CN204891255U - Enrichment facility that stepped down in steam heating vacuum - Google Patents
Enrichment facility that stepped down in steam heating vacuum Download PDFInfo
- Publication number
- CN204891255U CN204891255U CN201520660156.2U CN201520660156U CN204891255U CN 204891255 U CN204891255 U CN 204891255U CN 201520660156 U CN201520660156 U CN 201520660156U CN 204891255 U CN204891255 U CN 204891255U
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- inner bag
- steam
- condenser
- enrichment facility
- steam heating
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- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model discloses an enrichment facility that stepped down in steam heating vacuum, including steam heating device and condensing equipment, steam heating device is including pressing from both sides cover and inner bag, press from both sides cover parcel inner bag, it is provided with stabilizer blade, exhaust hole and waste liquid export to press from both sides the cover bottom, the left side that presss from both sides the cover middle part is provided with steam inlet, be provided with feed inlet, vacuum machine and vapour and liquid separator on the inner bag, the feed inlet is located the left side of inner bag, the vacuum seat in the plane in the right side of inner bag and with inner bag looks rigid coupling, vapour and liquid separator lies in the top of inner bag and connects steam heating device and condensing equipment, condensing equipment package condenser, cooling water ciculation import and bin, the condenser is located condensing equipment, the bin is located the below of condenser, it is concentrated that this enrichment facility that stepped down in steam heating vacuum can realize that steam steps down, have with low costs, concentration effect good, advantage that work efficiency is high.
Description
Technical field
The utility model relates to a kind of enrichment facility of steam heated vacuum pump-down.
Background technology
Evaporation and concentration is the difference utilizing solvent and solute volatility, thus the VLE condition that acquisition one is favourable, reach the object of separation; According to molecular motion viewpoint, when solution is heated, solvent molecule obtains kinetic energy, and when the energy of some solvent molecules is enough to overcome intermolecular attraction, solvent molecule liquid level of will overflowing enters upper space, becomes steam molecule, vaporization that Here it is; If do not manage to remove these steam molecules, then between vapour phase and liquid phase, the chemical potential of moisture will gradually balance, and vaporescence is also corresponding to be weakened so that stop carrying out gradually; Therefore the necessary condition of carrying out evaporating is exactly the continuous eliminating of the continuous supply of heat energy and the steam of generation.The equipment of current evaporation and concentration is numerous, with water-bath, electric hot plate heater with to vacuumize Rotary Evaporators more common, although water-bath can realize temperature control, homogeneous heating, evaporation and concentration efficiency is extremely slow, and maximum temperature is 100 DEG C, this also just becomes a large bottleneck of water-bath heating; Although electric hot plate heater can control temperature and temperature can reach more than 100 DEG C, heating surface area is little, and the phenomenon such as easily cause that local heating burns, and heat easily runs off, and causes its evaporation and concentration efficiency low.
Utility model content
The technical problems to be solved in the utility model is to provide one and can realizes steam pressure-reducing and concentrate, and has that cost is low, concentrated effect good, the enrichment facility of the steam heated vacuum pump-down that operating efficiency is high.
For solving the problem, the utility model adopts following technical scheme:
A kind of enrichment facility of steam heated vacuum pump-down, comprise steam heater and condensing unit, described steam heater comprises chuck and inner bag, described chuck parcel inner bag, leg is provided with bottom described chuck, steam vent and waste liquid outlet, left side in the middle part of described chuck is provided with steam inlet, described inner bag is provided with charging aperture, vacuum machine and gas-liquid separator, described charging aperture is positioned at the left side of inner bag, described vacuum machine is positioned at the right side of inner bag, and with inner bag Joint, described gas-liquid separator is positioned at the top of inner bag, and connect steam heater and condensing unit, described condensing unit bag condenser, circulating chilled water import and storage bin, described condenser is positioned at condensing unit, described storage bin is positioned at the below of condenser.
As preferably, in described steam vent and waste liquid outlet, be all provided with control valve, in concentration process, the concentrate in inner bag can be avoided to discharge, and prevent inner bag from not carrying out Steam Heating under vacuum conditions.
As preferably, described inner bag is arranged for sealing, is conducive to sealing inner container, makes inner bag carry out Steam Heating under vacuum conditions, make the enrichment of concentrate higher by the mode of step-down.
As preferably, described vapour liquid separator top is provided with arc-like rows gas hood, is conducive to carbonated drink to carry out vapor-liquid separation, and is discharged by air by arc-like rows gas hood.
As preferably, between described condensing unit and condenser, be provided with circulating chilled water wall, circulating chilled water cooling can be carried out for the obtained concentrate of steam heater in condensing unit.
The beneficial effects of the utility model are: owing to being provided with chuck, inner bag can be wrapped up, inner bag can be fixed, owing to being provided with steam inlet, steam can be inputted to inner bag, owing to being provided with vacuum machine, can by the air extraction in inner bag, inner bag is made to form vacuum, owing to being provided with vapour liquid separator, vapour-liquid can be separated, owing to being provided with condenser, can by visible layer of water condensate liquid, owing to being provided with circulating chilled water import, can make to carry out circulating chilled water in condensing unit, help and accelerate cooling, owing to being provided with storage bin, the concentrate cooled can be stored.
Accompanying drawing explanation
Fig. 1 is the overall structure schematic diagram of the enrichment facility of a kind of steam heated vacuum pump-down of the utility model.
Detailed description of the invention
As shown in Figure 1, a kind of enrichment facility of steam heated vacuum pump-down, comprise steam heater 1 and condensing unit 2, described steam heater 1 comprises chuck 3 and inner bag 8, described chuck 3 wraps up inner bag 8, leg 4 is provided with bottom described chuck 3, steam vent 5 and waste liquid outlet 6, left side in the middle part of described chuck 3 is provided with steam inlet 7, described inner bag 8 is provided with charging aperture 9, vacuum machine 10 and vapour liquid separator 11, described charging aperture 9 is positioned at the left side of inner bag 8, described vacuum machine 10 is positioned at the right side of inner bag 8, and with inner bag 8 Joint, described vapour liquid separator 11 is positioned at the top of inner bag 8, and connect steam heater 1 and condensing unit 2, described condensing unit 2 bag condenser 12, circulating chilled water import 13 and storage bin 14, described condenser 12 is positioned at condensing unit 2, described storage bin 14 is positioned at the below of condenser 12.
All be provided with control valve (not shown) in described steam vent 5 and waste liquid outlet 6, in concentration process, the concentrate in inner bag 8 can be avoided to discharge, and prevent inner bag from not carrying out Steam Heating under vacuum conditions.
Described inner bag 8 is arranged for sealing, is conducive to sealing inner container 8, makes inner bag 8 carry out Steam Heating under vacuum conditions, make the enrichment of concentrate higher by the mode of step-down.
Described vapour liquid separator 11 top is provided with arc-like rows gas hood, is conducive to carbonated drink to carry out vapor-liquid separation, and is discharged by air by arc-like rows gas hood.
Be provided with circulating chilled water wall between described condensing unit 2 and condenser 12, circulating chilled water cooling can be carried out for the obtained concentrate of steam heater 1 in condensing unit 1.
The beneficial effects of the utility model are: owing to being provided with chuck, inner bag can be wrapped up, inner bag can be fixed, owing to being provided with steam inlet, steam can be inputted to inner bag, owing to being provided with vacuum machine, can by the air extraction in inner bag, inner bag is made to form vacuum, owing to being provided with vapour liquid separator, vapour-liquid can be separated, owing to being provided with condenser, can by visible layer of water condensate liquid, owing to being provided with circulating chilled water import, can make to carry out circulating chilled water in condensing unit, help and accelerate cooling, owing to being provided with storage bin, the concentrate cooled can be stored.
The above, be only detailed description of the invention of the present utility model, but protection domain of the present utility model is not limited thereto, and any change of expecting without creative work or replacement, all should be encompassed within protection domain of the present utility model.
Claims (5)
1. the enrichment facility of a steam heated vacuum pump-down, it is characterized in that: comprise steam heater and condensing unit, described steam heater comprises chuck and inner bag, described chuck parcel inner bag, leg is provided with bottom described chuck, steam vent and waste liquid outlet, left side in the middle part of described chuck is provided with steam inlet, described inner bag is provided with charging aperture, vacuum machine and gas-liquid separator, described charging aperture is positioned at the left side of inner bag, described vacuum machine is positioned at the right side of inner bag, and with inner bag Joint, described gas-liquid separator is positioned at the top of inner bag, and connect steam heater and condensing unit, described condensing unit bag condenser, circulating chilled water import and storage bin, described condenser is positioned at condensing unit, described storage bin is positioned at the below of condenser.
2. the enrichment facility of a kind of steam heated vacuum pump-down as claimed in claim 1, is characterized in that: be all provided with control valve in described steam vent and waste liquid outlet.
3. the enrichment facility of a kind of steam heated vacuum pump-down as claimed in claim 2, is characterized in that: described inner bag is sealing setting.
4. the enrichment facility of a kind of steam heated vacuum pump-down as claimed in claim 3, is characterized in that: described gas-liquid separator top is provided with arc-like rows gas hood.
5. the enrichment facility of a kind of steam heated vacuum pump-down as claimed in claim 4, is characterized in that: be provided with circulating chilled water wall between described condensing unit and condenser.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520660156.2U CN204891255U (en) | 2015-08-29 | 2015-08-29 | Enrichment facility that stepped down in steam heating vacuum |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520660156.2U CN204891255U (en) | 2015-08-29 | 2015-08-29 | Enrichment facility that stepped down in steam heating vacuum |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204891255U true CN204891255U (en) | 2015-12-23 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520660156.2U Expired - Fee Related CN204891255U (en) | 2015-08-29 | 2015-08-29 | Enrichment facility that stepped down in steam heating vacuum |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204891255U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106730941A (en) * | 2016-12-28 | 2017-05-31 | 中核四0四有限公司 | The evaporation feeding device of HF in a kind of uranium conversion production process |
| CN107127115A (en) * | 2017-06-20 | 2017-09-05 | 芜湖夏鑫新型材料科技有限公司 | Diaphragm scrap rubber Water Sproading processing unit |
| CN115088795A (en) * | 2022-07-05 | 2022-09-23 | 梁和标 | Preparation method of herbal beverage |
-
2015
- 2015-08-29 CN CN201520660156.2U patent/CN204891255U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106730941A (en) * | 2016-12-28 | 2017-05-31 | 中核四0四有限公司 | The evaporation feeding device of HF in a kind of uranium conversion production process |
| CN106730941B (en) * | 2016-12-28 | 2019-04-16 | 中核四0四有限公司 | A kind of uranium converts the evaporation feeding device of HF in production process |
| CN107127115A (en) * | 2017-06-20 | 2017-09-05 | 芜湖夏鑫新型材料科技有限公司 | Diaphragm scrap rubber Water Sproading processing unit |
| CN115088795A (en) * | 2022-07-05 | 2022-09-23 | 梁和标 | Preparation method of herbal beverage |
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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 |
Granted publication date: 20151223 Termination date: 20160829 |
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| CF01 | Termination of patent right due to non-payment of annual fee |