CN206507214U - It is dried in vacuo extracting system - Google Patents
It is dried in vacuo extracting system Download PDFInfo
- Publication number
- CN206507214U CN206507214U CN201620990038.2U CN201620990038U CN206507214U CN 206507214 U CN206507214 U CN 206507214U CN 201620990038 U CN201620990038 U CN 201620990038U CN 206507214 U CN206507214 U CN 206507214U
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- vacuum
- chamber
- operation chamber
- dried
- extracting system
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Abstract
The utility model is related to a kind of vacuum drying extracting system.The vacuum drying extracting system includes an operation chamber, a temperature control device, a condensing chamber and a vacuum plant.The operation chamber is used to place an at least object.The temperature control device is used to control the temperature in the operation chamber to be located at a specific range of temperatures.The condensing chamber connects the operation chamber.The vacuum plant connects the condensing chamber to control the vacuum of the operation chamber.The vacuum that the utility model is controlled merely with the vacuum plant, can make an at least object while being dried and extraction processing.
Description
Technical field
The utility model system is related to a kind of vacuum drying extracting system, is particularly suitable for use in the vacuum drying of food processing field
Extracting system.
Background technology
Because food security is increasingly subject to social attention, the nutrient for how maintaining food original is reduced using chemistry
Mode is handled food, is gradually taken seriously.Existing food drying system, it is however generally that there was only two ways：Heating is dry
Dry method and freeze-drying.Heat drying method is usually required the moisture content of food by the operating environment more than 50 degree (Celsius)
Remove.Freeze-drying rule is to need to remove the moisture content of food by the operation temperature less than 0 degree (Celsius).Whether heat
Seasoning or freeze-drying are that the temperature for significantly alterring operating environment can be only achieved the mesh for removing the moisture content in food
, but so significantly temperature changes and causes a certain degree of destruction for food nutrient in itself and original flavor.
Referring in addition to existing patent TW201113489, another existing food drying system, the food drying system are disclosed
System is needed first by food directly with the freezing (Celsius) of -40 degree, and then the existing food drying system is only merely by microwave
Mode of heating makes the food, and contained moisture content vibration comes frictional heat and then drying kinetics food, but this microwave heating side in itself
Formula is same easily to be caused significantly to destroy to the food nutrient in itself and original flavor.
Another existing extracting system also has some technical problems：First, an article (food is contacted using a specific solvent
Or plant etc.) so that a predetermined substance of the article is dissolved in the specific solvent；Then, the specific solvent (is included
The predetermined substance) separated with the article (predetermined substance wholly or largely has been dissolved), so far can be at last
Complete extraction procedure.However, it is also possible to further remove the specific solvent, the predetermined substance is obtained.In general, institute
It can be that water can also be other organic or inorganic chemical solvents to state specific solvent, but these specific solvents may immerse
Produce chemical reaction in the article, it is same easily the food nutrient in itself and original flavor to be caused significantly to destroy or very
To the doubt for causing food security.
Therefore, during the above each known techniques are below high temperature (more than 50 degree Celsius) or low temperature (as being less than 0 degree Celsius)
Food is dried and/or extracted with chemical solvent, all exist food is likely to result in its nutrient be largely lost in, food materials it is former
The technical problem such as taste is destroyed.
Therefore, it is necessary to a kind of vacuum drying extracting system is proposed, to solve above-mentioned technical problem.
Utility model content
The problem of to solve above-mentioned known techniques, the purpose of this utility model is to provide a kind of vacuum drying extraction system
System.The utility model is dried by using dynamical vacuum plant with the article that low destruction is carried out in the environment close to normal temperature
Change (being usually food, plant etc..) and extractionization program, and then dried article (the first product) can be obtained simultaneously
And the extract (the second product) of article, therefore the utility model is avoided in known techniques because article is done in high temperature or low temperature
The technical problem such as the nutrient caused by dry and/or extraction is lost in, food materials original flavor is destroyed.
In the utility model, the boiling of liquid (such as water) is reduced by way of improving vacuum (gas pressure decline)
Point, then, will be described using the moment temperature difference therefore, it is possible to distil and/or gasify the extract of food (moisture content and grease)
Extract transforms back into grease and/or moisture content.In general, the extract is commonly referred to as hydrosol (hydrosol) and essential oil
(essential oil).In detail, be dissolved in water among the extract is hydrosol, and water insoluble part is essential oil..
For up to above-mentioned purpose, the utility model provides a kind of vacuum drying extracting system.The vacuum drying extracting system
Including an operation chamber, a temperature control device, a condensing chamber and a vacuum plant.
The operation chamber is used to place an at least object.The temperature control device is used to control the temperature in the operation chamber
Degree is located at a specific range of temperatures.The condensing chamber is used to connect the operation chamber.The vacuum plant is used to connect institute
Condensing chamber is stated to control the vacuum of the operation chamber, and the vacuum only controlled according to the vacuum plant, at least
One object, which is performed, to be dried and extraction processing.
In a preferred embodiment, the vacuum plant extract a gas contained in the operation chamber and it is described extremely
An at least material contained by a few object.
In a preferred embodiment, an at least material is further extracted to the condensing chamber by the vacuum plant
In, and the condensing chamber also includes a condensation an at least material to be condensed into admittedly in the condensing chamber
Body and/or liquid.
In a preferred embodiment, the specific range of temperatures is between 0-40 degree (Celsius).
In a preferred embodiment, the vacuum that the vacuum plant is controlled is the gas pressure in the operation chamber
Less than 133 handkerchiefs (pa).
In a preferred embodiment, an at least material includes aqueous vapor and/or grease.
For up to above-mentioned purpose, the utility model provides a kind of vacuum drying extracting process.The sampling method includes：It is first
First, at least an operation chamber will be positioned over by an object；Then, institute is controlled using a temperature control device for being connected to the operation chamber
The temperature of operation chamber is stated in a specific range of temperatures；Then, only extracted by a vacuum plant in the operation chamber
An at least material contained by one gas and an at least object, an at least object is dried and extraction processing.
In a preferred embodiment, the vacuum drying extracting process also includes：Then, an at least material is described
Vacuum plant, which is extracted to a condensing chamber, to carry out condensing into solid and/or liquid.
In a preferred embodiment, the specific range of temperatures is between 0-40 degree (Celsius).
In a preferred embodiment, the vacuum that the vacuum plant is controlled is the gas pressure in the operation chamber
Less than 133 handkerchiefs (pa).
In a preferred embodiment, an at least material includes aqueous vapor and/or grease.
Known techniques are compared, the utility model maintains food specific by the vacuum plant and the temperature control device
It is dried in temperature range (no more than 50 degree Celsius nor less than 0 degree Celsius), dried food (the can be obtained simultaneously
One product) and the extract (the second product) that is extracted from the food.The utility model avoid food in high temperature or
The technical problem that the nutrient being likely to result under low temperature is lost in.
Brief description of the drawings
Fig. 1 illustrates a kind of component signal of the vacuum drying extracting system of the first preferred embodiment according to the utility model
Figure；
Fig. 2 illustrates a kind of flow chart of the vacuum drying extracting process according to the second preferred embodiment of the present utility model；
And
Fig. 3 illustrates a kind of flow chart of the vacuum drying extracting process according to third preferred embodiment of the present utility model.
Embodiment
The explanation of following embodiment is to refer to schema, the particular implementation implemented to illustrate the utility model can be used to
Example.The direction term that the utility model is previously mentioned, such as " on ", " under ", "front", "rear", "left", "right", " interior ", " outer ", " side
Face " etc., is only the direction with reference to schema.Therefore, the direction term used is to illustrate and understand the utility model, Er Feiyong
To limit the utility model.
Fig. 1 illustrates a kind of signal of the vacuum drying extracting system 100 of first preferred embodiment according to the utility model
Figure.It is true that the vacuum drying extracting system 100 includes an operation chamber 110, a temperature control device 130, a condensing chamber 160 and one
Empty device 120.In detail, the vacuum plant 120 can be various forms of high power vacuum pumps.Preferably, it is described true
Empty device 120 can produce the Absolute truth reciprocal of duty cycle less than 10 handkerchiefs (pa).(Absolute truth reciprocal of duty cycle represents gas pressure)
The operation chamber 110 is used to place an at least object 150.The temperature control device 130 is used to control the operation
Temperature in chamber 110 is located in a specific range of temperatures.The condensing chamber 160 is used to connect the operation chamber 110.Institute
Stating vacuum plant 120 is used to connect the condensing chamber 160 to control the vacuum of the operation chamber 110, and only according to described
The vacuum that vacuum plant 120 is controlled, can at the same time or separately perform to an at least object 150 and dry and extraction processing；Cause
The pressure differential caused for pipeline, the vacuum plant 120 can not make the gas pressure of the operation chamber 110 such as the vacuum
The gas pressure at the end of device 120.Preferably, the vacuum that the vacuum plant 120 is controlled is 110 in the operation chamber
Gas pressure is less than 133 handkerchiefs (pa).According to Torricellian, an atmospheric pressure is approximately equal to 101.3 hundred handkerchiefs (mpa).As long as gas
Pressure, which is less than an atmospheric pressure (i.e. 101.3 hundred handkerchiefs), can be referred to as negative pressure.
In the utility model, liquid (Ru Shui, oil) is reduced by way of improving vacuum (gas pressure decline)
Boiling point, therefore, it is possible to distil and/or gasify the extract of food (moisture content and grease), then, using the moment temperature difference by institute
State extract and transform back into grease and/or moisture content.In general, the part of extraction is commonly referred to as hydrosol (hydrosol) and essential oil
(essential oil).In detail, be dissolved in water among an at least material 1502 for the extract is hydrosol, water insoluble
Part be essential oil.In the utility model, by high vacuum (that is, environment of negative pressure) material of liquid can be forced to divide
The mode of sonization is extracted.
An at least object 150 can be such as fruit, plant (flower, grass), fresh, meat, food and any need
The article of processing or extraction processing is dried.Above-mentioned drying process refers to removing moisture content contained in object 150；It is above-mentioned
Extraction processing refers to moisture content and/or other compositions (such as grease) contained in the object 150 removing the object 150
Outside separately used.In general, both processing are carried out separately；It is a lack of in the prior art in combination with described
The device and method of two kinds of processing.In the present embodiment, the vacuum plant 120 is except extracting institute in the operation chamber 110
At least gas (be substantially oxygen and/or nitrogen) contained is to reach that vacuum is antibacterial, the guarantor of an at least object 150 described in extension
Deposit outside the effect in time limit, also an at least material 1502 (such as water and/or other compositions contained by an at least object 150 described in extraction
(such as grease)) to complete drying process.Then, an at least material 1502 can further be taken out by the vacuum plant 120
Take into the condensing chamber 160, the condensing chamber 160 includes a condensation 140 to contact from an at least thing
At least material 1502 extracted in body 150, makes an at least material 1502 be coagulated in the condensing chamber 160
Become solid and/or liquid, and then complete extraction processing.In detail, the operation chamber 110 is an air-tightness and insulation
Property excellent container.
In practical operation, the temperature control device 130 can control the specific range of temperatures in the operation chamber 110
It is set between 0-40 degree (Celsius), in general the setting of specific range of temperatures can adjust according to different objects.Lift
For example, when the object 150 is seafood, it is preferable that the specific range of temperatures can be 0-30 degree (Celsius)；The thing
Then it is that the temperature by the object 150 in nature is defined when body 150 is plant, fruit or meat；Preferably, the spy
Determining temperature range can be 10-40 degree (Celsius).The vacuum drying extracting system 100 of the present utility model also allows for the thing
Extraction processing is directly dried under room temperature environment in body 150, it is to avoid nutrient and original flavor stream that temperature change is likely to result in
The technical problem of mistake.The dried object 150 and the extract extracted from the object 150 can be obtained simultaneously
(an i.e. described at least material 1502) two kinds of products.
Please further refer to the 1st and 2 figures, wherein Fig. 2 illustrates the vacuum drying of the second preferred embodiment of the present utility model
The flow chart of extracting process.(element numbers that refer to Fig. 1).First, step S01 is performed, at least an object 150 will be positioned over
One operation chamber 110；Then, step S02 is performed, institute is controlled using a temperature control device 130 for being connected to the operation chamber 110
The temperature of operation chamber 110 is stated in a specific range of temperatures；Then, step S03 is performed, is only taken out by a vacuum plant 120
Take in the operation chamber 110 a gas and an at least object 150 contained by an at least material 1502, to be done
Dry and extraction processing.
Please further refer to the 1st and 3 figures, wherein Fig. 3 illustrates the vacuum drying of third preferred embodiment of the present utility model
The flow chart of extracting process.The difference of this third preferred embodiment and the method for above-mentioned second embodiment is：Originally the 3rd is preferred
Embodiment increase by one performs step S04, and an at least material 1502 extracts to a condensing chamber 160 by the vacuum plant
Row condenses into solid and/or liquid further to obtain extract.Therefore, this method can also obtain the production that the article is extracted
Product.
Compared to known techniques, the utility model maintains to eat by the vacuum plant 120 and the temperature control device 130
Product are dried in the specific range of temperatures (no more than 50 degree Celsius nor less than 0 degree Celsius), and drying can be obtained simultaneously
Rear food (the first product) and the extract (the second product) extracted from the food.The utility model avoids food
The technical problem that the nutrient that product are likely to result at high or low temperatures is lost in.
Although the utility model is disclosed above with preferred embodiment, so it is not intended to limit the utility model, this reality
New those of ordinary skill in the art is used, it is each when that can make in the spirit and scope for not departing from the utility model
The change of kind and retouching, thus the utility model protection domain when depending on after the attached claim person of defining be defined.
Claims (6)
1. a vacuum drying extracting system, it is characterised in that including：
One operation chamber, for placing an at least object；
One temperature control device, for controlling the temperature in the operation chamber to be located at a specific range of temperatures；
One condensing chamber, for connecting the operation chamber, and
One vacuum plant, for connecting the condensing chamber to control the vacuum of the operation chamber, and only according to the vacuum
The vacuum that device is controlled, performs to an at least object and dries and extraction processing.
2. extracting system is dried in vacuo as claimed in claim 1, it is characterised in that the vacuum plant extracts the operating cavity
At least material contained by a gas and an at least object contained by interior.
3. extracting system is dried in vacuo as claimed in claim 2, it is characterised in that an at least material is by the vacuum holding
Put and further extract into the condensing chamber, and the condensing chamber also includes a condensation to an at least thing by described in
Matter is condensed into solid and/or liquid in the condensing chamber.
4. extracting system is dried in vacuo as claimed in claim 1, it is characterised in that the specific range of temperatures is between 0- Celsius
40 degree.
5. extracting system is dried in vacuo as claimed in claim 2, it is characterised in that the vacuum that the vacuum plant is controlled
It is less than 133 handkerchiefs for the gas pressure in the operation chamber.
6. as claimed in claim 2 vacuum drying extracting system, it is characterised in that an at least material include aqueous vapor and/
Or grease.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620990038.2U CN206507214U (en) | 2016-08-30 | 2016-08-30 | It is dried in vacuo extracting system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620990038.2U CN206507214U (en) | 2016-08-30 | 2016-08-30 | It is dried in vacuo extracting system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206507214U true CN206507214U (en) | 2017-09-22 |
Family
ID=59860988
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620990038.2U Expired - Fee Related CN206507214U (en) | 2016-08-30 | 2016-08-30 | It is dried in vacuo extracting system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206507214U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107772196A (en) * | 2016-08-30 | 2018-03-09 | 东钜能源科技实业有限公司 | It is dried in vacuo extracting system and its operating method |
-
2016
- 2016-08-30 CN CN201620990038.2U patent/CN206507214U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107772196A (en) * | 2016-08-30 | 2018-03-09 | 东钜能源科技实业有限公司 | It is dried in vacuo extracting system and its operating method |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20170922 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |