CN205156693U - Novel floating heat recuperator equipment - Google Patents
Novel floating heat recuperator equipment Download PDFInfo
- Publication number
- CN205156693U CN205156693U CN201520784132.8U CN201520784132U CN205156693U CN 205156693 U CN205156693 U CN 205156693U CN 201520784132 U CN201520784132 U CN 201520784132U CN 205156693 U CN205156693 U CN 205156693U
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- China
- Prior art keywords
- shell
- sewage draining
- draining exit
- drain
- steam inlet
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- Expired - Fee Related
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- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
The utility model provides a novel floating heat recuperator equipment, including relief valve, hot water mouth, branch road pipe connector mouth, manometer, the reactor of dividing, support frame, condensate outlet, drain, steam inlet, shell, the shell top sets up the relief valve and the relief valve imbeds in the shell surface, relief valve one side sets up the hot water mouth to branch road pipe connector mouth passes through hot water mouth and relief valve symmetry setting, shell bottom installation drain and drain one side set up steam inlet, condensate outlet is located drain one side and condensate outlet and steam inlet symmetry setting, divide reactor and reactor one end and the shell intercommunication of dividing are installed to the drain top, shell surface mounting manometer and manometer and shell internal connection, shell bottom erection bracing frame and support frame symmetric distribution in drain both sides, the utility model discloses an adopt the bilateral symmetry structure, the design is simple, installation convenient to use.
Description
Technical field
The utility model relates to a kind of heat exchange equipment, and especially a kind of floating type heat exchange equipment, belongs to thermal machine application.
Background technology
Along with the development of modern science and technology, floating type heat exchanger is widely used in producing, HVAC, sanitary hot water system, belong to the energy-conserving product of national recommendation, complete alternative old-fashioned GB heat exchanger, due to heat exchange coil dither, incrustation scale not easily ingratiates with tube wall, even if there is part incrustation scale, also be easy to come off, and the significant difference of copper and the hot swell-shrink characteristic of incrustation scale can be utilized, thermal shock method is adopted to be removed by incrustation, floating type heat exchanger shell material is carbon steel or stainless steel, heat exchanger tube material is red copper, also can according to the customized special material of designing requirement, the floating type heat exchanger of heat exchange area and working pressure class.
Also there is many weak points in floating type heat exchanger in the market, as heat exchange equipment most on market effectively can not utilize volume, cause many wasting phenomenons, and most equipment heat transfer coefficient is lower, causes thus reaching desirable heat transfer effect, affect real work needs, and the equipment scale that conducts heat in market condensation situation is serious, easily cause peril, therefore, we have proposed a kind of Novel float-type heat exchange equipment for the problems referred to above.
Utility model content
The technical problems to be solved in the utility model is to provide a kind of Novel float-type heat exchange equipment, not only can effectively conduct heat, and can also improve capacity utilization, effectively solves the problem in background technology.
In order to solve the problems of the technologies described above, the utility model provides following technical scheme:
The utility model provides a kind of Novel float-type heat exchange equipment, comprises safety valve, hot water mouth, bypass duct interface, Pressure gauge, point water reactor, bracing frame, condensation-water drain, sewage draining exit, steam inlet, shell; Described cover top portion arranges safety valve and safety valve is embedded in case surface; Described safety valve side arranges hot water mouth, and bypass duct interface is symmetrical arranged by hot water mouth and safety valve; Described outer casing bottom installs sewage draining exit and sewage draining exit side arranges steam inlet; Described condensation-water drain is positioned at sewage draining exit side and condensation-water drain and steam inlet are symmetrical arranged; Point water reactor is installed at described sewage draining exit top and a point water reactor one end is communicated with shell; Described case surface setting pressure table and Pressure gauge are connected with enclosure; Described outer casing bottom installs bracing frame and bracing frame is symmetrically distributed in sewage draining exit both sides.
As a kind of optimal technical scheme of the present utility model, described safety valve is a kind of safety valve of T-shaped structure.
As a kind of optimal technical scheme of the present utility model, described point of water reactor one end is connected with shell and case surface setting pressure table.
As a kind of optimal technical scheme of the present utility model, described condensation-water drain is communicated with bottom steam inlet, and runs through sewage draining exit bottom condensation-water drain and steam inlet.
As a kind of optimal technical scheme of the present utility model, described sewage draining exit is a kind of sewage draining exit of toroidal helical formula structure.
The beneficial effect that compared with prior art the utility model reaches is:
1, the utility model heat transfer coefficient is high, and output is steady, and applicability is strong.
2, the utility model can effectively solve incrustation scale phenomenon, and utilizes the principle energy detergency automatically of expanding with heat and contract with cold, and ensure that high heat conductive efficiency.
3, the utility model adopts new material, can reduce equipment cost, can save construction costs.
Accompanying drawing explanation
Accompanying drawing is used to provide further understanding of the present utility model, and forms a part for description, is used from explanation the utility model, does not form restriction of the present utility model with embodiment one of the present utility model.
In the accompanying drawings:
Fig. 1 is a kind of Novel float-type heat exchange equipment structural representation described in the utility model embodiment;
Number in the figure: 1, safety valve; 2, hot water mouth; 3, bypass duct interface; 4, Pressure gauge; 5, water reactor is divided; 6, bracing frame; 7, condensation-water drain; 8, sewage draining exit; 9, steam inlet; 10, shell.
Detailed description of the invention
Below in conjunction with accompanying drawing, preferred embodiment of the present utility model is described, should be appreciated that preferred embodiment described herein is only for instruction and explanation of the utility model, and be not used in restriction the utility model.
Embodiment: as shown in Figure 1, the utility model provides a kind of Novel float-type heat exchange equipment, comprises safety valve 1, hot water mouth 2, bypass duct interface 3, Pressure gauge 4, point water reactor 5, bracing frame 6, condensation-water drain 7, sewage draining exit 8, steam inlet 9, shell 10; Described shell 10 top arranges safety valve 1 and safety valve 1 is embedded in shell 10 surface; Described safety valve 1 side arranges hot water mouth 2, and bypass duct interface 3 is symmetrical arranged with safety valve 1 by hot water mouth 2; Bottom described shell 10, sewage draining exit 8 is installed and sewage draining exit 8 side arranges steam inlet 9; Described condensation-water drain 7 is positioned at sewage draining exit 8 side and condensation-water drain 7 and steam inlet 9 are symmetrical arranged; Point water reactor 5 is installed at described sewage draining exit 8 top and point water reactor 5 one end is communicated with shell 10; The surperficial setting pressure table 4 of described shell 10 and Pressure gauge 4 are connected with shell 10 inside; Bottom described shell 10, bracing frame 6 is installed and bracing frame 6 is symmetrically distributed in sewage draining exit 8 both sides.
In order to make heat-transfer effect better, reduce incrustation scale impact, described safety valve 1 is a kind of safety valve 1 of T-shaped structure; Described point of water reactor 5 one end is connected with shell 10 and the surperficial setting pressure table 4 of shell 10; Described condensation-water drain 7 is communicated with bottom steam inlet 9, and runs through sewage draining exit 8 bottom condensation-water drain 7 and steam inlet 9; State the sewage draining exit 8 that sewage draining exit 8 is a kind of toroidal helical formula structure.
The utility model it be made up of shell and heat conduction equipment, during equipment work, coil pipe is immersed in shell side water completely, coil pipe generally adopts the pipe of good springiness, so when equipment runs, coil pipe can float back and forth, produce micro-frequency vibration, make the water capacity of shell side easily reach turbulent flow, carry out heat exchange with heating agent in tube bank, improve heat exchange efficiency.Also be owing to vibrating when it works, so it has automatically descaling function.
Last it is noted that the foregoing is only preferred embodiment of the present utility model, be not limited to the utility model, although be described in detail the utility model with reference to previous embodiment, for a person skilled in the art, it still can be modified to the technical scheme described in foregoing embodiments, or carries out equivalent replacement to wherein portion of techniques feature.All within spirit of the present utility model and principle, any amendment done, equivalent replacement, improvement etc., all should be included within protection domain of the present utility model.
Claims (5)
1. a Novel float-type heat exchange equipment, is characterized in that: comprise safety valve (1), hot water mouth (2), bypass duct interface (3), Pressure gauge (4), point water reactor (5), bracing frame (6), condensation-water drain (7), sewage draining exit (8), steam inlet (9), shell (10); Described shell (10) top arranges safety valve (1) and safety valve (1) is embedded in shell (10) surface; Described safety valve (1) side arranges hot water mouth (2), and bypass duct interface (3) is symmetrical arranged with safety valve (1) by hot water mouth (2); Described shell (10) bottom installs sewage draining exit (8) and sewage draining exit (8) side arranges steam inlet (9); Described condensation-water drain (7) is positioned at sewage draining exit (8) side and condensation-water drain (7) and steam inlet (9) are symmetrical arranged; Point water reactor (5) is installed at described sewage draining exit (8) top and point water reactor (5) one end is communicated with shell (10); The surperficial setting pressure table (4) of described shell (10) and Pressure gauge (4) are connected with shell (10) inside; Described shell (10) bottom installs bracing frame (6) and bracing frame (6) is symmetrically distributed in sewage draining exit (8) both sides.
2. a kind of Novel float-type heat exchange equipment according to claim 1, is characterized in that: the safety valve (1) that described safety valve (1) is a kind of T-shaped structure.
3. a kind of Novel float-type heat exchange equipment according to claim 1, is characterized in that: described point of water reactor (5) one end is connected with shell (10) and the surperficial setting pressure table (4) of shell (10).
4. a kind of Novel float-type heat exchange equipment according to claim 1, is characterized in that: described condensation-water drain (7) is communicated with steam inlet (9) bottom, and condensation-water drain (7) runs through sewage draining exit (8) with steam inlet (9) bottom.
5. a kind of Novel float-type heat exchange equipment according to claim 1, is characterized in that: described sewage draining exit (8) is a kind of sewage draining exit (8) of toroidal helical formula structure.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201520784132.8U CN205156693U (en) | 2015-10-12 | 2015-10-12 | Novel floating heat recuperator equipment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201520784132.8U CN205156693U (en) | 2015-10-12 | 2015-10-12 | Novel floating heat recuperator equipment |
Publications (1)
Publication Number | Publication Date |
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CN205156693U true CN205156693U (en) | 2016-04-13 |
Family
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Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN201520784132.8U Expired - Fee Related CN205156693U (en) | 2015-10-12 | 2015-10-12 | Novel floating heat recuperator equipment |
Country Status (1)
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CN (1) | CN205156693U (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105202947A (en) * | 2015-10-12 | 2015-12-30 | 无锡市惠山合力传热设备厂 | Novel floating heat exchanger equipment |
-
2015
- 2015-10-12 CN CN201520784132.8U patent/CN205156693U/en not_active Expired - Fee Related
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105202947A (en) * | 2015-10-12 | 2015-12-30 | 无锡市惠山合力传热设备厂 | Novel floating heat exchanger equipment |
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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: 20160413 Termination date: 20161012 |
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CF01 | Termination of patent right due to non-payment of annual fee |