CN206924446U - One kind extraction concentration and recovery unit concentration tank - Google Patents
One kind extraction concentration and recovery unit concentration tank Download PDFInfo
- Publication number
- CN206924446U CN206924446U CN201720810596.0U CN201720810596U CN206924446U CN 206924446 U CN206924446 U CN 206924446U CN 201720810596 U CN201720810596 U CN 201720810596U CN 206924446 U CN206924446 U CN 206924446U
- Authority
- CN
- China
- Prior art keywords
- inner bag
- concentration
- heating interlayer
- capping
- heating
- 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
Links
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/10—Greenhouse gas [GHG] capture, material saving, heat recovery or other energy efficient measures, e.g. motor control, characterised by manufacturing processes, e.g. for rolling metal or metal working
Landscapes
- Heat Treatment Of Water, Waste Water Or Sewage (AREA)
Abstract
The utility model proposes one kind to extract concentration and recovery unit concentration tank, including tank body, opening is provided with the top of the tank body, the opening is provided with capping, and the capping is provided with agitator, the tank body includes outer courage and inner bag, the agitator is provided with the agitating paddle for extending inner bag, is heating interlayer between the outer courage and inner bag, the heating interlayer bottom is taper heating chamber, heater is provided with the taper heating chamber, pure water is marked with the heating interlayer；The capping is provided with the evaporation outlet being connected with interior gallbladder intracavity, and the heating interlayer top is provided with relief tube, and the relief tube is provided with thermometer and relief valve.The utility model thickening efficiency is high, and temperature output is stable, drives agitating paddle to stir the concentrate in inner bag by agitator during concentration, make its it is heated be more uniformly distributed, while defoaming effect can be played, without setting defoaming device.
Description
Technical field
It the utility model is related to and take liquid enrichment facility, and in particular to one kind extraction concentration and recovery unit concentration tank.
Background technology
In field of medicine and chemical technology, concentration tank is used to concentrate bright extraction, some existing concentration tanks are heated by water proof
The mode vacuumized is coordinated to be concentrated, but the mode vacuumized often produces a large amount of bubbles, while need to be equipped with negative pressure
Air-extractor, furthermore it is exactly that often water temperature such as can improve temperature in 100 degrees centigrades by the way of pressurization for water proof heating,
Often cause certain temperature inertness so that fluctuating temperature is larger.
Utility model content
Based on above mentioned problem, the utility model purpose is to provide a kind of thickening efficiency height, the extraction concentration of temperature stabilization
Reclaim unit concentration tank.
For problem above, there is provided following technical scheme：One kind extraction concentration and recovery unit concentration tank, including tank
Body, the tank body top are provided with opening, and the opening is provided with capping, and the capping is provided with agitator, and the tank body includes
Outer courage and inner bag, the agitator are provided with the agitating paddle for extending inner bag, are heating interlayer between the outer courage and inner bag, described
Heating interlayer bottom is taper heating chamber, and heater is provided with the taper heating chamber, and the heater is electrothermal tube, described to add
Pure water is marked with hot interlayer；The capping is provided with the evaporation outlet being connected with interior gallbladder intracavity, and the heating interlayer top is set
There is relief tube, the relief tube is provided with thermometer and relief valve.
In said structure, the agitating paddle is used to stir concentrate, and foam caused by concentrate evaporation can be carried out
Defoaming, the pure water flowing that taper heating chamber contributes to after heating, is consistent the temperature at each position of inner bag, pure water has
After evaporation the advantages of Non-scale, the scale effect efficiency of heating surface in heating interlayer is avoided, evaporation outlet is used to discharge concentrate evaporation
Caused vapor, relief tube set relief valve, and the discharge pressure of steam is controlled by the unlatching dynamics of adjusting pressure release valve,
The water temperature in heating interlayer is controlled with this, coordinates thermometer intuitively to set the current desired temperature wanted.
The utility model is further arranged to, and the observation window being connected with the external world is additionally provided with the inner bag.
In said structure, observation window is used to observe the concentrate enrichment stage in inner bag.
The utility model is further arranged to, and the side wall of inner is provided with feed pipe, and the liner at the bottom is provided with discharge nozzle.
