CN205718530U - A kind of fractional condensaion dish structure being applicable to vacuum distilling - Google Patents
A kind of fractional condensaion dish structure being applicable to vacuum distilling Download PDFInfo
- Publication number
- CN205718530U CN205718530U CN201620364373.1U CN201620364373U CN205718530U CN 205718530 U CN205718530 U CN 205718530U CN 201620364373 U CN201620364373 U CN 201620364373U CN 205718530 U CN205718530 U CN 205718530U
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- China
- Prior art keywords
- condensate pans
- steam channel
- dish structure
- applicable
- fractional condensaion
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- 239000002184 metal Substances 0.000 claims abstract description 28
- 229910052751 metal Inorganic materials 0.000 claims abstract description 28
- 238000009434 installation Methods 0.000 claims abstract description 18
- 229910001338 liquidmetal Inorganic materials 0.000 claims abstract description 8
- 238000001704 evaporation Methods 0.000 abstract description 5
- 230000008020 evaporation Effects 0.000 abstract description 3
- 238000001291 vacuum drying Methods 0.000 abstract description 3
- 238000005272 metallurgy Methods 0.000 abstract description 2
- 238000009833 condensation Methods 0.000 description 17
- 230000005494 condensation Effects 0.000 description 17
- 238000000034 method Methods 0.000 description 4
- 238000009835 boiling Methods 0.000 description 2
- 238000005292 vacuum distillation Methods 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
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
- Y02P10/00—Technologies related to metal processing
- Y02P10/20—Recycling
Landscapes
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
This utility model relates to a kind of fractional condensaion dish structure being applicable to vacuum distilling, belongs to vacuum metallurgy equipment technical field.This is applicable to the fractional condensaion dish structure of vacuum distilling, including condensate pans and the steam channel being positioned at condensate pans centre position, it it is the inclined-plane that steam channel is high, end face is low bottom condensate pans, the straight line that condensate pans two ends minimum point is formed with steam channel respectively and horizontal angle are 5～10 °, being provided with condensing metal outlet bottom condensate pans, condensing metal outlet connects flow guiding disc or liquid metals collection device.This fractional condensaion dish structure being applicable to vacuum distilling uses multistage installation, is placed in the top of evaporation region in vacuum drying oven, and metal vapors prolongs steam channel entrance condensate pans after volatilize in evaporating pan.
Description
Technical field
This utility model relates to a kind of fractional condensaion dish structure being applicable to vacuum distilling, belongs to vacuum metallurgy equipment technical field.
Background technology
At present, in known continuous vacuum distillation resistance furnace, the general mode using total condensation, material directly condenses in condenser or cooling collection device after distilling from raw material, collects, or different condensation baffle plates is set outside condenser zone, realize the condensation of metal vapors, and enter discharging opening outflow by guiding device, it is thus achieved that liquid metals product.The a certain component of enrichment that can not orient in single distilled metal vapors in the first direct condensation process, cause product quality to reduce, reduce production efficiency.During the condensation arranging fractional condensaion cover, the temperature of condenser zone is uncontrollable, and is only applicable to process the vacuum drying oven that amount of metal is bigger.
Summary of the invention
The problem existed for above-mentioned prior art and deficiency, this utility model provides a kind of fractional condensaion dish structure being applicable to vacuum distilling.This fractional condensaion dish structure being applicable to vacuum distilling uses multistage installation, is placed in the top of evaporation region in vacuum drying oven, and metal vapors prolongs steam channel entrance condensate pans after volatilize in evaporating pan, this utility model is achieved through the following technical solutions.
A kind of fractional condensaion dish structure being applicable to vacuum distilling, including condensate pans 2 and the steam channel 1 being positioned at condensate pans 2 centre position, it it is the inclined-plane that steam channel 1 is high, end face is low bottom condensate pans 2, the straight line that condensate pans 2 two ends minimum point is formed with steam channel respectively and horizontal angle are 5～10 °, condensing metal outlet 3, condensing metal outlet 3 connection flow guiding disc or liquid metals collection device it is provided with bottom condensate pans 2.
Described fractional condensaion dish structure uses multistage installation, is provided with bayonet connection projection 4 bottom every one-level condensate pans 2, and every one-level condensate pans 2 inside top is provided with and groove 5, and this groove 5 coordinates installation with next stage bayonet connection protruding 4.
Described fractional condensaion dish structure uses three grades of installations, and one-level condensate pans is the condensate pans of bottom, and one-level condensate pans is minimum, collects a condensate, and by outlet 3 releasing；Uncooled steam enters B-grade condensation dish, B-grade condensation dish collection bigger than one-level condensate pans time condensation thing, and is released by outlet 3；Three grades of condensate pans are bigger than B-grade condensation dish, and in B-grade condensation dish, uncooled steam enters three grades of condensate pans, and three grades of condensate pans are bigger than B-grade condensation dish, collect three condensates, and by outlet 3 releasing；The fractional condensaion realizing metal vapors successively separates.
This one-level condensate pans be applicable to the fractional condensaion dish structure of vacuum distilling is closest from evaporation region, its condensation temperature is the highest, B-grade condensation dish temperature is taken second place, up temperature reduces successively, the condensate of higher metal is obtained in one-level condensate pans, B-grade condensation dish condenses the condensate of relatively low boiling metal, and the boiling point of the condensate metal of three grades of condensate pans acquisitions is lower, it is achieved the fractional condensaion of metal vapors.
The beneficial effects of the utility model are:
(1), in distillation condensation process, it is achieved the fractional condensaion of metal vapors, the condensed product of every one-level is collected, is improve separation efficiency.
(2) condensing unit is condensate pans at different levels composition in bulk, but it is easy to assembly, and condensation progression can be increased or decreased according to use condition.
(3) vaporising device and condensing unit are carried out in an airtight system, it is easy to collect, decrease the loss in metal vapors condensation process；
(4) during the structure of this condensate pans can be applicable to vacuum distillation furnace intermittently or serially, it is achieved the fractional condensaion of metal vapors and collection.
Accompanying drawing explanation
Fig. 1 is this utility model schematic top plan view figure；
Fig. 2 is this utility model A-A face cross-sectional schematic.
In figure: 1-steam channel, 2-condensate pans, 3-condensing metal exports, and 4-bayonet connection is protruding, 5-groove.
Detailed description of the invention
Below in conjunction with the accompanying drawings and detailed description of the invention, the utility model is described in further detail.
Embodiment 1
If Fig. 1 is to shown in 2, this is applicable to the fractional condensaion dish structure of vacuum distilling, including condensate pans 2 and the steam channel 1 being positioned at condensate pans 2 centre position, it it is the inclined-plane that steam channel 1 is high, end face is low bottom condensate pans 2, the straight line that condensate pans 2 two ends minimum point is formed with steam channel respectively and horizontal angle are 5～10 °, condensing metal outlet 3, condensing metal outlet 3 connection flow guiding disc or liquid metals collection device it is provided with bottom condensate pans 2.
Wherein fractional condensaion dish structure uses multistage installation, is provided with bayonet connection projection 4 bottom every one-level condensate pans 2, and every one-level condensate pans 2 inside top is provided with and groove 5, and this groove 5 coordinates installation with next stage bayonet connection protruding 4.
Embodiment 2
If Fig. 1 is to shown in 2, this is applicable to the fractional condensaion dish structure of vacuum distilling, including condensate pans 2 and the steam channel 1 being positioned at condensate pans 2 centre position, it it is the inclined-plane that steam channel 1 is high, end face is low bottom condensate pans 2, the straight line that condensate pans 2 two ends minimum point is formed with steam channel respectively and horizontal angle are 5～10 °, condensing metal outlet 3, condensing metal outlet 3 connection flow guiding disc or liquid metals collection device it is provided with bottom condensate pans 2.
Wherein fractional condensaion dish structure uses multistage installation, is provided with bayonet connection projection 4 bottom every one-level condensate pans 2, and every one-level condensate pans 2 inside top is provided with and groove 5, and this groove 5 coordinates installation with next stage bayonet connection protruding 4.Fractional condensaion dish structure uses three grades of installations, and one-level condensate pans is the condensate pans of bottom.
Embodiment 3
If Fig. 1 is to shown in 2, this is applicable to the fractional condensaion dish structure of vacuum distilling, including condensate pans 2 and the steam channel 1 being positioned at condensate pans 2 centre position, it it is the inclined-plane that steam channel 1 is high, end face is low bottom condensate pans 2, the straight line that condensate pans 2 two ends minimum point is formed with steam channel respectively and horizontal angle are 5～10 °, condensing metal outlet 3, condensing metal outlet 3 connection flow guiding disc or liquid metals collection device it is provided with bottom condensate pans 2.
Wherein fractional condensaion dish structure uses multistage installation, is provided with bayonet connection projection 4 bottom every one-level condensate pans 2, and every one-level condensate pans 2 inside top is provided with and groove 5, and this groove 5 coordinates installation with next stage bayonet connection protruding 4.Fractional condensaion dish structure uses three grades of installations, and one-level condensate pans is the condensate pans of bottom.
Embodiment 4
If Fig. 1 is to shown in 2, this is applicable to the fractional condensaion dish structure of vacuum distilling, including condensate pans 2 and the steam channel 1 being positioned at condensate pans 2 centre position, it it is the inclined-plane that steam channel 1 is high, end face is low bottom condensate pans 2, the straight line that condensate pans 2 two ends minimum point is formed with steam channel respectively and horizontal angle are 5～10 °, condensing metal outlet 3, condensing metal outlet 3 connection flow guiding disc or liquid metals collection device it is provided with bottom condensate pans 2.
Wherein fractional condensaion dish structure uses multistage installation, is provided with bayonet connection projection 4 bottom every one-level condensate pans 2, and every one-level condensate pans 2 inside top is provided with and groove 5, and this groove 5 coordinates installation with next stage bayonet connection protruding 4.Fractional condensaion dish structure uses three grades of installations, and one-level condensate pans is the condensate pans of bottom.
Above in association with accompanying drawing, detailed description of the invention of the present utility model is explained in detail, but this utility model is not limited to above-mentioned embodiment, in the ken that those of ordinary skill in the art are possessed, it is also possible on the premise of without departing from this utility model objective, various changes can be made.
Claims (2)
1. the fractional condensaion dish structure being applicable to vacuum distilling, it is characterized in that: include condensate pans (2) and be positioned at the steam channel (1) in condensate pans (2) centre position, condensate pans (2) bottom is the inclined-plane that steam channel (1) is high, end face is low, the straight line that condensate pans (2) two ends minimum point is formed with steam channel respectively and horizontal angle are 5～10 °, condensate pans (2) bottom is provided with condensing metal outlet (3), and condensing metal outlet (3) connects flow guiding disc or liquid metals collection device.
The fractional condensaion dish structure being applicable to vacuum distilling the most according to claim 1, it is characterized in that: described fractional condensaion dish structure uses multistage installation, it is protruding (4) that every one-level condensate pans (2) bottom is provided with bayonet connection, every one-level condensate pans (2) inside top is provided with and groove (5), and this groove (5) coordinates installation with next stage bayonet connection protruding (4).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620364373.1U CN205718530U (en) | 2016-04-27 | 2016-04-27 | A kind of fractional condensaion dish structure being applicable to vacuum distilling |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620364373.1U CN205718530U (en) | 2016-04-27 | 2016-04-27 | A kind of fractional condensaion dish structure being applicable to vacuum distilling |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205718530U true CN205718530U (en) | 2016-11-23 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620364373.1U Expired - Fee Related CN205718530U (en) | 2016-04-27 | 2016-04-27 | A kind of fractional condensaion dish structure being applicable to vacuum distilling |
Country Status (1)
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| CN (1) | CN205718530U (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111926524A (en) * | 2020-08-24 | 2020-11-13 | 长虹美菱股份有限公司 | Washing and drying integrated machine |
| CN112080646A (en) * | 2020-08-26 | 2020-12-15 | 昆明理工大学 | Method for removing arsenic and antimony in crude stannous sulfide of tin refining sulfur slag product treated by vacuum distillation |
| CN113368522A (en) * | 2021-07-02 | 2021-09-10 | 上海大学 | Vacuum distillation device and distillation method for indium |
| CN113444893A (en) * | 2020-03-27 | 2021-09-28 | 核工业理化工程研究院 | Height-adjustable vacuum multilayer evaporation device and evaporation method |
| CN113846231A (en) * | 2021-09-02 | 2021-12-28 | 昆明理工大学 | Vacuum gasification separation furnace for fractional volatilization |
| CN115522079A (en) * | 2022-05-17 | 2022-12-27 | 鲍少聪 | Recovery device for recovering rare earth metal from rare earth metal slag |
-
2016
- 2016-04-27 CN CN201620364373.1U patent/CN205718530U/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113444893A (en) * | 2020-03-27 | 2021-09-28 | 核工业理化工程研究院 | Height-adjustable vacuum multilayer evaporation device and evaporation method |
| CN111926524A (en) * | 2020-08-24 | 2020-11-13 | 长虹美菱股份有限公司 | Washing and drying integrated machine |
| CN112080646A (en) * | 2020-08-26 | 2020-12-15 | 昆明理工大学 | Method for removing arsenic and antimony in crude stannous sulfide of tin refining sulfur slag product treated by vacuum distillation |
| CN113368522A (en) * | 2021-07-02 | 2021-09-10 | 上海大学 | Vacuum distillation device and distillation method for indium |
| CN113846231A (en) * | 2021-09-02 | 2021-12-28 | 昆明理工大学 | Vacuum gasification separation furnace for fractional volatilization |
| CN115522079A (en) * | 2022-05-17 | 2022-12-27 | 鲍少聪 | Recovery device for recovering rare earth metal from rare earth metal slag |
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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: 20161123 Termination date: 20210427 |