CN202254925U - Heat transfer coagulation device for vapor water - Google Patents
Heat transfer coagulation device for vapor water Download PDFInfo
- Publication number
- CN202254925U CN202254925U CN2011203057287U CN201120305728U CN202254925U CN 202254925 U CN202254925 U CN 202254925U CN 2011203057287 U CN2011203057287 U CN 2011203057287U CN 201120305728 U CN201120305728 U CN 201120305728U CN 202254925 U CN202254925 U CN 202254925U
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- steam
- coagulator
- water
- flange
- coagulation
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Abstract
A heat transfer coagulation device for vapor water comprises a coagulation device casing, coagulation devices, steam bending pipes, a water inlet bending pipe and the like. A water inlet pipe is respectively arranged on two sides of the coagulation device casing, four coagulation devices are fixedly installed in the coagulation device casing in parallel, and four ways of steam bending pipes are connected in parallel with the four coagulation devices through steam inlet flanges. The four coagulation devices of the heat transfer coagulation device for vapor water are fixedly installed in the same casing in parallel, four groups of jet flow sprayers and tubes are arranged, water inlets and water outlets all adopt large-diameter flanges, so that a large amount of water through quantity can be maintained. Four jet flow devices are maintained to work simultaneously and are not interfered, so that jet flow mixing effect is better, heat loss is smaller, and simultaneously casing materials and space occupied by the space are saved.
Description
Technical field
The utility model relates to heating equipment, is specifically related to a kind of steam-water heat exchanging coagulator.
Background technology
Many users need use a large amount of high-temperature-hot-waters in therrmodynamic system is used, and its thermal source generally comes from steam power plant's afterheat steam, need many parallel connections to use when using standard DN40 bore steam-water heat exchanging device; Not only floor space is big; And because pipeline, valve are many, and the big heat loss of area of dissipation is also bigger, therefore in order to realize the high-efficiency large capacity steam-water heat exchanging; The general heavy caliber coagulator that adopts; But heavy caliber coagulator spout and tail pipe greater than DN80 after the increase of heat transfer sheet area be restricted, bore increases, heat but can not increase synchronously.
The utility model content
The utility model provides a kind of steam-water heat exchanging coagulator, and it is low to have solved old steam-water heat exchanging coagulator heat exchange efficiency, the problem that floor space is big.
For realizing above-mentioned purpose, adopt following technical scheme:
A kind of steam-water heat exchanging coagulator; Comprise coagulator housing, coagulator, steam bend pipe, water inlet bend pipe etc.; Respectively there is a water inlet bend pipe said coagulator housing both sides; Parallel connection is installed with four coagulators in the coagulator housing, and has four road steam bend pipes to insert four coagulators through the parallel connection simultaneously of steam inlet flange.
As a preferred version, said steam bend pipe inserts through the steam inlet flange of coagulator housing one end, and the coagulator housing other end has the hot water outlet flange, and water inlet bend pipe end has the cooling water inlet flange.
As further preferred version, steam inlet flange and hot water outlet flange are the DN250 flange, and the cooling water inlet flange is the DN150 flange.
As the preferred version in a nearlyer step, the coagulator in the said coagulator housing is the DN80 coagulator.
The utility model is fixedly mounted on four coagulator parallel connections in the same housing; And being provided with four groups of jet nozzles and trunnion, intake-outlet all adopts large-diameter flanged, thereby can keep being bigger than the water yield; Keep four ejectors to work simultaneously, do not disturb mutually; The jet mixed effect is better, and thermal loss is littler, has saved case material and equipment simultaneously again and has taken up an area of the space.
Description of drawings
According to embodiment and accompanying drawing the utility model is done further explain below.
Fig. 1 is the utility model general structure sketch map;
Fig. 2 is a coagulator main part cutaway view;
Fig. 3 is the right view of Fig. 2.
Among the figure:
1, coagulator housing; 2, steam bend pipe; 3, steam inlet flange; 4, water inlet bend pipe; 5, cooling water inlet flange; 6, hot water outlet flange; 7, coagulator; 8, outlet pipe.
The specific embodiment
Shown in Fig. 1 to 3; Provided a specific embodiment of the utility model; Comprise coagulator housing 1, steam bend pipe 2, steam inlet flange 3, water inlet bend pipe 4, cooling water inlet flange 5, hot water outlet flange 6, coagulator 7, outlet pipe 8 among the figure; Wherein coagulator housing 1 two ends are separately installed with steam inlet flange 3 and hot water outlet flange 6; Two of both sides water inlet bend pipe 4 ends are equipped with cooling water inlet flange 5, and wherein coagulator housing 1 four external steam bend pipes 2 are parallel-connected to 7, four outlet pipes 8 of four DN80 coagulators of being fixedly mounted in the coagulator housing 1 from 6 outputs of hot water outlet flange through steam inlet flange 3; Wherein steam inlet flange 3 all adopts heavy caliber DN250 flange with hot water outlet flange 6, and the cooling water inlet flange 5 on the water inlet bend pipe 4 is the DN150 flange.
In the present embodiment; For fluidic device reduces heat waste and practices thrift steel, four groups of DN80 coagulators are uniformly distributed be installed in the same housing, the space between coagulator nozzle and the trunnion is a common space; Cold water this is sucked trunnion by steam jet in the vapor mixing heat exchange; Steam chance cold water condenses and emits heat water temperature is raise, and Venturi effect guarantees carbonated drink mixing, and latent heat of vaporization power conversion raises hydraulic pressure simultaneously; Make the outlet heat hydraulic pressure can be higher than the import cold water pressure, realize that energy makes full use of.Steam inlet flange and hot water outlet flange on the housing are accomplished DN250; And cooling water inlet is because structural limitations is designed to two DN150 of bilateral as the cooling water inlet flange; Thereby guaranteed the water yield 400 tons/time more than; This structure both can keep former four ejectors and work simultaneously, do not disturb mutually; The jet mixed effect is better, and thermal loss is littler, can save case material and equipment simultaneously again and take up an area of the space.
The utility model is fixedly mounted on four coagulator parallel connections in the same housing, makes that the jet mixed effect is better, and thermal loss is littler, has saved case material and equipment simultaneously again and has taken up an area of the space.
Claims (4)
1. steam-water heat exchanging coagulator; Comprise coagulator housing, coagulator, steam bend pipe, water inlet bend pipe etc.; It is characterized in that; Respectively there is a water inlet bend pipe said coagulator housing both sides, and parallel connection is installed with four coagulators in the coagulator housing, and have four road steam bend pipes to insert four coagulators through the parallel connection simultaneously of steam inlet flange.
2. a kind of steam-water heat exchanging coagulator according to claim 1 is characterized in that, said steam bend pipe inserts through the steam inlet flange of coagulator housing one end, and the coagulator housing other end has the hot water outlet flange, and water inlet bend pipe end has the cooling water inlet flange.
3. a kind of steam-water heat exchanging coagulator according to claim 1 is characterized in that steam inlet flange and hot water outlet flange are the DN250 flange, and the cooling water inlet flange is the DN150 flange.
4. a kind of steam-water heat exchanging coagulator according to claim 1 is characterized in that, the coagulator in the said coagulator housing is the DN80 coagulator.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011203057287U CN202254925U (en) | 2011-08-22 | 2011-08-22 | Heat transfer coagulation device for vapor water |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011203057287U CN202254925U (en) | 2011-08-22 | 2011-08-22 | Heat transfer coagulation device for vapor water |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202254925U true CN202254925U (en) | 2012-05-30 |
Family
ID=46116155
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011203057287U Expired - Fee Related CN202254925U (en) | 2011-08-22 | 2011-08-22 | Heat transfer coagulation device for vapor water |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202254925U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103256588A (en) * | 2013-05-24 | 2013-08-21 | 张家港十方电力科技有限公司 | Steam heater |
| CN104061796A (en) * | 2014-06-17 | 2014-09-24 | 中科华核电技术研究院有限公司 | Vapor and liquid two-phase fluid mixing condensation device |
| CN105225706A (en) * | 2015-08-26 | 2016-01-06 | 成都七博新能源研究所 | The coagulator of Natural Circulation and forced circulation circuit system and regulator design method |
-
2011
- 2011-08-22 CN CN2011203057287U patent/CN202254925U/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103256588A (en) * | 2013-05-24 | 2013-08-21 | 张家港十方电力科技有限公司 | Steam heater |
| CN104061796A (en) * | 2014-06-17 | 2014-09-24 | 中科华核电技术研究院有限公司 | Vapor and liquid two-phase fluid mixing condensation device |
| CN104061796B (en) * | 2014-06-17 | 2016-03-23 | 中科华核电技术研究院有限公司 | Vehicle repair major fluid condensation by mixing device |
| CN105225706A (en) * | 2015-08-26 | 2016-01-06 | 成都七博新能源研究所 | The coagulator of Natural Circulation and forced circulation circuit system and regulator design method |
| CN105225706B (en) * | 2015-08-26 | 2018-09-25 | 成都七博新能源研究所 | The coagulator and regulator design method of Natural Circulation and forced circulation circuit system |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| ASS | Succession or assignment of patent right |
Owner name: ANNENG ZHIDA ENERGY SAVING AND ENVIRONMENTAL PROTE Free format text: FORMER OWNER: BEIJING CITY AUTOMATIC SYSTEM COMPLETE ENGINEERING CO. Effective date: 20141210 |
|
| C41 | Transfer of patent application or patent right or utility model | ||
| COR | Change of bibliographic data |
Free format text: CORRECT: ADDRESS; FROM: 100000 DONGCHENG, BEIJING TO: 300457 HANGU, TIANJIN |
|
| TR01 | Transfer of patent right |
Effective date of registration: 20141210 Address after: 300457 B-432 room, Telford new world science and technology building, 131 Dongting Road, Dongting Road, Tianjin Patentee after: It's an energy saving and environmental protection technology (Tianjin) Co., Ltd. Address before: 100000 Beijing city Dongcheng District Wai Xing habitat No. 9 Patentee before: Beijing Controls Company |
|
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20120530 Termination date: 20150822 |
|
| EXPY | Termination of patent right or utility model |