The utility model is further arranged to, and the outer courage is provided with the compensation water pipe being connected with heating interlayer, described
Compensation water pipe is provided with check valve.
In said structure, compensation water pipe is used to inject pure water into heating interlayer, and check valve is closed automatically after charging
Compensate water pipe.
The beneficial effects of the utility model：Thickening efficiency is high, and temperature output is stable, and passing through agitator during concentration drives stirring
Concentrate in oar stirring inner bag, makes it be heated and is more uniformly distributed, while can play defoaming effect, without setting defoaming device.
Brief description of the drawings
Fig. 1 is overall structure diagram of the present utility model.
Fig. 2 is tank body half section structure diagram of the present utility model.
Label implication in figure：10- tank bodies；11- is open；12- is covered；121- agitators；122- agitating paddles；123- is evaporated
Mouthful；The outer courages of 13-；131- compensates water pipe；132- check valves；14- inner bags；141- observation windows；142- feed pipes；143- discharge nozzles；
15- heating interlayers；151- taper heating chambers；152- heaters；153- relief tubes；154- thermometers；155- relief valves.
Embodiment
With reference to the accompanying drawings and examples, specific embodiment of the present utility model is described in further detail.Below
Embodiment is used to illustrate the utility model, but is not limited to the scope of the utility model.
With reference to figure 1 and Fig. 2, a kind of extraction concentration and recovery unit concentration tank as shown in Figures 1 and 2, including tank body 10,
The top of tank body 10 is provided with opening 11, and the opening 11 is provided with capping 12, and the capping 12 is provided with agitator 121, institute
Stating tank body 10 includes outer courage 13 and inner bag 14, and the agitator 121 is provided with the agitating paddle 122 for extending inner bag 14, the outer courage
It is heating interlayer 15 between 13 and inner bag 14, the bottom of heating interlayer 15 is taper heating chamber 151, the taper heating chamber
Heater 152 is provided with 151, the heater 152 is electrothermal tube, and pure water is marked with the heating interlayer 15；The capping
12 are provided with the evaporation outlet 123 being connected with the inner chamber of inner bag 14, and the top of heating interlayer 15 is provided with relief tube 153, described to let out
Pressure pipe 153 is provided with thermometer 154 and relief valve 155.
In said structure, the agitating paddle 122 is used to stir concentrate, and foam caused by concentrate evaporation can be entered
Row defoaming, the pure water flowing that taper heating chamber 151 contributes to after heating, is consistent the temperature at 14 each position of inner bag, pure
With the scale effect efficiency of heating surface in heating interlayer 15 the advantages of Non-scale, is avoided after evaporation, evaporation outlet 123 is used to arrange water purification
Go out vapor caused by concentrate evaporation, relief tube 153 sets relief valve 155, passes through the unlatching dynamics of adjusting pressure release valve 155
To control the discharge pressure of steam, the water temperature in heating interlayer 15 is controlled with this, coordinates thermometer 154 intuitively to set currently
Required temperature.
In the present embodiment, the observation window 141 being connected with the external world is additionally provided with the inner bag 14.
In said structure, observation window 141 is used to observe the concentrate enrichment stage in inner bag 14.
In the present embodiment, the side wall of inner bag 14 is provided with feed pipe 142, and the bottom of inner bag 14 is provided with discharge nozzle 143.
In the present embodiment, the outer courage 13 is provided with the compensation water pipe 131 being connected with heating interlayer 15, the compensation water
Pipe 131 is provided with check valve 132.
In said structure, compensation water pipe 131 is used to inject pure water into heating interlayer 15, and check valve 132 is after charging
It is automatic to close compensation water pipe 131.
The beneficial effects of the utility model：Thickening efficiency is high, and temperature output is stable, is driven by agitator 121 during concentration
Agitating paddle 122 stirs the concentrate in inner bag 14, it is heated and is more uniformly distributed, while can play defoaming effect, disappears without setting
Bulb apparatus.
Described above is only preferred embodiment of the present utility model, it is noted that for the common skill of the art
For art personnel, on the premise of the utility model technical principle is not departed from, some improvement and modification, above-mentioned vacation can also be made
If these improvement and modification also should be regarded as the scope of protection of the utility model.
