CN209997217U - Double-shell type supergravity vaporizing device - Google Patents
Double-shell type supergravity vaporizing device Download PDFInfo
- Publication number
- CN209997217U CN209997217U CN201920460980.1U CN201920460980U CN209997217U CN 209997217 U CN209997217 U CN 209997217U CN 201920460980 U CN201920460980 U CN 201920460980U CN 209997217 U CN209997217 U CN 209997217U
- Authority
- CN
- China
- Prior art keywords
- shell
- rotating
- unit
- liquid
- hypergravity
- 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.)
- Active
Links
Images
Landscapes
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
A dual-shell supergravity vaporizer for vaporizing hot liquid is composed of an inner shell, a rotary baseplate, a rotary axle, a dispersing unit for dispersing said hot liquid, a dispersing space defined by said rotary baseplate and said dispersing unit, a temperature holding space defined by said inner shell and said outer shell, an inner gas outlet communicated with said dispersing space and said temperature holding space, and an outer gas outlet communicated with said temperature holding space.
Description
Technical Field
The utility model relates to an kinds of hypergravity vapourizing units, especially relate to kinds of double shell type hypergravity vapourizing units.
Background
Referring to fig. 1, there are conventional supergravity vaporization devices 1 capable of evaporating hot liquid, where the supergravity vaporization device 1 includes housings 11, rotating substrates 12, rotating shafts 13, dispersing units 14, conduits 15 and exhaust pipes 16, the dispersing units 14 are disposed on the rotating substrates 12 and are adapted to disperse the hot liquid, the rotating substrates 12 and the dispersing units 14 together define dispersing spaces 17, the conduits 15 extend from the outside of the housings 11 to the dispersing spaces 17, the exhaust pipes 16 communicate with the outside and the dispersing spaces 17, when the hot liquid to be evaporated enters the dispersing spaces 17 from the conduits 15, the rotating shafts 13 drive the rotating substrates 12 and the dispersing units 14 to rotate and the hot liquid to be evaporated is dispersed into smaller droplets by the dispersing units 14 to be evaporated, and finally, the gas formed after the hot liquid is evaporated is exhausted from the exhaust pipes 16.
Although the evaporation efficiency of the hot liquid can be improved by the dispersion unit 14 in the conventional supergravity evaporation device 1, the heat preservation effect is not good, and thus more energy is consumed to increase the temperature of the hot liquid to be evaporated, if the device is required to have the heat preservation effect, a heat preservation material is required to be additionally coated on the housing 11, which causes cost waste, and a condensing device is required to be arranged at the rear end to condense the evaporated liquid, and in addition, the exhaust pipe 16 is arranged at the top of the device, which causes the overall height of the device to be higher, which is disadvantageous to pipeline arrangement, therefore, the conventional supergravity evaporation device 1 is still to be improved by .
Disclosure of Invention
An object of the utility model is to provide kinds of better, the lower double-shelled hypergravity vapourizing unit of ability reduction energy consumption and its whole height of heat preservation effect.
The utility model discloses a double-shell type hypergravity vapourizing unit for the evaporation hot liquid, this double-shell type hypergravity vapourizing unit contains inner shell, rotatory base plate, rotation axis, dispersion unit, shell and pipe.
The rotating base plate is positioned in the inner shell and is spaced from the inner shell.
The rotating shaft is connected with the rotating base plate and extends out of the inner shell from the rotating base plate.
The dispersion unit is disposed on the rotating substrate and adapted to disperse the hot liquid, and the rotating substrate and the dispersion unit define a dispersion space together.
The outer shell is arranged outside the inner shell and surrounds the dispersing units at intervals in the radial direction of the rotating shaft, the inner shell and the outer shell define a temperature holding space together in a surrounding mode, the inner shell comprises an inner air outlet communicated with the dispersing space and the temperature holding space, and the outer shell comprises an outer air outlet communicated with the outside of the outer shell and the temperature holding space.
The conduit extends from the exterior of the housing to the dispersion space and is adapted to direct the hot liquid into the dispersion space.
The utility model discloses a double-shell type hypergravity vapourizing unit, this dispersion unit are the filling layer.
The utility model discloses a double-shell type hypergravity vapourizing unit, double-shell type hypergravity vapourizing unit still contains the liquid fog unit that removes who sets up in this dispersion unit top, and this liquid fog unit that removes includes:
an th gas-liquid separator plate disposed on the packed bed and connected to the duct in a gas-tight manner;
a liquid mist removing layer arranged above the th gas-liquid partition plate, and
and the second gas-liquid partition plate is arranged on the liquid-removing fog layer and is hermetically connected with the inner shell.
The utility model discloses a double-shell type hypergravity vapourizing unit, this inner shell still include by the interior gas outlet periphery of this extend to the interior diaphragma of giving vent to anger of this second gas-liquid baffle.
The utility model discloses a double-shell type hypergravity vapourizing unit, this dispersion unit includes:
a plurality of rotating annular walls which are spaced from each other and respectively extend from the rotating base plate in the axial direction of the rotating shaft, and the rotating annular wall which is positioned at the innermost side and the rotating base plate define the dispersing space; and
at least internal fixed ring walls are arranged between two adjacent rotating ring walls and extend from the inner shell in the axial direction of the rotating shaft beyond the ends of the adjacent rotating ring walls located at the inner side of the rotating shaft.
The utility model discloses a double-shell type hypergravity vapourizing unit, this dispersion unit still include by the outer fixed rampart that this inner shell extended in the axial of this rotation axis, this outer fixed rampart around setting up outside being located this rotatory rampart in the outside to it is terminal to extend to exceed this rotatory rampart that is located the outside.
The utility model discloses a double-shell type hypergravity vapourizing unit, this rotation axis are located this rotating base plate below, and this dispersion unit is located this rotating base plate top.
The utility model discloses a double-shell type hypergravity vapourizing unit, this go out gas port is close to the bottom of this shell.
The utility model discloses a double-shell type hypergravity vapourizing unit, double-shell type hypergravity vapourizing unit still contains intercommunication external and the inside gas transmission passageway of this inner shell.
The beneficial effects of the utility model reside in that: because the double-shell type hypergravity vaporization device of the utility model comprises the temperature holding space, the heat preservation effect is good and the energy consumption can be reduced; in addition, because the utility model discloses double-shelled hypergravity vapourizing unit does not contain the blast pipe that current hypergravity vapourizing unit necessarily need to set up in the device top, so the whole height of device is lower and is favorable to the configuration of pipeline.
To the explanation of the aforesaid heat preservation effect further step, the utility model discloses double-shell hypergravity vapourizing unit is after leading-in hot liquid wherein forms gas through the evaporation, and this gas can be earlier got into this space of holding the temperature via this interior gas outlet and then discharged by this gas port of going out, so this gas can be filled in this space of holding the temperature, and should hold partial gas in the space of holding the temperature and also can take place the condensation and release heat, again because should hold the heat that releases after gas in the space of holding the temperature and the gas condensation to this inner shell inside, can be like layer cladding outside heat preservation and to this inner shell inside production heat preservation effect, so the utility model discloses double-shell hypergravity vapourizing unit's heat preservation effect is good.
Drawings
Other features and advantages of the present invention will become apparent from the following detailed description of the preferred embodiments with reference to the accompanying drawings, in which:
FIG. 1 is a schematic cross-sectional view of illustrating a prior art supergravity vaporization device;
FIG. 2 is a schematic cross-sectional view of illustrating the embodiment of the dual shell hypergravity vaporization apparatus of the present invention;
FIG. 3 is a schematic cross-sectional view of illustrating this embodiment of the dual shell hypergravity vaporization device of the present invention;
FIG. 4 is a schematic cross-sectional view of illustrating second embodiments of the dual shell hypergravity vaporization unit of the present invention;
FIG. 5 is a schematic cross-sectional view of showing a third embodiment of of the dual-shell supergravity vaporization device of the present invention, an
Fig. 6 is a schematic cross-sectional view of illustrating fourth embodiments of the dual-shell supergravity vaporization device of the present invention.
Detailed Description
The invention will be further described in relation to the following examples , but it should be understood that this example is illustrative only and should not be construed as limiting the practice of the invention.
Before the present invention is described in detail, it should be noted that in the following description, similar components are denoted by the same reference numerals.
< embodiment >
Referring to fig. 2, the st embodiment of the present invention is used to evaporate hot liquids heated by external heaters (not shown), and has a good heat preservation effect and a low overall height, and the dual-shell type supergravity vaporizer comprises inner shells 21, rotating base plates 22, rotating shafts 23, dispersing units 24, outer shells 25 and guide tubes 26.
The rotating base 22 is located in the inner housing 21 and spaced apart from the inner housing 21.
The rotation shaft 23 is connected to the rotation base 22 and extends from the rotation base 22 to the outside of the inner housing 21, and can be driven to rotate by the outside.
The dispersing units 24 of the present embodiment are filling layers, and are disposed on the rotating base plate 22 and adapted to disperse the hot liquid, the dispersing units (i.e., filling layers) 24 are hollow cylinders extending in the axial direction of the rotating shaft 23, the rotating base plate 22 and the dispersing units 24 together define dispersing spaces 27, and the material filled in the dispersing units (i.e., filling layers) 24 is selected from a wire mesh, a glass ball, a plastic filler, activated carbon, zeolite, a metal plate, or a combination thereof.
The outer shell 25 is disposed outside the inner shell 21 and surrounds the dispersing unit 24 at intervals in the radial direction of the rotating shaft 23, and the inner shell 21 and the outer shell 25 together define temperature-holding spaces 28.
The inner casing 21 comprises inner air outlets 211 communicating the dispersion space 27 and the temperature-holding space 28, the outer casing 25 comprises outer air outlets 251 communicating the outside thereof with the temperature-holding space 28. in the present embodiment, the rotating shaft 23 is located below the rotating base plate 22, the dispersion unit 24 is located above the rotating base plate 22, the inner air outlets 211 are located above the dispersion space 27, the bottom of the outer casing 25 is located between the top and the bottom of the inner casing 21, and the outer air outlets 251 are located at the side of the outer casing 25 and adjacent to the bottom of the outer casing 25.
The conduit 26 extends from the outside of the housing 25 to the dispersion space 27 and is adapted to conduct the hot liquid into the dispersion space 27.
The dual-shell supergravity vaporizing apparatus of the embodiment further includes bearing seats 40, wherein the bearing seats 40 are disposed at the bottom of the inner shell 21, and the rotating shaft 23 extends out of the bearing seats 40.
In the dual-shell supergravity vaporization device of the embodiment , when the rotating shaft 23 is driven by the external to rotate so that the rotating base plate 22 and the dispersing unit 24 rotate relative to the inner shell 21, the heated hot liquid flows into the dispersing space 27 through the conduit 26, at this time, with the driving of the centrifugal force, referring to the direction of the dotted arrow in the left half of fig. 2, the hot liquid moves from inside to outside along the radial direction of the rotating shaft 23 to the dispersing unit (i.e., the filling layer) 24 and is thinned and dispersed into tiny droplets, liquid threads, or liquid films in the dispersing unit (i.e., the filling layer) 24 to evaporate after evaporation, the gas formed after evaporation of the hot liquid enters the temperature holding space 28 through the inner gas outlet 211 and then is discharged through the gas outlet 251, so that the gas is filled in the temperature holding space 28, and a portion of the gas in the temperature holding space 28 is condensed to release heat, and the entire vaporization device is disposed on the inner shell 21, thereby providing a better heat-preserving effect for the conventional dual-shell supergravity vaporization device, which is advantageous for solving the problems of the conventional heat-preserving pipeline disposed in the conventional heat-preserving pipeline, such as the conventional supergravity vaporization device.
It should be noted that the range of the outer shell 25 of the dual-shell supergravity vaporization device surrounding the inner shell 21 is not particularly limited, and the surrounding range can be adjusted according to the required heat preservation effect as long as the inner gas outlet 211 can surround the temperature-maintaining space 28, for example, referring to fig. 2, the bottom of the outer shell 25 of the dual-shell supergravity vaporization device can be lower than the bottom plane of the inner shell 21, or referring to fig. 3, the bottom of the outer shell 25 of the dual-shell supergravity vaporization device can also be located on planes together with the bottom of the inner shell 21.
< second embodiment >
Referring to fig. 4, the second embodiment of the present invention is similar to the embodiment, and the difference is that the double-shell type hypergravity vaporization apparatus of the present invention further includes liquid mist removing units 29 disposed above the dispersing unit (i.e. the filling layer) 24. the liquid mist removing unit 29 includes gas-liquid partition plates 291, liquid mist removing layers 292, and second gas-liquid partition plates 293.
The th gas-liquid partition 291 is disposed on the dispersion unit (i.e., the packed bed) 24, and is hermetically connected to the conduit 26 by th dynamic seals 294, and can block direct penetration of gas and fluid.
The liquid-mist removing layer 292 is disposed above the th gas-liquid partition 291, has hollow columns extending in the axial direction of the rotating shaft 23, and is used for blocking liquid droplets entrained by the gas passing through the rotating shaft 23 radially inward.
The second gas-liquid separation plate 293 is disposed on the mist-removing layer 292 and can be used to block the gas from directly penetrating therethrough, the inner casing 21 further includes inner gas outlet ring walls 212 extending from the periphery of the inner gas outlet 211 to the second gas-liquid separation plate 293, the second gas-liquid separation plate 293 is hermetically connected to the inner gas outlet ring walls 212 of the inner casing 21 by second dynamic seals 295, and the second dynamic seals 295 can be a straight seal or a labyrinth seal.
In the dual-shell type supergravity vaporization device according to the second embodiment, when the rotating shaft 23 is externally driven to rotate so that the rotating base plate 22 and the dispersion unit 24 rotate relative to the inner shell 21, the heated hot liquid simultaneously flows into the dispersion space 27 through the conduit 26, and at this time, the hot liquid moves from inside to outside along the radial direction of the rotating shaft 23 to the dispersion unit (i.e., the filling layer) 24 and is thinned and dispersed into minute liquid droplets, liquid filaments, or liquid films in the dispersion unit (i.e., the filling layer) 24 and then evaporates as the centrifugal force is driven and the dashed arrow in the left half of fig. 4 is referred to. Then, the gas formed after the hot liquid evaporates flows out from the inside of the dispersion unit 24, continues to flow upward and passes through the mist removing layer 292 from the outside to the inside in the radial direction of the rotating shaft 23, at this time, the liquid droplets entrained in the gas are blocked in the mist removing layer 292 and thrown out outwards along with the centrifugal force, so that the mist can be separated and removed from the gas in a counter-current manner by the gas and the blocked liquid, and the gas without entrained mist can be obtained. Finally, the dry gas passing through the liquid mist removing layer 292 enters the temperature maintaining space 28 through the inner gas outlet 211 and then is discharged through the outer gas outlet 251.
< third embodiment >
Referring to fig. 5, the third embodiment of the present invention is similar to the embodiment, and the difference is that the dispersion unit 24 of the present invention is a plurality of baffles, which is different from the packing layers of the second embodiment, and more specifically, the dispersion unit 24 of the present invention comprises three rotating ring walls 241, two inner fixed ring walls 242, and outer fixed ring walls 243.
The rotating annular walls 241 are spaced apart from each other and respectively extend from the rotating base 22 in the axial direction of the rotating shaft 23, and the innermost rotating annular wall 241 and the rotating base 22 define the dispersing space 27.
The inner fixing ring walls 242 are respectively disposed between two adjacent rotating ring walls 241, and extend from the inner shell 21 to the end of the rotating ring wall 241 located inside and adjacent to the inner fixing ring wall in the axial direction of the rotating shaft 23.
The outer fixing annular wall 243 extends from the inner casing 21 in the axial direction of the rotating shaft 23, surrounds the outermost rotating annular wall 241, and extends beyond the end of the outermost rotating annular wall 241.
