CN203719489U - Double-phase-change latent heat exchanger - Google Patents
Double-phase-change latent heat exchanger Download PDFInfo
- Publication number
- CN203719489U CN203719489U CN201420036603.2U CN201420036603U CN203719489U CN 203719489 U CN203719489 U CN 203719489U CN 201420036603 U CN201420036603 U CN 201420036603U CN 203719489 U CN203719489 U CN 203719489U
- Authority
- CN
- China
- Prior art keywords
- steam
- liquid
- heat exchange
- cover body
- phase
- 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
Landscapes
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
The utility model discloses a double-phase-change latent heat exchanger which comprises heat exchange units. Each heat exchange unit comprises a sealing shell, an upper sealing barrier and a lower sealing barrier are arranged in each shell, a plurality of vertical tubes are arranged between each upper sealing barrier and the corresponding lower sealing barrier, middle chambers are formed by each sealing shell in an encircled manner and are positioned among the corresponding vertical tubes, the corresponding upper sealing barrier and the corresponding lower sealing barrier, a steam chamber is arranged on the upper side of each upper sealing barrier, and top openings of the various vertical tubes are communicated with the steam chambers; the bottoms of the various vertical tubes of each sealing shell are communicated with a liquid chamber; length-diameter ratios of the vertical tubes are smaller than 20; first steam access openings are formed in the shells and are positioned at the steam chambers, second steam access openings are formed in the shells and are positioned at the middle chambers, first liquid access openings are formed in the shells and are positioned at the bottoms of the middle chambers, and second liquid access openings are formed in the shells and are positioned at the liquid chambers. The double-phase-change latent heat exchanger has the advantages that double-phase-change latent heat exchange can be normally carried out, the density of heat flow which flows through heat exchange surfaces can be greatly increased, accordingly, the size of the heat exchanger can be greatly reduced, and at least 95% of energy which is consumed when single-phase-change heat exchange is carried out and cooling working media are delivered can be saved.
Description
Technical field
The utility model relates to technical field of heat exchangers.
Background technology
Conventional heat exchanger is when work, and the medium of its heat-transfer surface both sides does not generally undergo phase transition, such as liquid/liquid, gas/gas, gas/liquid heat exchange.Or the medium of heat-transfer surface one side undergoes phase transition, such as steam/liquid, steam/hot-air heater.Without phase-change heat-exchanger, can only transmit the sensible heat of material, latent heat is emitted in the steam end generation condensation phase transformation of one-sided phase transformation heater, and opposite side liquid or gas material do not have phase transformation, and just temperature is raised.Conventionally the sensible heat amount of material wants specific latent heat amount much smaller, so same heat exchange amount, traditional heat exchangers needs very large equipment size conventionally, and a large amount of liquid or gas conveying energy consumption.
Conventional heat exchanger has two kinds: plate type heat exchanger and shell-and-tube heat exchanger.Why there is not the heat exchanger that the medium of heat-transfer surface both sides all undergoes phase transition, be because existing two kinds of heat exchangers are all not suitable with the working condition that two-phase becomes, and this lacked to regular understanding.
Creative research through present inventor, existing two kinds of heat exchangers are not suitable with to the two-phase reason of doing of exchanging work and have had regular understanding, be that material is when undergo phase transition, must be accompanied by the acute variation of volume flow, gap between plate type heat exchanger heat-transfer surface is less, so be difficult to adapt to this variation, can not be as two phase-change heat-exchangers; The shell side of shell-and-tube heat exchanger normally length is greater than diameter, and (draw ratio refers to the ratio of the boiling in ducts liquid level degree of depth and pipe diameter to single tube draw ratio.) be generally far longer than 20; The phase transformation side of seething with excitement in this case must cause acutely mixed state of gas-liquid, condensation phase transformation side windage loss is large, tube bank effect is obvious, liquid film thermal resistance effect is strong, these combined factors together, cause long tube (long tube refer to draw ratio be greater than 20 pipe) design cannot stablize and undergo phase transition heat transfer.
Summary of the invention
The purpose of this utility model is to provide a kind of two-phase that can significantly dwindle heat exchanger volume, reduction medium transport energy consumption to become latent heat exchanger.
For achieving the above object, two-phase of the present utility model becomes latent heat exchanger and comprises heat exchange unit, heat exchange unit comprises seal casinghousing, in housing, be interval with up and down sealing baffle and lower seal baffle plate, between upper and lower sealing baffle, be evenly provided with some vertical tubes, housing between vertical tube and upper and lower sealing baffle surrounds intermediate cavity, and upper sealing baffle top is provided with steam chambers, and the open top of each vertical tube is connected with steam chambers; Each vertical tube bottom is all connected with a liquid chamber, and liquid chamber is positioned at lower seal baffle plate below and faces mutually with lower seal baffle plate; The draw ratio of described vertical tube is less than 20; The housing at described steam chambers place is provided with the first steam and imports and exports, the housing at described intermediate cavity top is provided with the second steam and imports and exports, the housing of described intermediate cavity bottom is provided with first liquid and imports and exports, and the housing at described liquid chamber place is provided with second liquid and imports and exports.
Described heat exchange unit stacked on top is provided with more than two.
Described each heat exchange unit being stacked is all placed in a cover body, each heat exchange unit and cover body surround steam void, in cover body, be provided with steam pipe, steam pipe selects to be communicated with the first steam import and export or the second steam is imported and exported, and the top of steam pipe protrudes upward cover body; In cover body, be provided with liquid pipe, liquid pipe selects to be communicated with first liquid import and export or second liquid is imported and exported, and the bottom of liquid pipe is stretched out cover body downwards; The sidewall middle part of described cover body is provided with cover body steam inlet, and the bottom of described cover body is communicated with cover body liquid outlet.
The case top of the heat exchange unit of top is end enclosure structure, and the housing bottom of the heat exchange unit of bottommost is end enclosure structure.
The utlity model has following advantage:
The draw ratio of vertical tube is less than 20, phase transformation one side of can avoiding seething with excitement causes acutely mixed phenomenon of gas-liquid, avoid the phenomenons such as condensation phase transformation side windage loss is large, tube bank effect is obvious, liquid film thermal resistance effect is strong, thereby guarantee stable condensation or boiling, guarantee heat exchange efficiency.The utility model can guarantee normally carrying out of two phase-change heat-exchanges, adopt two kinds of inside and outside working medias of vertical tube all to undergo phase transition the working method of (working media that is tube side and shell side all undergoes phase transition), the utility model has improved the heat flow density by heat-transfer surface greatly, thereby can greatly reduce the size of heat exchanger, effectively realize the heat exchange of latent heat high density, also saved the energy consuming when more than 95% liquid or gas (being working media) are carried simultaneously.
Elementary cell is used short tube, and floor space is conventionally larger; Use stacking method, a plurality of heat exchange unit stacked on top are gathered together, so not only floor space is little, and the mutual balance of the pressure between each heat exchange unit, and pressure vessel more easily designs.
If cover body is not set, each heat exchange unit will externally connect 4 pipelines, causes external pipe not only much but also more random, increases the compact degree that connects difficulty and make to reduce equipment.Owing to being provided with cover body, the steam state of volume flow maximum stream just can be cancelled distribution pipeline.Do like this that not only flow distribution is more even, integral device compact appearance simultaneously, comprehensive heat exchange efficiency is also high; Be used for interior coagulating while boiling formula outward, the circumferential surface of unit also can be used for condensing heat-exchange, and heat exchange area significantly improves.Finally, the utility model is simple in structure, is convenient to manufacture and use.
In a word, the utility model can guarantee normally carrying out of two phase-change heat-exchanges, has greatly improved the heat flow density by heat-transfer surface, thereby can greatly reduce the size of heat exchanger and save the energy consuming when more than 95% working media is carried.Stacked on top arranges a plurality of heat exchange units, and cover body is set, and can simplify syndeton of the present utility model, makes integral device compacter, and makes the flow distribution ground of working media more even, improves comprehensive heat exchange efficiency.
Accompanying drawing explanation
Fig. 1 is the structural representation of heat exchange unit in the utility model;
Fig. 2 is three heat exchange unit stacked on top structural representations together;
Fig. 3 is structural representation of the present utility model while being provided with cover body.
The specific embodiment
As shown in Figure 1, Figure 2 and Figure 3, two-phase of the present utility model becomes latent heat exchanger and comprises heat exchange unit, heat exchange unit comprises seal casinghousing 1, interior sealing baffle 2 and the lower seal baffle plate 3 of being interval with up and down of housing 1, between upper and lower sealing baffle 2,3, be evenly provided with some vertical tubes 4, housing 1 between vertical tube 4 and upper and lower sealing baffle 2,3 surrounds intermediate cavity 5, and upper sealing baffle 2 tops are provided with steam chambers 6, and the open top of each vertical tube 4 is connected with steam chambers 6; Each vertical tube 4 bottoms are all connected with a liquid chamber 7, and liquid chamber 7 is positioned at lower seal baffle plate 3 belows and faces mutually with lower seal baffle plate 3; The draw ratio of described vertical tube 4 is less than 20, and those skilled in the art can choose different draw ratios according to different material character.
The housing 1 at described steam chambers 6 places is provided with the first steam and imports and exports 8, the housing 1 at described intermediate cavity 5 tops is provided with the second steam and imports and exports 9, the housing 1 of described intermediate cavity 5 bottoms is provided with first liquid and imports and exports 10, and the housing 1 at described liquid chamber 7 places is provided with second liquid and imports and exports 11.The caliber of first, second liquid entrance 10,11 is less than first, second steam and imports and exports 8,9 caliber.
Described heat exchange unit stacked on top is provided with more than two.Described each heat exchange unit being stacked is all placed in a cover body 12, and each heat exchange unit and cover body 12 surround steam void 13.
In cover body 12, be provided with steam pipe 14, steam pipe 14 is selected to be communicated with the first steam and is imported and exported the 8 or second steam import and export 9, and the top of steam pipe 14 protrudes upward cover body 12.
In cover body 12, be provided with liquid pipe 15, liquid pipe 15 selects to be communicated with first liquid import and export 10 or second liquid imports and exports 11, and the bottom of liquid pipe 15 is stretched out cover body 12 downwards.
The sidewall middle part of described cover body 12 is provided with cover body steam inlet 16, and the bottom of described cover body 12 is communicated with cover body liquid outlet 17.
Housing 1 top of the heat exchange unit of top is end enclosure structure, and housing 1 bottom of the heat exchange unit of bottommost is end enclosure structure.
The working media that the utility model adopts: the medium undergoing phase transition has different choice, such as: water, ammonia, carbon dioxide etc.; All kinds of simple substance cold-producing mediums or mixed non-azeotropic refrigerant (CFC class, HCFC class, HFC class, R400 etc.); Each hydrocarbon (propane, ethanol, ethene, acetone etc.).Based on the technical solution of the utility model, those skilled in the art have the ability need to select suitable working media according to practical application.
The utility model is applicable to all kinds of Low Temperature Steams and reclaims occasion, particularly combines with mechanical compression type heat pump.
Be used on the evaporimeter of source pump, can directly reclaim the latent heat of Low Temperature Steam, cancelled water consumption, water conveying energy consumption and cooling tower investment and the running expense of water condenser, and improved recovered temperature and then improved source pump overall efficiency.
Be used on the condenser of source pump, can directly produce steam for industrial production line.Particularly be used on each quasi-tradition evaporation concentration equipment.Tradition evaporation concentration equipment all consumes external Boiler Steam in a large number, and uses condenser in conjunction with cooling tower, final stage Low Temperature Steam to be directly discharged in atmosphere.Utilize the utility model, the final stage Low Temperature Steam of evaporation concentration equipment is introduced to the evaporimeter of source pump, the high-temperature steam that source pump condenser is produced is directly sent evaporation concentration equipment back to, can fully phase out like this use of external Boiler Steam, thereby greatly reduce energy-output ratio.On basis of the present utility model, also can adopt all kinds of surface peening heat transfer technologies, promote overall efficiency, reduce heat transfer temperature difference, reduce cost of investment.
During use, two-phase of the present utility model becomes latent heat exchanger and both can adopt and boil in solidifying outward and (refer to be evaporated to gaseous state after medium in each vertical tube 4 is absorbed heat by liquid state, simultaneously the medium in outer, the intermediate cavity 5 of each vertical tube 4 is that pipe shell journey medium is by being condensed into liquid state after gaseous state heat release) working method, also can adopt interior solidifying outer working method of boiling.
While adopting the working method of boiling in outer coagulating, as shown in Figure 3, steam pipe 14 is communicated with the first steam and imports and exports 8, and liquid pipe 15 is communicated with second liquid import and export 11 simultaneously.Heat transfer process is: high-temperature steam enters steam void 13 by cover body steam inlet 16, then by the second steam of each heat exchange unit, import and export 9 and enter intermediate cavity 5, carry out obtaining condensation after heat exchange with the evaporative medium in each vertical tube 4, the liquid forming after condensation is imported and exported 10 by first liquid and is flowed out intermediate cavity 5, then drop on the bottom of steam void 13, and flow out cover body 12 by cover body liquid outlet 17; Meanwhile, liquid evaporative medium flows into cover body 12 by cover body liquid outlet 17, by entering the second liquid of each heat exchange unit after liquid pipe 15, imports and exports 11; Then, liquid evaporative medium flows into each vertical tube 4 through liquid chamber 7, while flowing through vertical tube 4, liquid evaporative medium obtains evaporating after the heat of out-tubular condensing medium, the gas forming after evaporation successively through steam chambers 6, the first steam import and export 8 and steam pipe 14 after flow out cover body 12.
While boiling interior solidifying working method outside adopting, steam pipe 14 is communicated with the second steam and imports and exports 9, and liquid pipe 15 is communicated with first liquid import and export 10 simultaneously.Heat transfer process is: the high-temperature steam of evaporative medium enters steam void 13 by cover body steam inlet 16, then by the first steam of each heat exchange unit, import and export 8 and enter intermediate cavity 5, carry out obtaining condensation after heat exchange with the evaporative medium in each vertical tube 4, the liquid forming after condensation is imported and exported 11 by second liquid and is flowed out intermediate cavity 5, then drop on the bottom of steam void 13, and flow out cover body 12 by cover body liquid outlet 17; Meanwhile, liquid evaporative medium flows into cover body 12 by cover body liquid outlet 17, by entering the first liquid of each heat exchange unit after liquid pipe 15, imports and exports 10; Then, liquid evaporative medium flows into each vertical tube 4 through liquid chamber 7, while flowing through vertical tube 4, liquid evaporative medium obtains evaporating after the heat of out-tubular condensing medium, the gas forming after evaporation successively through steam chambers 6, the second steam import and export 9 and steam pipe 14 after flow out cover body 12.
The utility model can guarantee normally carrying out of two phase-change heat-exchanges, has greatly improved the heat flow density by heat-transfer surface, thereby can greatly reduce the size of heat exchanger and save the energy consuming when more than 95% working media is carried.Stacked on top arranges a plurality of heat exchange units, and cover body 12 is set, and can simplify syndeton of the present utility model, makes integral device compacter, and makes the flow distribution ground of working media more even, improves comprehensive heat exchange efficiency.
Above embodiment is the unrestricted the technical solution of the utility model in order to explanation only, although the utility model is had been described in detail with reference to above-described embodiment, those of ordinary skill in the art is to be understood that: still can modify or be equal to replacement the utility model, and not departing from any modification or partial replacement of spirit and scope of the present utility model, it all should be encompassed in the middle of claim scope of the present utility model.
Claims (4)
1. two-phase becomes latent heat exchanger, it is characterized in that: comprise heat exchange unit, heat exchange unit comprises seal casinghousing, in housing, be interval with up and down sealing baffle and lower seal baffle plate, between upper and lower sealing baffle, be evenly provided with some vertical tubes, housing between vertical tube and upper and lower sealing baffle surrounds intermediate cavity, and upper sealing baffle top is provided with steam chambers, and the open top of each vertical tube is connected with steam chambers; Each vertical tube bottom is all connected with a liquid chamber, and liquid chamber is positioned at lower seal baffle plate below and faces mutually with lower seal baffle plate; The draw ratio of described vertical tube is less than 20;
The housing at described steam chambers place is provided with the first steam and imports and exports, the housing at described intermediate cavity top is provided with the second steam and imports and exports, the housing of described intermediate cavity bottom is provided with first liquid and imports and exports, and the housing at described liquid chamber place is provided with second liquid and imports and exports.
2. two-phase according to claim 1 becomes latent heat exchanger, it is characterized in that: described heat exchange unit stacked on top is provided with more than two.
3. two-phase according to claim 2 becomes latent heat exchanger, it is characterized in that: described in each heat exchange unit of being stacked be all placed in a cover body, each heat exchange unit and cover body surround steam void,
In cover body, be provided with steam pipe, steam pipe selects to be communicated with the first steam import and export or the second steam is imported and exported, and the top of steam pipe protrudes upward cover body;
In cover body, be provided with liquid pipe, liquid pipe selects to be communicated with first liquid import and export or second liquid is imported and exported, and the bottom of liquid pipe is stretched out cover body downwards;
The sidewall middle part of described cover body is provided with cover body steam inlet, and the bottom of described cover body is communicated with cover body liquid outlet.
4. according to the two-phase described in claim 2 or 3, become latent heat exchanger, it is characterized in that: the case top of the heat exchange unit of top is end enclosure structure, the housing bottom of the heat exchange unit of bottommost is end enclosure structure.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420036603.2U CN203719489U (en) | 2014-01-21 | 2014-01-21 | Double-phase-change latent heat exchanger |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420036603.2U CN203719489U (en) | 2014-01-21 | 2014-01-21 | Double-phase-change latent heat exchanger |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203719489U true CN203719489U (en) | 2014-07-16 |
Family
ID=51158633
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420036603.2U Expired - Fee Related CN203719489U (en) | 2014-01-21 | 2014-01-21 | Double-phase-change latent heat exchanger |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203719489U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103791744A (en) * | 2014-01-21 | 2014-05-14 | 郑州四维淀粉技术开发有限公司 | Double-phase-change latent heat exchanger |
| CN104075489A (en) * | 2014-07-19 | 2014-10-01 | 烟台明辉热泵节能科技有限公司 | High-temperature steam heat pump unit |
-
2014
- 2014-01-21 CN CN201420036603.2U patent/CN203719489U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103791744A (en) * | 2014-01-21 | 2014-05-14 | 郑州四维淀粉技术开发有限公司 | Double-phase-change latent heat exchanger |
| CN103791744B (en) * | 2014-01-21 | 2017-02-08 | 郑州四维淀粉技术开发有限公司 | Double-phase-change latent heat exchanger |
| CN104075489A (en) * | 2014-07-19 | 2014-10-01 | 烟台明辉热泵节能科技有限公司 | High-temperature steam heat pump unit |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN100587383C (en) | Heat-storing heat exchanger | |
| CN101666589B (en) | Combined heat pipe exchanger | |
| CN101245971B (en) | Enclosed cavity type heat exchanger | |
| CN103090712A (en) | Full liquid type medium and high temperature heat accumulator and application thereof in flue gas waste heat recovery | |
| CN103245226A (en) | Small liquefied natural gas vaporizer | |
| CN104596107A (en) | Outer disc microchannel liquid dividing condensation type heat-pump water heater water tank | |
| CN203478730U (en) | Horizontal shell-and-tube water-cooled condenser | |
| CN203719489U (en) | Double-phase-change latent heat exchanger | |
| CN104390492B (en) | A kind of horizontal pair of phase-change heat-exchanger | |
| CN103791744B (en) | Double-phase-change latent heat exchanger | |
| CN105020942B (en) | A kind of more package full-liquid type heat exchangers | |
| CN204177245U (en) | Horizontal pair of phase-change heat-exchanger | |
| CN204359169U (en) | A kind of horizontal pair of phase-change heat-exchanger | |
| CN103185425B (en) | Shell-and-tube sewage-refrigerant phase change heat exchanger | |
| CN201935605U (en) | Spiral coil heat exchanger | |
| CN204923933U (en) | Evaporative condenser | |
| CN204513776U (en) | Separatory condensation type heat pump water-heater water tank | |
| CN205066242U (en) | Cauldron formula flooded evaporator | |
| CN103673412A (en) | Double-level falling film evaporator | |
| CN203803134U (en) | Reduced pressure distiller capable of performing two-time phase change in same cavity and with built-in condenser | |
| CN105953476A (en) | Heat pipe falling film generator for low grade heat drive absorption refrigeration | |
| CN202835940U (en) | Air return superheater | |
| CN201811622U (en) | Radial heat pipe heat exchanger | |
| CN204705076U (en) | A kind of many packages full-liquid type heat exchanger | |
| CN103954158B (en) | Heat-accumulating type heat exchanger and steam-water separator thereof |
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: 20140716 Termination date: 20180121 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |