CN105202947A - Novel floating heat exchanger equipment - Google Patents
Novel floating heat exchanger equipment Download PDFInfo
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- CN105202947A CN105202947A CN201510653636.0A CN201510653636A CN105202947A CN 105202947 A CN105202947 A CN 105202947A CN 201510653636 A CN201510653636 A CN 201510653636A CN 105202947 A CN105202947 A CN 105202947A
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- shell
- safety valve
- sewage draining
- draining exit
- steam inlet
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Abstract
The invention provides novel floating heat exchanger equipment. The novel floating heat exchanger equipment comprises a safety valve, a hot water opening, a branched pipe connector, a pressure gauge, a water-distribution reactor, supporting frames, a condensate outlet, a sewage discharging opening, a steam inlet and a shell. The safety valve is arranged at the top of the shell and embedded into the surface of the shell. The hot water opening is formed in one side of the safety valve, and the branched pipe connector and the safety valve are symmetrically arranged through the hot water opening. The sewage discharging opening is formed in the bottom of the shell, and the steam inlet is formed in one side of the sewage discharging opening. The condensate outlet is formed in one side of the sewage discharging opening, and the condensate outlet and the steam inlet are symmetrically formed. The water-distribution reactor is installed at the top of the sewage discharging opening, and one end of the water-distribution reactor is communicated with the shell. The pressure gauge is installed on the surface of the shell and connected with the interior of the shell. The supporting frames are installed at the bottom of the shell and symmetrically distributed on the two sides of the sewage discharging opening. The left and right symmetrical structure is adopted, design is simple, and installing and using are convenient.
Description
Technical field
The present invention relates to a kind of heat exchange equipment, 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.
Summary of the invention
The technical problem to be solved in the present invention 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 invention provides following technical scheme:
The invention provides a kind of Novel float-type heat exchange equipment, comprise 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 preferred technical solution of the present invention, described safety valve is a kind of safety valve of T-shaped structure.
As a preferred technical solution of the present invention, described point of water reactor one end is connected with shell and case surface setting pressure table.
As a preferred technical solution of the present invention, 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 preferred technical solution of the present invention, 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 present invention reaches is:
1, heat transfer coefficient of the present invention is high, and output is steady, and applicability is strong.
2, the present invention 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 present invention adopts new material, can reduce equipment cost, can save construction costs.
Accompanying drawing explanation
Accompanying drawing is used to provide a further understanding of the present invention, and forms a part for description, together with embodiments of the present invention for explaining the present invention, is not construed as limiting the invention.
In the accompanying drawings:
Fig. 1 is a kind of Novel float-type heat exchange equipment structural representation described in the embodiment of the present invention;
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, the preferred embodiments of the present invention are described, should be appreciated that preferred embodiment described herein is only for instruction and explanation of the present invention, is not intended to limit the present invention.
Embodiment: as shown in Figure 1, the invention provides a kind of Novel float-type heat exchange equipment, comprise safety valve 1, hot water mouth 2, bypass duct interface 3, Pressure gauge 4, point water reactor 5, bracing frame 6, condensation 7 water out, 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 present invention 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 the preferred embodiments of the present invention, be not limited to the present invention, although with reference to previous embodiment to invention has been detailed description, 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.Within the spirit and principles in the present invention all, any amendment done, equivalent replacement, improvement etc., all should be included within protection scope of the present invention.
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 (7) water out, 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 |
|---|---|---|---|
| CN201510653636.0A CN105202947A (en) | 2015-10-12 | 2015-10-12 | Novel floating heat exchanger equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510653636.0A CN105202947A (en) | 2015-10-12 | 2015-10-12 | Novel floating heat exchanger equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN105202947A true CN105202947A (en) | 2015-12-30 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201510653636.0A Pending CN105202947A (en) | 2015-10-12 | 2015-10-12 | Novel floating heat exchanger equipment |
Country Status (1)
| Country | Link |
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| CN (1) | CN105202947A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111141171A (en) * | 2020-01-17 | 2020-05-12 | 珠海格力电器股份有限公司 | Heat exchange tube self-cleaning method and heat pump water heater |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4197907A (en) * | 1978-04-05 | 1980-04-15 | Exxon Research & Engineering Co. | Floating head support system for shell and tube heat exchanger |
| CN2244711Y (en) * | 1995-03-16 | 1997-01-08 | 张玉森 | Water-water, steam-water heat exchanger |
| CN2370373Y (en) * | 1999-05-28 | 2000-03-22 | 徐顺宽 | Heat exchanger |
| CN202304498U (en) * | 2011-10-18 | 2012-07-04 | 天津国际机械有限公司 | Improved structure of cartridge type floating coiled tube heat exchanger |
| CN205156693U (en) * | 2015-10-12 | 2016-04-13 | 无锡市惠山合力传热设备厂 | Novel floating heat recuperator equipment |
-
2015
- 2015-10-12 CN CN201510653636.0A patent/CN105202947A/en active Pending
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4197907A (en) * | 1978-04-05 | 1980-04-15 | Exxon Research & Engineering Co. | Floating head support system for shell and tube heat exchanger |
| CN2244711Y (en) * | 1995-03-16 | 1997-01-08 | 张玉森 | Water-water, steam-water heat exchanger |
| CN2370373Y (en) * | 1999-05-28 | 2000-03-22 | 徐顺宽 | Heat exchanger |
| CN202304498U (en) * | 2011-10-18 | 2012-07-04 | 天津国际机械有限公司 | Improved structure of cartridge type floating coiled tube heat exchanger |
| CN205156693U (en) * | 2015-10-12 | 2016-04-13 | 无锡市惠山合力传热设备厂 | Novel floating heat recuperator equipment |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111141171A (en) * | 2020-01-17 | 2020-05-12 | 珠海格力电器股份有限公司 | Heat exchange tube self-cleaning method and heat pump water heater |
| CN111141171B (en) * | 2020-01-17 | 2020-12-29 | 珠海格力电器股份有限公司 | Heat exchange tube self-cleaning method and heat pump water heater |
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| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| WD01 | Invention patent application deemed withdrawn after publication | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20151230 |