CN205884617U - Integrated device is retrieved with flash steam to maceration extract - Google Patents
Integrated device is retrieved with flash steam to maceration extract Download PDFInfo
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- CN205884617U CN205884617U CN201620497042.5U CN201620497042U CN205884617U CN 205884617 U CN205884617 U CN 205884617U CN 201620497042 U CN201620497042 U CN 201620497042U CN 205884617 U CN205884617 U CN 205884617U
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- pipeline
- maceration extract
- vacuum impregnation
- indirect steam
- integrating device
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Abstract
The utility model discloses an integrated device is retrieved with flash steam to maceration extract. The device includes the vacuum impregnation jar, and a pot shell is established to the outer wall cover of vacuum impregnation jar, forms the heating chamber between pot shell and the outer wall, connect the cistern, the below that connects the cistern to be located the vacuum impregnation jar connects the inlet department of cistern to be equipped with the filter screen, the jar of keeping in is kept in jar through first pipeline and the liquid outlet intercommunication that connects the cistern, the filter, the filter is equipped with first discharging pump through the second pipeline and jar intercommunication of keeping in on the second pipeline, the filter passes through the third pipeline and communicates with importing of vacuum impregnation jar, is equipped with first valve on the third pipeline, the separator, the heating chamber of separator passes through fourth duct and filter intercommunication, is equipped with the second valve on the fourth pipeline, the heating chamber intercommunication of steam conduit and vacuum impregnation jar is passed through through the 5th pipeline and jar intercommunication of keeping in, the top of separator in the bottom of separator. Device, but recycle maceration extract and separation flash steam, and it is with low costs, small.
Description
Technical field
The utility model is related to garden stuff processing impregnating equipment technical field and in particular to maceration extract reclaims collection with indirect steam
Become device.
Background technology
With more and more extensively in food processing process, vacuum impregnation is fruit and vegetable crisp chip to fruit and vegetable crisp chip deep process technology
Important process technique, fresh fruit of vegetables carries out impregnation process under vacuo, dipping liquid energy rapidly penetrate into food each is trickle
In pore and space, be conducive to keeping the shape of fruit and vegetable crisp chip and improve appearance luster.
After dipping, in food, about 40% dipping solute still remains in maceration extract about 60% dipping solute penetration.By
Maceration extract material composition in residual declines, and moisture increases, and technique cannot directly use, typically directly drain as waste liquid.
So both increase the production cost of enterprise, cause the pollution of environment again.In food service industry, steam concentrating and separating device can be adopted
Separate the moisture in solution, improve solute concentration, reach concentration and detached purpose, but generally existing indirect steam is difficult by
Or complicated using apparatus structure, bulky, the problems such as cost input is high.
Utility model content
Based on this, the utility model provides a kind of recoverable maceration extract and separates indirect steam, and low cost, body
Long-pending little maceration extract and indirect steam reclaim integrating device.
In order to realize the purpose of this utility model, the utility model employs the following technical solutions:
A kind of maceration extract reclaims integrating device with indirect steam, comprising:
Vacuum impregnation tank, described vacuum impregnation tank has heating chamber；
Connect liquid bath, described connect the lower section that liquid bath is located at described vacuum impregnation tank, the described liquid bath that connects has inlet and goes out liquid
Mouthful, it is provided with filter screen at described inlet；
Temporary storage tank, described temporary storage tank is connected with the described liquid outlet connecing liquid bath by one first pipeline；
Filter, described filter is connected with described temporary storage tank by a second pipe, and described second pipe is provided with
One discharging pump；Described filter passes through the inlet communication of the 3rd pipeline and described vacuum impregnation tank, and described 3rd pipeline is provided with
First valve；
Separator, the heating chamber of described separator is connected with described filter by the 4th pipeline, on described 4th pipeline
It is provided with the second valve；The bottom of described separator is connected with described temporary storage tank by the 5th pipeline, and the top of described separator leads to
The heating chamber crossing jet chimney with described vacuum impregnation tank connects.
Wherein in some embodiments, described jet chimney extends a blast pipe, described blast pipe is provided with air bleeding valve
Door.
Wherein in some embodiments, the described liquid outlet connecing liquid bath is connected with a raw material adding trough by a drain pipe,
Described raw material adding trough is connected with described temporary storage tank by described first pipeline, and described drain pipe is provided with the 3rd valve.
Wherein in some embodiments, described first pipeline is provided with the second discharging pump.
Wherein in some embodiments, described 5th pipeline is provided with the 3rd discharging pump.
Wherein in some embodiments, described vacuum impregnation tank top is provided with Cap for tin body, and described Cap for tin body seals described true
The import of empty impregnating autoclave, described Cap for tin body is connected with pneumatic tensile axis, pulls pneumatic tensile axis can open described import.
Wherein in some embodiments, the import of described vacuum impregnation tank is connected with vacuum tube.
Wherein in some embodiments, described vacuum impregnation tank has rabbling mechanism, and described rabbling mechanism is included located at institute
State the agitator in vacuum impregnation tank, the motor outside described vacuum impregnation tank and the transmission belt with described motor connection,
Described transmission belt is connected with the main shaft of described agitator.
Wherein in some embodiments, described maceration extract and indirect steam reclaim integrating device and also include plc control system,
Described plc control system is electrically connected with described first discharging pump, the first valve and the second valve pneumatic tensile axis respectively.
Wherein in some embodiments, the described bottom angled setting connecing liquid bath.
Maceration extract described in the utility model reclaims integrating device with indirect steam, including vacuum impregnation tank, connects liquid bath, keeps in
Tank, filter and separator, the residual maceration extract after vacuum impregnation tank dipping is poured into and is connect liquid bath, and the filter screen connecing liquid bath is first carried out
Filter, after carrying out solid-liquid initial gross separation, flow into temporary storage tank storage, the maceration extract in temporary storage tank pumps into after filter is filtered again
Secondary addition vacuum impregnation tank recycles, and has reached the purpose reclaiming maceration extract；A part of maceration extract enters separator to be carried out admittedly
Liquid separates, and the liquids recovery after separating enters temporary storage tank and is continuing with, and the indirect steam that separator produces is recycled to vacuum impregnation tank,
For heating, vacuum impregnating autoclave, reach the purpose of Steam Recovery utilization；Whole equipment becomes one, small volume；And all use
Conventional part, low cost.
Brief description
Fig. 1 is the structural representation that maceration extract described in the utility model embodiment and indirect steam reclaim integrating device.
Specific embodiment
For the ease of understanding the utility model, below with reference to relevant drawings, the utility model is more fully retouched
State.Preferred embodiment of the present utility model is given in accompanying drawing.But, the utility model can come real in many different forms
Existing however it is not limited to embodiment described herein.On the contrary, providing the purpose of these embodiments to be to make to public affairs of the present utility model
The understanding opening content is more thoroughly comprehensive.
It should be noted that when element is referred to as " being fixed on " another element, it can be directly on another element
Or can also there is element placed in the middle.When an element is considered as " connection " another element, it can be directly connected to
To another element or may be simultaneously present centering elements.
Unless otherwise defined, all of technology used herein and scientific terminology are led with belonging to technology of the present utility model
The implication that the technical staff in domain is generally understood that is identical.In term used in the description of the present utility model it is simply herein
The purpose of description specific embodiment is it is not intended that in limiting the utility model.
Embodiment
Refer to Fig. 1, maceration extract described in the utility model reclaims integrating device 100 with indirect steam, including Vaccum Permeating
Stain tank 10, connect liquid bath 20, raw material adding trough 30, temporary storage tank 40, filter 50, separator 60 and a plc control system 70, very
Pour maceration extract in empty impregnating autoclave 10, for impregnating to food, have partial immersion liquid after the completion of dipping and stay Vaccum Permeating
In stain tank 10, the maceration extract of residual is poured into and is connect in liquid bath 20, is tentatively filtered connecing in liquid bath 20, flows into raw material adding trough
30, need to add maceration extract by raw material adding trough 30 when adding maceration extract, the maceration extract in raw material adding trough 30 flows into temporary storage tank
40, temporarily preserved by temporary storage tank 40, when needing maceration extract, the maceration extract in temporary storage tank 40 is pumped into filter 50 and is filtered,
Then part inflow separator 60 carries out separation of solid and liquid, and another part flows into vacuum impregnation tank 10 recovery and uses maceration extract.
Vacuum impregnation tank 10 has heating chamber 12, is used for being installed with steam, is that vacuum impregnation tank 10 heats.Specifically: vacuum
The sheathed tank set 11 of outer wall of impregnating autoclave 10, forms heating chamber 12, secondary steaming between tank set 11 and the outer wall of vacuum impregnation tank 10
Vapour can flow in heating chamber 12, and vacuum impregnation tank 10 is heated, and reaches the purpose reclaiming indirect steam.Vacuum impregnation tank 10 upper
Portion has import 13, is provided with Cap for tin body 14 at import 13, and Cap for tin body 14 seals the import 13 of vacuum impregnation tank 10, Cap for tin body 14 with
Pneumatic tensile axis 15 connect, and the pneumatic tensile axis of crawl 15 can open vacuum impregnation tank 10 import, to add into vacuum impregnation tank 10
With maceration extract and raw material.Pneumatic tensile axis 15 are electrically connected with plc control system 70, directly control point in plc control system 70
Take offence dynamic tensile axis 15, you can open or close Cap for tin body 14.The import 13 of vacuum impregnation tank 10 is connected with vacuum tube 16, to true
Empty impregnating autoclave 10 vacuumizes.There is rabbling mechanism 17, for carrying out to the material in vacuum impregnation tank 10 in vacuum impregnation tank 10
Stirring, preferably to be impregnated, rabbling mechanism 17 includes agitator 171 in vacuum impregnation tank 10, located at Vaccum Permeating
Motor 172 outside stain tank 10 and the transmission belt 173 being connected with motor 172, transmission belt 173 is connected with the main shaft of agitator 171,
When motor 172 rotates, transmission belt 173 is driven to be driven, transmission belt 173 drives agitator 171 to rotate.This vacuum impregnation tank 10 can incline
Tiltedly, internal maceration extract is poured out to connecing liquid bath 20.Motor 172 is electrically connected with plc control system 70, by plc control system 70
Control and run.
Connect the lower section that liquid bath 20 is located at vacuum impregnation tank 10, there is inlet and liquid outlet, connect at the inlet of liquid bath 20
It is provided with filter screen 21 so that dipping material that vacuum impregnation tank 10 is poured out first passes through this filter screen 21 is filtered so that separation of solid and liquid,
Enter back into and connect in liquid bath 20, connect the bottom angled setting of liquid bath 20.The liquid outlet connecing liquid bath 20 is added by drain pipe 22 and raw material
Plus groove 30 connects, can prevent from connecing maceration extract spilling in liquid bath 20, drain pipe 22 is provided with the 3rd valve 23, can pass through the 3rd valve
The circulation of 23 control maceration extracts.Raw material adding trough 30 has lid, opens lid, can add dipping into raw material adding trough 30
Liquid, is mixed with original maceration extract.Raw material adding trough 30 is connected with temporary storage tank 40 by the first pipeline 31, and raw material is added
Plus the maceration extract in groove 30 flows in temporary storage tank 40 and temporarily stores.First pipeline 31 is provided with the second discharging pump 32, by second
Maceration extract in raw material adding trough 30 is pumped into temporary storage tank 40 by discharging pump 32.Plc control system 70 respectively with the 3rd valve 23 with
Second discharging pump 32 electrically connects, and controls the 3rd valve 23 to run with the second discharging pump 32 in plc control system 70.Raw material adds
Groove 30 can also be not provided with, and reason is directly can to pour maceration extract into from the import of vacuum impregnation tank 10.
Temporary storage tank 40 is a tank body, for storing maceration extract.
Filter 50 is connected with temporary storage tank 40 by second pipe 51, and second pipe 51 is provided with the first discharging pump 52, leads to
Cross the first discharging pump 52 to pump into the maceration extract in temporary storage tank 40 in filter 50.Filter 50 passes through the 3rd pipeline 53 and vacuum
The inlet communication of impregnating autoclave 10, the maceration extract after filter 50 filtration flows in vacuum impregnation tank 10 and is recycled.3rd
Pipeline 53 is provided with the first valve 54, for controlling maceration extract to flow in vacuum impregnation tank 10.Plc control system 70 is respectively with
One discharging pump 52, the first valve 54 electrically connect, and control the first discharging pump 52 to run with the first valve 54.
Separator 60 is solid-liquid separator, and it has heating chamber 61, and maceration extract can be dense by heating after entering heating chamber 61
Contracting, carries out separation of solid and liquid, produces indirect steam, and liquid then drops down onto the bottom of separator 60.The heating chamber 61 of separator 60 is passed through
4th pipeline 62 is connected with filter 50, and the 4th pipeline 62 is provided with the second valve 63 so that the part in filter 50 is soaked
Stain liquid is flowed in the heating chamber 61 of separator 60 by the 4th pipeline 62 and carries out separation of solid and liquid.The bottom of separator 60 passes through the 5th
Pipeline 64 is connected with temporary storage tank 40, and the 5th pipeline is provided with the 3rd discharging pump 68, and the maceration extract of separator 60 bottom is pumped into temporarily
Deposit storage in tank 40.The top of separator 60 is connected with the heating chamber 12 of vacuum impregnation tank 10 by jet chimney 65, separator
The indirect steam of 60 generations is flowed in the heating chamber 12 of vacuum impregnation tank 10 by jet chimney 65, provides for vacuum impregnation tank 10
Heat, thus reclaim indirect steam.One blast pipe 69 is extended on jet chimney 65, blast pipe 69 is provided with drain tap 67,
For discharging the steam of many surpluses, to control the temperature of vacuum impregnation tank 10.The bottom of separator 60 is additionally provided with condenser pipe 66, and two
The condensed water that secondary steam condensation produces is discharged by condenser pipe 66.Plc control system 70 respectively with the second valve 63, the 3rd discharging
Pump 68 and steam valve 67 electrically connect, and control the operation of the second valve 63, the 3rd discharging pump 68 and steam valve 67.
During the work of this device, the pneumatic tensile axis of crawl 15 in plc control system 70, pneumatic tensile axis 15 open Cap for tin body
14, it would be desirable to the material of dipping is poured in vacuum impregnation tank 10 by the import 13 of vacuum impregnation tank 10, open the first valve 54, will
Maceration extract in temporary storage tank 40 is pumped into by the first discharging pump 52 and flows in vacuum impregnation tank 10 after filter 50 filters, as true
The maceration extract of empty impregnating autoclave 10.Vacuum impregnation tank 10 is vacuumized it is ensured that vacuum reaches -0.06mpa in impregnating autoclave, open motor
172, drive agitator 171 to rotate, so that material and maceration extract is sufficiently mixed.In dipping process, the secondary steaming that separator 60 produces
Vapour is flowed in the heating chamber 12 of vacuum impregnation tank 10 by jet chimney 65, and vacuum impregnation tank 10 is heated, when vapor (steam) temperature surpasses
Go out vacuum impregnation tank 10 control temperature when, open drain tap 67 and be exhausted, make dipping process temperature be maintained at setting
In the range of.After dipping terminates, stop motor 172, the pneumatic tensile axis of crawl 15, pneumatic tensile axis 15 open Cap for tin body 14, can body
Tilt certain angle, the whole materials after dipping are poured into and connects liquid bath 20, filtered by filter screen 21, the food after dipping stays
On filter screen 21, and the maceration extract after impregnating flows into and connects in liquid bath 20, treats the maceration extract in raw material adding trough 30 and temporary storage tank 40
After pumping into vacuum impregnation tank 10, open the 3rd valve 23, by drain pipe 22, the maceration extract connecing in liquid bath 20 inflow raw material is added
Plus groove 30, start the second discharging pump 32, the maceration extract in raw material adding trough 30 is all pumped in temporary storage tank 40.Close the first valve
Door 54, opens the second valve 63, starts the first discharging pump 52, the maceration extract in temporary storage tank 40 is all pumped into filter 50 and filters
Enter the heating chamber 61 of separator 60 afterwards so that the moisture in maceration extract vaporizes, the portion that the indirect steam being formed after vaporization is carried secretly
Sub-material liquid separates in separator 60, and maceration extract back flows back into heating chamber 61, and indirect steam passes through jet chimney 65 to Vaccum Permeating
Stain tank 10 heats, and the maceration extract after concentration pumps into storage in temporary storage tank 40 through the 5th pipeline 64.
Embodiment described above only have expressed several embodiments of the present utility model, and its description is more concrete and detailed,
But therefore can not be interpreted as the restriction to the utility model the scope of the claims.It should be pointed out that it is common for this area
For technical staff, without departing from the concept of the premise utility, some deformation can also be made and improve, these all belong to
In protection domain of the present utility model.Therefore, the protection domain of the utility model patent should be defined by claims.
Claims (10)
1. a kind of maceration extract reclaims integrating device with indirect steam it is characterised in that including:
Vacuum impregnation tank, described vacuum impregnation tank has heating chamber；
Connect liquid bath, described connect the lower section that liquid bath is located at described vacuum impregnation tank, the described liquid bath that connects has inlet and liquid outlet, institute
State and at inlet, be provided with filter screen；
Temporary storage tank, described temporary storage tank is connected with the described liquid outlet connecing liquid bath by one first pipeline；
Filter, described filter is connected with described temporary storage tank by a second pipe, and described second pipe is provided with first and goes out
Material pump；Described filter passes through the inlet communication of the 3rd pipeline and described vacuum impregnation tank, and described 3rd pipeline is provided with first
Valve；
Separator, the heating chamber of described separator is connected with described filter by the 4th pipeline, and described 4th pipeline is provided with
Second valve；The bottom of described separator is connected with described temporary storage tank by the 5th pipeline, and the top of described separator is passed through to steam
Steam pipe road is connected with the heating chamber of described vacuum impregnation tank.
2. maceration extract according to claim 1 and indirect steam reclaim integrating device it is characterised in that: described jet chimney
Upper extension one blast pipe, described blast pipe is provided with drain tap.
3. maceration extract according to claim 1 and indirect steam reclaim integrating device it is characterised in that: the described liquid bath that connects
Liquid outlet is connected with a raw material adding trough by a drain pipe, and it is temporary with described that described raw material adding trough passes through described first pipeline
Tank connects, and described drain pipe is provided with the 3rd valve.
4. maceration extract according to claim 1 and indirect steam reclaim integrating device it is characterised in that: described first pipeline
It is provided with the second discharging pump.
5. maceration extract according to claim 1 and indirect steam reclaim integrating device it is characterised in that: described 5th pipeline
It is provided with the 3rd discharging pump.
6. maceration extract according to claim 1 and indirect steam reclaim integrating device it is characterised in that: described vacuum impregnation
Tank top is provided with Cap for tin body, and described Cap for tin body seals the import of described vacuum impregnation tank, and described Cap for tin body is with pneumatic tensile axis even
Connect, pull pneumatic tensile axis can open described import.
7. the maceration extract according to claim 1 or 6 and indirect steam reclaim integrating device it is characterised in that: described vacuum
The import of impregnating autoclave is connected with vacuum tube.
8. the maceration extract according to claim 1 or 6 and indirect steam reclaim integrating device it is characterised in that: described vacuum
Impregnating autoclave has rabbling mechanism, and described rabbling mechanism includes agitator in described vacuum impregnation tank, located at described vacuum
Motor outside impregnating autoclave and the transmission belt with described motor connection, described transmission belt is connected with the main shaft of described agitator.
9. the maceration extract according to any one of claim 1 and indirect steam reclaim integrating device it is characterised in that: described leaching
Stain liquid and indirect steam reclaim integrating device and also include plc control system, described plc control system respectively with described first discharging
Pump, the first valve and the electrical connection of the second valve.
10. maceration extract according to claim 1 and indirect steam reclaim integrating device it is characterised in that: described connect liquid bath
Bottom angled setting.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620497042.5U CN205884617U (en) | 2016-05-25 | 2016-05-25 | Integrated device is retrieved with flash steam to maceration extract |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620497042.5U CN205884617U (en) | 2016-05-25 | 2016-05-25 | Integrated device is retrieved with flash steam to maceration extract |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205884617U true CN205884617U (en) | 2017-01-18 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620497042.5U Expired - Fee Related CN205884617U (en) | 2016-05-25 | 2016-05-25 | Integrated device is retrieved with flash steam to maceration extract |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205884617U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110870543A (en) * | 2018-09-04 | 2020-03-10 | 中国农业大学 | Circulating mixing device and method for pickling liquid |
| CN111972637A (en) * | 2020-08-19 | 2020-11-24 | 安徽东方果园生物科技有限公司 | Fruit and vegetable crisp chip impregnation adjusting system |
-
2016
- 2016-05-25 CN CN201620497042.5U patent/CN205884617U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110870543A (en) * | 2018-09-04 | 2020-03-10 | 中国农业大学 | Circulating mixing device and method for pickling liquid |
| CN111972637A (en) * | 2020-08-19 | 2020-11-24 | 安徽东方果园生物科技有限公司 | Fruit and vegetable crisp chip impregnation adjusting 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 | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20170118 Termination date: 20190525 |