CN203100489U - Tank type heat exchanger with synchronous spiral flow deflector - Google Patents
Tank type heat exchanger with synchronous spiral flow deflector Download PDFInfo
- Publication number
- CN203100489U CN203100489U CN 201220684902 CN201220684902U CN203100489U CN 203100489 U CN203100489 U CN 203100489U CN 201220684902 CN201220684902 CN 201220684902 CN 201220684902 U CN201220684902 U CN 201220684902U CN 203100489 U CN203100489 U CN 203100489U
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- CN
- China
- Prior art keywords
- inner barrel
- shell body
- flow deflector
- heat exchanger
- outer shell
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- Expired - Fee Related
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Abstract
The utility model relates to a tank type heat exchanger with a synchronous spiral flow deflector. The tank type heat exchanger with the synchronous spiral flow deflector comprises a closed outer shell and an inner barrel which is arranged in the outer shell, wherein a spiral flow deflector is connected between the outer shell and the inner barrel, the inner wall of the outer shell, the outer wall of the inner barrel and the spiral flow deflector are connected to form a spiral cavity, a water pipe is further coiled on the periphery of the inner barrel, and is arranged along the coiling direction of the spiral cavity, a water outlet end of the water pipe passes through the upper portion of the outer shell, a water inlet end of the water pipe passes through the lower portion of the outer shell, a refrigerating fluid inlet pipe and a refrigerating fluid outlet pipe are arranged on the outer portion of the outer shell, the refrigerating fluid inlet pipe is communicated with the spiral cavity which is arranged on the upper portion of the outer shell, and the refrigerating fluid outlet pipe is communicated with the spiral cavity which is arranged on the bottom portion of the outer shell. The spiral flow deflector which is synchronous with the water pipe which is coiled along the inner barrel is arranged in the space of the outer shell, an original circular cylinder is divided into the spiral cavity, the route of refrigerating fluid in the outer shell is prolonged, and the heat exchange effect is enhanced.
Description
Technical field
The utility model relates to the pot type heat exchanger.
Background technology
The pot type heat exchanger that is used for Teat pump boiler and air-conditioner in the market is made up of housing, inner barrel and helical form coil pipe.The work schedule cryogen flows in tank inner chamber, flows in the water to be heated helical form coil pipe in jar.Because it is tightr that the helical form coil pipe mostly coils, tube pitch is very little, is unfavorable for the transmission of the heat between cold-producing medium and the helical form coil pipe, has influenced the efficient of complete machine.
The utility model content
The purpose of this utility model is to propose a kind of pot type heat exchanger that has the synchronous screw flow deflector, and it can solve the low problem of heat exchange efficiency.
In order to achieve the above object, the technical scheme that the utility model adopted is as follows:
A kind of pot type heat exchanger that has the synchronous screw flow deflector, the inner barrel that it comprises airtight shell body and is positioned at shell body, be connected with a helical form flow deflector between shell body and the inner barrel, the inwall of shell body, the outer wall of inner barrel and helical form flow deflector have been connected to form a helical form cavity; The peripheral counter offer of described inner barrel is wound with a water pipe, and described water pipe is along the coil direction setting of helical form cavity, and the water side of water pipe is piercing in the top of shell body, and the water inlet end of water pipe is piercing in the bottom of shell body; The outside of shell body is provided with cold-producing medium feed tube, cold-producing medium drain pipe, and the cold-producing medium feed tube is communicated with the helical form cavity on shell body top, and the cold-producing medium drain pipe is communicated with the helical form cavity of shell body bottom.
Preferably, in order to prolong the time of cold-producing medium in shell body, the upper end of inner barrel and the welded top of shell body, the lower end of inner barrel and the bottom of shell body have gap (described gap is as much as possible little), offer first through hole on the sidewall of the lower end of inner barrel, the junction of cold-producing medium drain pipe and shell body is positioned at the projection of lower end on the bottom of shell body of inner barrel.Further preferred, the quantity of first through hole is two, and two first through holes relatively are arranged on the sidewall of inner barrel lower end.Further preferred, be welded with a base plate in the inner barrel, offer one second through hole on the described base plate; Described base plate is positioned at first through hole top.
The shape of above-mentioned shell body can be cylindric.
The shape of above-mentioned inner barrel can be cylindric.
The utlity model has following beneficial effect:
Being provided with in the space of shell body and the synchronous helical form flow deflector of water pipe that coils along inner barrel, is the helical form cavity with original circular cylinder spatial division, has prolonged the stroke of cold-producing medium in shell body, has strengthened the heat exchange effect.
Description of drawings
Fig. 1 is the structural representation of the pot type heat exchanger that has the synchronous screw flow deflector of the utility model preferred embodiment;
Fig. 2 is the internal structure schematic diagram of the pot type heat exchanger that has the synchronous screw flow deflector of the utility model preferred embodiment.
Reference numeral: 1, shell body; 2, inner barrel; 3, helical form flow deflector; 4, helical form cavity; 5, water pipe; 21, the first through hole a; 22, the first through hole b; 23, base plate; 24, second through hole; 51, water side; 52, water inlet end; 61, cold-producing medium feed tube; 62, cold-producing medium drain pipe.
The specific embodiment
Below, in conjunction with the accompanying drawings and the specific embodiment, the utility model is described further:
As depicted in figs. 1 and 2, a kind of pot type heat exchanger that has the synchronous screw flow deflector, the inner barrel 2 that it comprises airtight shell body 1 and is positioned at shell body 1.
Be connected with a helical form flow deflector 3 between shell body 1 and the inner barrel 2, the outer wall of the inwall of shell body 1, inner barrel 2 and helical form flow deflector 3 have been connected to form a helical form cavity 4.
The peripheral counter offer of described inner barrel 2 is wound with a water pipe 5, and described water pipe 5 is along the coil direction setting of helical form cavity 4, and the water side 51 of water pipe 5 is piercing in the top of shell body 1, and the water inlet end 52 of water pipe 5 is piercing in the bottom of shell body 1.
The outside of shell body 1 is provided with cold-producing medium feed tube 61, cold-producing medium drain pipe 62, and cold-producing medium feed tube 61 is communicated with the helical form cavity 4 on shell body 1 top, and cold-producing medium drain pipe 62 is communicated with the helical form cavity 4 of shell body 1 bottom.
The welded top of the upper end of inner barrel 2 and shell body 1, the bottom of the lower end of inner barrel 2 and shell body 1 has gap (described gap is as much as possible little), offer first through hole on the sidewall of the lower end of inner barrel 2, the quantity of first through hole is two, be respectively the first through hole a21, the first through hole b22, two first through holes relatively are arranged on the sidewall of inner barrel 2 lower ends.The junction of cold-producing medium drain pipe 62 and shell body 1 is positioned at the projection of lower end on the bottom of shell body 1 of inner barrel 2, that is to say, the cold-producing medium of bottom is just discharged by cold-producing medium drain pipe 62 after entering in the inner barrel 2 by first through hole.Be welded with a base plate 23 in the inner barrel 2, offer one second through hole 24 on the described base plate 23; Described base plate 23 is positioned at first through hole top.
The shell body 1 of present embodiment, the shape of inner barrel 2 all can be cylindric.
During work, water enters from water inlet end 52, and water flows from descending, 51 outflows from the water side at last; Cold-producing medium enters from cold-producing medium feed tube 61, flows downward along helical form cavity 4, and the cold-producing medium drain pipe 62 from the bottom flows out at last.
Owing to set up helical form flow deflector 3, cold-producing medium is limited in the helical form cavity 4 flows, prolonged the stroke of cold-producing medium in heat exchanger, strengthened the heat exchange between cold-producing medium and the water pipe 5.
For a person skilled in the art, can make other various corresponding changes and distortion, and these all changes and distortion should belong within the protection domain of the utility model claim all according to technical scheme described above and design.
Claims (6)
1. pot type heat exchanger that has the synchronous screw flow deflector, comprise airtight shell body and the inner barrel that is positioned at shell body, it is characterized in that, be connected with a helical form flow deflector between shell body and the inner barrel, the inwall of shell body, the outer wall of inner barrel and helical form flow deflector have been connected to form a helical form cavity; The peripheral counter offer of described inner barrel is wound with a water pipe, and described water pipe is along the coil direction setting of helical form cavity, and the water side of water pipe is piercing in the top of shell body, and the water inlet end of water pipe is piercing in the bottom of shell body; The outside of shell body is provided with cold-producing medium feed tube, cold-producing medium drain pipe, and the cold-producing medium feed tube is communicated with the helical form cavity on shell body top, and the cold-producing medium drain pipe is communicated with the helical form cavity of shell body bottom.
2. the pot type heat exchanger that has the synchronous screw flow deflector as claimed in claim 1, it is characterized in that, the upper end of inner barrel and the welded top of shell body, the lower end of inner barrel and the bottom of shell body have the gap, offer first through hole on the sidewall of the lower end of inner barrel, the junction of cold-producing medium drain pipe and shell body is positioned at the projection of lower end on the bottom of shell body of inner barrel.
3. the pot type heat exchanger that has the synchronous screw flow deflector as claimed in claim 2 is characterized in that the quantity of first through hole is two, and two first through holes relatively are arranged on the sidewall of inner barrel lower end.
4. the pot type heat exchanger that has the synchronous screw flow deflector as claimed in claim 2 is characterized in that, is welded with a base plate in the inner barrel, offers one second through hole on the described base plate; Described base plate is positioned at first through hole top.
5. as each described pot type heat exchanger that has the synchronous screw flow deflector of claim 1-4, it is characterized in that being shaped as of described shell body is cylindric.
6. as each described pot type heat exchanger that has the synchronous screw flow deflector of claim 1-4, it is characterized in that being shaped as of described inner barrel is cylindric.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 201220684902 CN203100489U (en) | 2012-12-12 | 2012-12-12 | Tank type heat exchanger with synchronous spiral flow deflector |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 201220684902 CN203100489U (en) | 2012-12-12 | 2012-12-12 | Tank type heat exchanger with synchronous spiral flow deflector |
Publications (1)
Publication Number | Publication Date |
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CN203100489U true CN203100489U (en) | 2013-07-31 |
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Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN 201220684902 Expired - Fee Related CN203100489U (en) | 2012-12-12 | 2012-12-12 | Tank type heat exchanger with synchronous spiral flow deflector |
Country Status (1)
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CN (1) | CN203100489U (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103994689A (en) * | 2014-05-30 | 2014-08-20 | 威海石岛重工有限公司 | Guiding device of jacketed vessel |
CN106123639A (en) * | 2016-08-08 | 2016-11-16 | 中国海洋石油总公司 | The wrap-round tubular heat exchanger of cylinder dividing plate and AND DEWATERING FOR ORIFICE STRUCTURE is set in a kind of housing |
CN106323046A (en) * | 2016-08-23 | 2017-01-11 | 新奥科技发展有限公司 | Coil pipe heat exchanger |
CN107202453A (en) * | 2017-06-30 | 2017-09-26 | 江苏唯益换热器股份有限公司 | A kind of heat pump high-efficiency tank heat exchanger |
CN109405589A (en) * | 2018-11-30 | 2019-03-01 | 华南理工大学 | A kind of spherical heat exchanger that two-tube-pass independently exchanges heat |
-
2012
- 2012-12-12 CN CN 201220684902 patent/CN203100489U/en not_active Expired - Fee Related
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103994689A (en) * | 2014-05-30 | 2014-08-20 | 威海石岛重工有限公司 | Guiding device of jacketed vessel |
CN106123639A (en) * | 2016-08-08 | 2016-11-16 | 中国海洋石油总公司 | The wrap-round tubular heat exchanger of cylinder dividing plate and AND DEWATERING FOR ORIFICE STRUCTURE is set in a kind of housing |
CN106123639B (en) * | 2016-08-08 | 2018-04-06 | 中国海洋石油总公司 | Cylinder dividing plate and the wrap-round tubular heat exchanger of AND DEWATERING FOR ORIFICE STRUCTURE are set in a kind of housing |
CN106323046A (en) * | 2016-08-23 | 2017-01-11 | 新奥科技发展有限公司 | Coil pipe heat exchanger |
CN107202453A (en) * | 2017-06-30 | 2017-09-26 | 江苏唯益换热器股份有限公司 | A kind of heat pump high-efficiency tank heat exchanger |
CN109405589A (en) * | 2018-11-30 | 2019-03-01 | 华南理工大学 | A kind of spherical heat exchanger that two-tube-pass independently exchanges heat |
CN109405589B (en) * | 2018-11-30 | 2023-10-27 | 华南理工大学 | Spherical heat exchanger with double tube-pass independent heat exchange |
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Legal Events
Date | Code | Title | Description |
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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: 20130731 Termination date: 20151212 |
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EXPY | Termination of patent right or utility model |