Claims (4)
1. one kind extraction concentration and recovery unit concentration tank, including tank body, the tank body top is provided with opening, is set in the opening
There is capping, the capping is provided with agitator, it is characterised in that：The tank body includes outer courage and inner bag, is set on the agitator
There is the agitating paddle for extending inner bag, be heating interlayer between the outer courage and inner bag, the heating interlayer bottom is taper heating chamber,
Heater is provided with the taper heating chamber, pure water is marked with the heating interlayer；The capping is provided with and interior gallbladder intracavity
Connected evaporation outlet, the heating interlayer top are provided with relief tube, and the relief tube is provided with thermometer and relief valve.
A kind of 2. extraction concentration and recovery unit concentration tank according to claim 1, it is characterised in that：On the inner bag also
Provided with the observation window being connected with the external world.
A kind of 3. extraction concentration and recovery unit concentration tank according to claim 1, it is characterised in that：The side wall of inner
Provided with feed pipe, the liner at the bottom is provided with discharge nozzle.
A kind of 4. extraction concentration and recovery unit concentration tank according to claim 1, it is characterised in that：Set on the outer courage
There is the compensation water pipe being connected with heating interlayer, the compensation water pipe is provided with check valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720810596.0U CN206924446U (en) | 2017-07-06 | 2017-07-06 | One kind extraction concentration and recovery unit concentration tank |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720810596.0U CN206924446U (en) | 2017-07-06 | 2017-07-06 | One kind extraction concentration and recovery unit concentration tank |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206924446U true CN206924446U (en) | 2018-01-26 |
Family
ID=61353513
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720810596.0U Expired - Fee Related CN206924446U (en) | 2017-07-06 | 2017-07-06 | One kind extraction concentration and recovery unit concentration tank |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206924446U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113680127A (en) * | 2021-07-12 | 2021-11-23 | 泰州市宏泰电力设备有限公司 | Vacuum oil filter with detect function |
-
2017
- 2017-07-06 CN CN201720810596.0U patent/CN206924446U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113680127A (en) * | 2021-07-12 | 2021-11-23 | 泰州市宏泰电力设备有限公司 | Vacuum oil filter with detect function |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN206368170U (en) | A kind of multi-strain fermentation tank | |
| CN205517449U (en) | High -efficient medicament proportioning device | |
| CN206924446U (en) | One kind extraction concentration and recovery unit concentration tank | |
| CN206157155U (en) | Anaerobic fermentation device | |
| CN102198339A (en) | Reduced pressure ultrasonic combined extraction device | |
| CN205974481U (en) | Wine liquid heating evaporation system of cyclic utilization wine vapour heat energy | |
| CN207627977U (en) | A kind of Chinese medicine concentrating tank with density measurement | |
| CN210612903U (en) | Novel ball-type concentrator is used in medicine subsides production | |
| CN202096785U (en) | Depressurizing ultrasonic combination extraction device | |
| CN207065093U (en) | A kind of vaporized hydrogen peroxide generating means | |
| CN103173347A (en) | Multifunctional continuous fermentation and extraction integrated apparatus | |
| CN207384868U (en) | Plant extraction liquid enrichment facility | |
| CN204874479U (en) | White spirit distillation plant | |
| CN207237309U (en) | Chinese medicinal concentration equipment | |
| CN107485872A (en) | Chinese medicinal concentration equipment | |
| CN205796583U (en) | A kind of flash tank | |
| CN209259842U (en) | A kind of high-purity wetting system of clinical laboratory | |
| CN209005224U (en) | A kind of interior circulating-heating evaporator | |
| CN207539891U (en) | Supercritical unit voltage stabilizing steam-line blowing water charging system | |
| CN202002075U (en) | Thermal energy recovery device for boiler steam | |
| CN206701268U (en) | A kind of energy-efficient titanium tube temperature control reactor for preparing aluminium polychloride | |
| CN208260207U (en) | A kind of Chinese medicinal concentration equipment | |
| CN206121181U (en) | Tomato is with heating enrichment facility | |
| CN219481620U (en) | Closed continuous dynamic extraction and concentration device | |
| CN205906506U (en) | Vapour -pressure type water storage tank |
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: 20180126 Termination date: 20210706 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |