device also includes temperature Table (8) is spent, the thermometer (8) is arranged on the tank body of heating in vacuum boiling agitator tank (1).
- A kind of 5. lossless edible oil deacidifying device according to claim 4, it is characterised in that：Described device also includes true Hollow pressure gauge (9), the pressure vacuum gauge (9) are arranged on the tank body of heating in vacuum boiling agitator tank (1).
- A kind of 6. lossless edible oil deacidifying device according to claim 5, it is characterised in that：Described device also includes the One valve (12), first valve (12) are arranged in the first connecting tube (6).
- A kind of 7. lossless edible oil deacidifying device according to claim 6, it is characterised in that：Described device also includes the Two valves (13), second valve (13) are arranged in the second connecting tube (7).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721064293.5U CN207210364U (en) | 2017-08-23 | 2017-08-23 | A kind of lossless edible oil deacidifying device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721064293.5U CN207210364U (en) | 2017-08-23 | 2017-08-23 | A kind of lossless edible oil deacidifying device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207210364U true CN207210364U (en) | 2018-04-10 |
Family
ID=61816511
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721064293.5U Expired - Fee Related CN207210364U (en) | 2017-08-23 | 2017-08-23 | A kind of lossless edible oil deacidifying device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207210364U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115364735A (en) * | 2022-06-20 | 2022-11-22 | 岳阳耀宁新能源科技有限公司 | Paddle-free stirring system and negative electrode slurry paddle-free stirring method |
-
2017
- 2017-08-23 CN CN201721064293.5U patent/CN207210364U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115364735A (en) * | 2022-06-20 | 2022-11-22 | 岳阳耀宁新能源科技有限公司 | Paddle-free stirring system and negative electrode slurry paddle-free stirring method |
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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: 20180410 Termination date: 20210823 |
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| CF01 | Termination of patent right due to non-payment of annual fee |