CN201397065Y - Tubular heat exchanger - Google Patents
Tubular heat exchanger Download PDFInfo
- Publication number
- CN201397065Y CN201397065Y CN2009200179853U CN200920017985U CN201397065Y CN 201397065 Y CN201397065 Y CN 201397065Y CN 2009200179853 U CN2009200179853 U CN 2009200179853U CN 200920017985 U CN200920017985 U CN 200920017985U CN 201397065 Y CN201397065 Y CN 201397065Y
- Authority
- CN
- China
- Prior art keywords
- heat exchanger
- medium
- pipeline
- utility
- water
- 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
- 238000009413 insulation Methods 0.000 claims description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 6
- 238000005516 engineering process Methods 0.000 abstract description 4
- 238000010438 heat treatment Methods 0.000 abstract description 3
- 238000004519 manufacturing process Methods 0.000 abstract description 3
- 238000001816 cooling Methods 0.000 abstract 2
- 238000004378 air conditioning Methods 0.000 abstract 1
- 238000007710 freezing Methods 0.000 abstract 1
- 230000008014 freezing Effects 0.000 abstract 1
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 abstract 1
- 230000008676 import Effects 0.000 description 4
- 230000000694 effects Effects 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
- 230000003628 erosive effect Effects 0.000 description 1
- 239000012774 insulation material Substances 0.000 description 1
- 238000005057 refrigeration Methods 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
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- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
The utility mode relates to a tubular heat exchanger, belonging to the cooling and heating technical field. The plate-type (or bushing-type) heat exchanger of the prior art has the problems of no dirtresistance, no incrustant resistance, no freezing resistance, large flow resistance, complex technology, high price and the like. The heat exchanger is formed by combining a medium channel formed bya curved pipeline with another medium channel which is sleeved outside the curved pipeline and is formed by a thick straight pipeline. When medium flows in each pipeline, the heat energy of a medium can be transferred to another medium to the greatest extent. The utility model has the advantages of high heat exchanging efficiency, energy resource saving, simple manufacture, convenient use, long service life and the like. The utility model serves as a condenser or an evaporator in a cooling air-conditioning device and as an air-water or water-water heat exchanger in a heating system.
Description
Technical field
The utility model provides a kind of pipe heat exchanger, belongs to the refrigerating and heat-supplying technical field.
Background technology
Now heat exchanger commonly used has shell-tube type, bushing type and board-like etc. several in refrigeration plant and the heating system, and wherein, plate type heat exchanger is to be produced by external imported technology the nineties in last century, and the compact conformation volume is little, and the heat exchange efficiency height is used more.But because its inside is made up of many stainless steel plates that are pressed into the herringbone ripple, between sheet and the sheet gap less (have only several millimeters), therefore exist in use and be afraid of that dirty, water funk dirt, fearness are frozen, flow resistance is big, need the more high-power and high-lift problems such as water pump of configuration, and the manufacturing process complexity, the price height.
Summary of the invention
The purpose of this utility model is exactly to design in order to address the above problem to provide a kind of volume little, the heat exchange efficiency height, and manufacturing process is simple, and flow resistance is little, long service life, the heat exchanger of convenient and energy-saving.
Embodiment
The purpose of this utility model is achieved in that
This heat exchanger is to be formed by inside and outside two media passage fit.A kind of medium channel is made up of the curved pipeline of multichannel, and an end has import, and the other end has outlet; Be with than the extra heavy pipe road in each curved pipeline outside, two ends are set up import and export separately and are formed another medium channel.Comprise another medium channel and the inside and outside passage that forms by an above medium channel, created condition for two media fully carries out heat exchange.Medium is flowed into, is exported and flow out by import separately, constantly circulation, and the heat energy of certain medium farthest passes to another medium simultaneously, thus the exchange of realization heat energy.
Advantage of the present utility model:
(1) technology simple, easily manufactured, looser runner is arranged, solved dirty, the water funk dirt of fearness, problems such as fearness is frozen, flow resistance is big, price height that plate type heat exchanger exists.
(2) the two media passage is made up of the some branch roads that are linked in together, provides sufficient condition for two media carries out heat exchange, particularly produces turbulent flow during through curved pipeline when MEDIA FLOW, so the heat exchanger effectiveness height.
(3) because flow resistance is little, configurable lower-powered water pump, the supporting water pump that the utility model uses only is 1/5～1/6 of a plate type heat exchanger, the Energy Efficiency Ratio height, energy-saving effect is obvious.
Description of drawings
Accompanying drawing 1 is a cross-sectional schematic of the present utility model.
Describe concrete structure of the present utility model in detail below in conjunction with accompanying drawing
The utility model pipe heat exchanger is formed by heat-insulation layer (7) and inside and outside two media passage (medium 1, medium 2) fit.
Medium 1 passage (interior): make the curved pipeline of multichannel (3) with the higher tubing of thermal conductivity factor, be connected in parallel, an end is inlet pipe (1), and the other end is pipe (2), (way of curved pipeline and the diameter of required tubing, length are determined by the size of heat exchange amount).
Medium 2 passages (outward): overlap the thick straight tube road (4) that the tubing of useful not easy rusting erosion is made in the outside of the curved pipeline in every road, an end has inlet pipe (5), and the other end has the pipe of going out (6).
More than formed by medium 2 passages and comprised medium 1 passage outside at interior inside and outside two passes.
In order to make heat exchanger more energy-conservation and be protected, with insulation material two media passage integral body is wrapped up, be isolated from the outside, only stay import and export.
Claims (2)
1, a kind of pipe heat exchanger, comprising that heat-insulation layer (7), the curved pipeline of inlet pipe (1) (3) go out pipe (2), the thick straight tube road (4) of inlet pipe (5) and go out pipe (6) fit forms, and it is characterized in that: by inlet pipe (1) and multichannel or one road curved pipeline (3) with go out to manage (2) and form a kind of medium channel.
2, pipe heat exchanger as claimed in claim 1 is characterized in that: by inlet pipe (5) and be enclosed within the thick straight tube road (4) of curved pipeline (3) outside and go out to manage (6) and form another kind of medium channel.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009200179853U CN201397065Y (en) | 2009-01-16 | 2009-01-16 | Tubular heat exchanger |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009200179853U CN201397065Y (en) | 2009-01-16 | 2009-01-16 | Tubular heat exchanger |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201397065Y true CN201397065Y (en) | 2010-02-03 |
Family
ID=41619583
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2009200179853U Expired - Fee Related CN201397065Y (en) | 2009-01-16 | 2009-01-16 | Tubular heat exchanger |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201397065Y (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104251546A (en) * | 2013-06-26 | 2014-12-31 | 杨楚 | Condensed water evaporation energy-saving air conditioner |
| CN104764254A (en) * | 2015-03-12 | 2015-07-08 | 广东海悟科技有限公司 | a heat exchanger |
| CN109373437A (en) * | 2018-11-27 | 2019-02-22 | 枣庄福源环能机械制造有限公司 | Pipe row and tandem heating heat-exchange hydrophone |
-
2009
- 2009-01-16 CN CN2009200179853U patent/CN201397065Y/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104251546A (en) * | 2013-06-26 | 2014-12-31 | 杨楚 | Condensed water evaporation energy-saving air conditioner |
| CN104764254A (en) * | 2015-03-12 | 2015-07-08 | 广东海悟科技有限公司 | a heat exchanger |
| CN109373437A (en) * | 2018-11-27 | 2019-02-22 | 枣庄福源环能机械制造有限公司 | Pipe row and tandem heating heat-exchange hydrophone |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20100203 Termination date: 20110116 |