It should be noted that, the number of the rotating annular wall 241 and the inner fixed annular wall 242 of the dual-shell supergravity vaporizing device of the present embodiment is not limited to the number illustrated in the present embodiment, and the number of the rotating annular wall 241 and the inner fixed annular wall 242 may be increased according to the requirement. For example, the number of the rotating annular walls 241 of the dual-shell supergravity vaporizing device of the present embodiment can be increased to four, and the number of the internal fixed annular walls 242 can be simultaneously increased to three.
In the dual-shell type supergravity vaporization device of the third embodiment, when the rotating shaft 23 is driven to rotate by the outside to rotate the rotating base plate 22 and the dispersing unit 24 relative to the inner shell 21, the heated hot liquid flows into the dispersing space 27 through the conduit 26 at the same time, and at this time, the hot liquid in the dispersing space 27 is driven by the centrifugal force caused by the rotation to sequentially contact the rotating annular wall 241, the inner fixed annular wall 242 and the outer fixed annular wall 243 from inside to outside, and is dispersed into tiny liquid droplets, liquid threads or liquid films and then evaporated. The gas formed by the evaporation of the hot liquid enters the temperature-maintaining space 28 through the inner gas outlet 211 and then is discharged through the outer gas outlet 251.
< fourth embodiment >
Referring to fig. 6, the fourth embodiment of the present invention is similar to the embodiment, and the difference is that the double-shell type hypergravity vaporization apparatus of the present invention further comprises gas transmission channels 30 for communicating the outside with the inside of the inner shell 21, and the gas transmission channels 30 can externally input hot gas (such as water vapor, organic vapor, air, nitrogen, etc.) to the inside of the inner shell 21 (i.e. the hot gas can enter the dispersion space 27).
The hot liquid of the fourth embodiment is formed by the hot gas supplied from the gas supply passage 30 contacting liquids introduced into the dispersion space 27 through the conduit 26.
In conclusion, the double-shell type supergravity vaporizing device comprises the temperature holding space 28, so that the heat preservation effect is good, and the energy consumption can be reduced; in addition, because the utility model discloses double-shelled hypergravity vapourizing unit does not contain the blast pipe that current hypergravity vapourizing unit necessarily set up in the device top, so the whole height of device is lower and be favorable to the configuration of pipeline, consequently, can reach the purpose of the utility model with the cost really.
The above description is only an example of the present invention, and the scope of the present invention should not be limited thereby, and all the simple equivalent changes and modifications made according to the claims and the description of the present invention are still within the scope of the present invention.
Claims (9)
1, A dual shell type supergravity vaporization device for vaporizing a hot liquid, comprising:
an inner shell;
a rotating base plate positioned in the inner shell and spaced from the inner shell;
a rotating shaft connected to the rotating base plate and extending from the rotating base plate to the outside of the inner shell;
a dispersion unit disposed on the rotating substrate and adapted to disperse the hot liquid, wherein the rotating substrate and the dispersion unit define a dispersion space together;
the outer shell is arranged outside the inner shell and surrounds the dispersing units at intervals in the radial direction of the rotating shaft, the inner shell and the outer shell jointly define a temperature holding space in a surrounding mode, the inner shell comprises an inner air outlet communicated with the dispersing space and the temperature holding space, and the outer shell comprises an outer air outlet communicated with the outside of the outer shell and the temperature holding space; and
a conduit extending from the exterior of the housing to the dispersion space adapted to direct the hot liquid into the dispersion space.
2. The dual shell hypergravity vaporization unit of claim 1, wherein: the dispersion unit is a filling layer.
3. The dual shell hypergravity vaporization unit of claim 2, wherein: the double-shell type hypergravity vaporization device further comprises a liquid-mist removing unit arranged above the dispersion unit, and the liquid-mist removing unit comprises:
an th gas-liquid separator plate disposed on the packed bed and connected to the duct in a gas-tight manner;
a liquid mist removing layer arranged above the th gas-liquid partition plate, and
and the second gas-liquid partition plate is arranged on the liquid-removing fog layer and is hermetically connected with the inner shell.
4. The dual shell hypergravity vaporization unit of claim 3, wherein: the inner shell also comprises an inner air outlet annular wall extending from the periphery of the inner air outlet to the second gas-liquid partition plate.
5. The dual shell hypergravity vaporization unit of claim 1, wherein: the dispersion unit includes:
a plurality of rotating annular walls which are spaced from each other and respectively extend from the rotating base plate in the axial direction of the rotating shaft, and the rotating annular wall which is positioned at the innermost side and the rotating base plate define the dispersing space; and
at least internal fixed ring walls are arranged between two adjacent rotating ring walls and extend from the inner shell in the axial direction of the rotating shaft beyond the ends of the adjacent rotating ring walls located at the inner side of the rotating shaft.
6. The dual shell hypergravity vaporization unit of claim 5, wherein: the dispersion unit further includes an outer fixed annular wall extending in the axial direction of the rotary shaft from the inner casing, the outer fixed annular wall being disposed around the outermost rotary annular wall and extending beyond the outermost end of the rotary annular wall.
7. The dual shell hypergravity vaporization unit of claim 1, wherein: the rotating shaft is located below the rotating substrate, and the dispersing unit is located above the rotating substrate.
8. The dual shell hypergravity vaporization unit of claim 7, wherein: the outer air outlet is adjacent to the bottom of the housing.
9. The dual shell hypergravity vaporization unit of claim 1, wherein: the double-shell type supergravity vaporization device also comprises a gas transmission channel for communicating the outside and the inside of the inner shell.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920460980.1U CN209997217U (en) | 2019-04-08 | 2019-04-08 | Double-shell type supergravity vaporizing device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920460980.1U CN209997217U (en) | 2019-04-08 | 2019-04-08 | Double-shell type supergravity vaporizing device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN209997217U true CN209997217U (en) | 2020-01-31 |
Family
ID=69303174
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201920460980.1U Active CN209997217U (en) | 2019-04-08 | 2019-04-08 | Double-shell type supergravity vaporizing device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN209997217U (en) |
-
2019
- 2019-04-08 CN CN201920460980.1U patent/CN209997217U/en active Active
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US5431716A (en) | Sorption device | |
| FI76699C (en) | INDUNSTARE AV ROERTYP. | |
| CN1549912A (en) | Method and apparatus for exchanging energy and/or mass | |
| WO2020093713A1 (en) | Heat exchange device and freeze dryer | |
| WO2017018208A1 (en) | Absorption heat pump device | |
| CN209997217U (en) | Double-shell type supergravity vaporizing device | |
| TWM582419U (en) | Dual-shell ultra-gravity vaporization device | |
| MXPA03010710A (en) | Tank manifold for internally mounted radial flow intercooler for a combustion air charger. | |
| JPH0221166A (en) | Absorption cycle heat pump | |
| TW202005693A (en) | Countercurrent type liquid mist removing high gravity device capable of achieving excellent liquid mist removing effect | |
| CN103908791A (en) | Condenser-built-in same-cavity reduced-pressure distillation device with two-time phase change | |
| GB2057113A (en) | Rotary heat exchange apparatus | |
| US10058816B2 (en) | Solid desiccant cooling system | |
| ES2365420T3 (en) | SHORT EVAPORATOR TRAVELED. | |
| CN104422313B (en) | Shell and tube heat exchanger and air conditioner with same | |
| CN107013893B (en) | Scale-free steam generator | |
| JPH11501394A (en) | Sorption device | |
| CN211393921U (en) | Evaporation concentration system | |
| CN105289451A (en) | Multi-layer zigzag rotating bed with heat exchange function | |
| US3990503A (en) | Regenerative heat exchanger | |
| US10166504B2 (en) | System and method for desorption of acid gas from an absorption liquid | |
| CN103968686A (en) | Efficient anti-plugging heat exchanger | |
| TWI750903B (en) | Reverse cross-flow supergravity device with gas choke ring wall | |
| JP2016205784A (en) | heat pump | |
| CN111380372B (en) | Closed cooling tower admits air to multistage |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |