CN206724755U - Small micro-channel heat exchanger - Google Patents
Small micro-channel heat exchanger Download PDFInfo
- Publication number
- CN206724755U CN206724755U CN201720196823.5U CN201720196823U CN206724755U CN 206724755 U CN206724755 U CN 206724755U CN 201720196823 U CN201720196823 U CN 201720196823U CN 206724755 U CN206724755 U CN 206724755U
- Authority
- CN
- China
- Prior art keywords
- heat
- collector
- tube bundle
- heat exchanger
- exchanging tube
- 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.)
- Active
Links
- 230000035939 shock Effects 0.000 claims abstract description 12
- 230000000452 restraining effect Effects 0.000 claims abstract description 3
- 238000003466 welding Methods 0.000 claims description 4
- 239000002184 metal Substances 0.000 claims description 3
- 230000008859 change Effects 0.000 claims description 2
- 239000007769 metal material Substances 0.000 claims description 2
- 238000000034 method Methods 0.000 abstract description 15
- 238000004134 energy conservation Methods 0.000 abstract description 2
- 238000005265 energy consumption Methods 0.000 abstract description 2
- 208000020442 loss of weight Diseases 0.000 abstract description 2
- 230000002195 synergetic effect Effects 0.000 abstract 1
- 230000008569 process Effects 0.000 description 11
- 239000012530 fluid Substances 0.000 description 4
- 230000000694 effects Effects 0.000 description 3
- 238000010586 diagram Methods 0.000 description 2
- 230000009977 dual effect Effects 0.000 description 2
- 230000008676 import Effects 0.000 description 2
- 210000001367 artery Anatomy 0.000 description 1
- 230000008878 coupling Effects 0.000 description 1
- 238000010168 coupling process Methods 0.000 description 1
- 238000005859 coupling reaction Methods 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000002708 enhancing effect Effects 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 238000003780 insertion Methods 0.000 description 1
- 230000037431 insertion Effects 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 229910052755 nonmetal Inorganic materials 0.000 description 1
- 230000010349 pulsation Effects 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 210000003462 vein Anatomy 0.000 description 1
Landscapes
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
A kind of small micro-channel heat exchanger and heat-exchange method are the utility model is related to, belongs to the energy-conservation loss of weight Synergistic technique field of heat exchanger.The small micro-channel heat exchanger, it is characterised in that：Collector（2）Interior setting horizontal baffle（10）, the horizontal baffle is by collector（2、4）It is divided into two chambers up and down, wherein close to heat-exchanging tube bundle（3）For balance shock chamber（11）, away from heat-exchanging tube bundle（3）To flow chamber（9）；Horizontal baffle（10）It is provided with tube bank mounting hole（4）, heat-exchanging tube bundle（3）Through collector（2）Wall and balance shock chamber（11）Afterwards with horizontal baffle（10）In tube bank mounting hole（4）Place is connected, and by restraining mounting hole（4）With flowing chamber（9）UNICOM；Horizontal baffle（10）Being additionally provided with makes balance shock chamber（11）Flow chamber（9）The balance pipe of UNICOM（12）.The utility model is compact-sized, heat exchange efficiency is high, energy consumption is low.
Description
Technical field
A kind of small micro-channel heat exchanger and heat-exchange method are the utility model is related to, belongs to the energy-conservation loss of weight synergy of heat exchanger
Technical field.
Background technology
At present, the application of heat exchanger is more and more extensive, but the volume of many occasion heat exchangers is larger, and weight is larger, consumption
Material is more, is not easy to install.Using more for shell-and-tube heat exchanger, but the heat exchange efficiency of shell-and-tube heat exchanger is relatively low, into
This is high.
Existing tubular heat exchanger, collector are cylinder, and section is round, and tube bank is laterally inserted directly into, because insertion outer rim is
Circular arc, cause every pipe and the resistance that the intersection of collector is different space curves, welding difficulty, and the import of pipe special
Property it is different, it is difficult to accomplish that shunting is uniform, every tube length is inconsistent in addition, and the overall efficiency of heat exchanging device has a great influence.
Existing improvement tubular heat exchanger, it is semicircular cylinder to cut pipe, and section is D types, restrains the line part in laterally inserted D types section
Point, solve the equal problem of tube length substantially, due to on-circular cross-section, intensity, the rigidity in section are very poor, only increase and cut pipe
Wall thickness, this is particularly disadvantageous to reducing heat exchanger weight, and due to the deformation of stress concentration and its issuable coupling part, pipe
The straight line portion that beam need to cross D types section has certain depth to be welded and fixed, and this has a negative impact to shunting.
The unrestraint ability in addition, existing tubular heat exchanger without balance shock mechanism, is pulsed to caused by dynamic change, and
Pulsation can cause to shunt uneven deterioration heat-transfer effect.
Utility model content
The purpose of this utility model is to provide a kind of small micro-channel heat exchanger compact-sized, heat exchange efficiency is high, energy consumption is low.
A kind of small micro-channel heat exchanger, including heat-exchanging tube bundle, one collector of each UNICOM of upper/lower terminal of heat-exchanging tube bundle, collection
It is circle to manage as horizontal tubular, its longitudinal section；One of collector is provided with header inlet, and another collector is provided with collector and gone out
Mouthful；It is characterized in that：Horizontal baffle is set in collector, and collector is divided into two chambers up and down by the horizontal baffle, wherein close to heat exchange
Tube bank for balance shock chamber, away from heat-exchanging tube bundle to flow chamber；Horizontal baffle is provided with tube bank mounting hole, and heat-exchanging tube bundle is worn
Cross after collector wall and balance shock chamber and be connected with horizontal baffle at tube bank mounting hole, and by restraining mounting hole with flowing
Chamber UNICOM；Horizontal baffle is additionally provided with the balance pipe for making balance shock chamber and Jun Liu chambers UNICOM.
The heat-exchange method of described small micro-channel heat exchanger, it is characterised in that：The heat transfer process passage of intraductal working medium is as follows：
Intraductal working medium enters collector by header inlet, and heat-exchanging tube bundle is flowed into after shunting, after carrying out heat exchange with working medium outside pipe, flows into collection
Pipe, by manifold outlet ports outflow heat exchanger；Balance pipe is for offsetting, arteries and veins caused by buffer fluid flow instabilities or outside exciting
It is dynamic；The heat transfer process passage of the outer working medium of pipe is as follows：Outer horizontal plunder of working medium of pipe washes away heat-exchanging tube bundle, foundation be actually needed as cold side or
Hot side absorbs or released the heat of intraductal working medium, completes diabatic process.
Dividing plate can use the modes such as tube expansion or welding to mechanically connect with tube bank, tube bank and collector, and balance pipe is set on dividing plate
Pulsed for offsetting, caused by buffer fluid flow instabilities or outside exciting.Fluid working substance enters upper header by header inlet
Inside flow chamber, flow to passage aisle tube bank, with tube bank outer fluid heat exchange, into lower collector pipe in flow chamber, flowed out by manifold outlet ports.
For the utility model by using the design of two collectors and its inside, every heat exchanger tube and collector and its dividing plate are dual
Connection, enhance the bonding strength of tube bank, it is important that the every small microchannel of tube bank is isometric and conformity, stream chamber cause
Shunting is uniform, and overall heat exchange effect is significant, and restrains isometric design and make it that the pressure drop of heat transfer process is consistent, further
The uniform process of shunting is enhanced, integrates pipe shell as tubular so that voltage endurance capability increases substantially, and the wall thickness of collector can greatly drop
Low, this volume miniaturization, lightweight to small micro-channel heat exchanger, the cost for reducing heat exchanger plays an important roll.
Described heat-exchanging tube bundle is multipaths.
Described heat-exchanging tube bundle is metal or non-metallic material.
Described heat-exchanging tube bundle is that multilayer fork is arranged or the diameter of in-line arrangement forms less than 3mm passage aisles pipe.
Brief description of the drawings
Fig. 1, small micro-channel heat exchanger overlook schematic diagram；
Fig. 2, small micro-channel heat exchanger left view schematic diagram；
Fig. 3, small micro-channel heat exchanger collector partial schematic；
Wherein, 1, header inlet；2nd, collector；3rd, heat-exchanging tube bundle；4th, mounting hole is restrained；5th, manifold outlet ports；6th, intraductal working medium
7th, outer working medium is managed；8th, pipe shell is collected；9th, chamber is flowed；10th, horizontal baffle；11st, balance shock chamber；12nd, balance pipe.
Embodiment
Such as Fig. 1, as shown in Figure 2 and Figure 3, the heat transfer process passage of intraductal working medium 6 is as follows：Intraductal working medium 6 is by header inlet 1
Into upper header, heat-exchanging tube bundle 4 is flowed into after shunting, after carrying out heat exchange with working medium outside pipe 7, lower collector pipe is flowed into, by manifold outlet ports 5
Outflow heat exchanger；The heat transfer process passage of the outer working medium 7 of pipe is as follows：Outer horizontal plunder of working medium 7 of pipe washes away heat-exchanging tube bundle 3, is needed according to actual
Will as it is cold while or it is hot while absorb or release the heats of 7 intraductal working mediums 6, complete diabatic process.
The architectural feature and efficiency that the heat transfer process of intraductal working medium 6 needs are ensured by the design of collector：Collector is by section
Metal or non-metal shell, the built-in horizontal baffle 10 of pipe form, wherein upper and lower collector is made provided with collector import and export 1,5
To be imported and exported for intraductal working medium, heat-exchanging tube bundle is connected by way of welding or tube expansion between the two through pipe shell 8 is collected,
Collector is divided into by horizontal baffle 10 flows chamber 9 and balance shock chamber 11, is realized by the balance pipe 12 on horizontal baffle between two chambers
Pressure balance, the end plate as heat-exchanging tube bundle 3 simultaneously of horizontal baffle 10, be fixedly connected with heat-exchanging tube bundle 3.
By using the design of two collectors and its inside, every heat exchanger tube and collector and its dual connection of dividing plate, enhancing
The bonding strength of tube bank, it is important that the every small microchannel of tube bank is isometric and conformity, flows chamber and make it that shunting is uniform,
Overall heat exchange effect is significant, isometric design is restrained and make it that the pressure drop of heat transfer process is consistent, further enhance point
Uniform process is flowed, collection pipe shell is circle so that voltage endurance capability is increased substantially, and the wall thickness of collector can be reduced greatly, and this is right
Volume miniaturization, the lightweight of small micro-channel heat exchanger, the cost for reducing heat exchanger play an important roll
In a word, a variety of requirements after the intensive heat exchanger small macro of small micro-channel heat exchanger, enhance unit area（Unit
Volume, weight）Exchange capability of heat, in the case of identical heat exchange amount, heat exchange area（Volume, weight）It can reduce, so as to drop
The cost of low heat exchanger.The raising of heat exchange efficiency, make the heat exchange of therrmodynamic system more abundant, reach so as to reduce the power consumption of system
The purpose of energy-saving and emission-reduction.
Claims (5)
1. a kind of small micro-channel heat exchanger, including heat-exchanging tube bundle（3）, heat-exchanging tube bundle（3）One collector of each UNICOM of upper/lower terminal
（2）, collector（2）For horizontal tubular, its longitudinal section is circle；One of collector is provided with header inlet（1）, another collector
It is provided with manifold outlet ports（5）；
It is characterized in that：
Collector（2）Interior setting horizontal baffle（10）, the horizontal baffle is by collector（2、4）It is divided into two chambers up and down, wherein close change
Heat pipe bundle（3）For balance shock chamber（11）, away from heat-exchanging tube bundle（3）To flow chamber（9）；
Horizontal baffle（10）It is provided with tube bank mounting hole（4）, heat-exchanging tube bundle（3）Through collector（2）Wall and balance shock chamber
（11）Afterwards with horizontal baffle（10）In tube bank mounting hole（4）Place is connected, and by restraining mounting hole（4）With flowing chamber（9）UNICOM；
Horizontal baffle（10）Being additionally provided with makes balance shock chamber（11）Flow chamber（9）The balance pipe of UNICOM（12）.
2. small micro-channel heat exchanger according to claim 1, it is characterised in that：Above-mentioned horizontal baffle（10）With heat-exchanging tube bundle
（3）, heat-exchanging tube bundle（3）With collector（2）Connected using tube expansion or welding manner.
3. small micro-channel heat exchanger according to claim 1, it is characterised in that：Described heat-exchanging tube bundle（3）For multipaths.
4. small micro-channel heat exchanger according to claim 1, it is characterised in that：Described heat-exchanging tube bundle（3）For metal or
Non-metallic material.
5. small micro-channel heat exchanger according to claim 1, it is characterised in that：Described heat-exchanging tube bundle（3）Pitched for multilayer
The diameter of row or in-line arrangement forms less than 3mm passage aisles pipe.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720196823.5U CN206724755U (en) | 2017-03-02 | 2017-03-02 | Small micro-channel heat exchanger |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720196823.5U CN206724755U (en) | 2017-03-02 | 2017-03-02 | Small micro-channel heat exchanger |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206724755U true CN206724755U (en) | 2017-12-08 |
Family
ID=60500896
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720196823.5U Active CN206724755U (en) | 2017-03-02 | 2017-03-02 | Small micro-channel heat exchanger |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206724755U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106949754A (en) * | 2017-03-02 | 2017-07-14 | 南京航空航天大学 | Small micro-channel heat exchanger and heat-exchange method |
-
2017
- 2017-03-02 CN CN201720196823.5U patent/CN206724755U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106949754A (en) * | 2017-03-02 | 2017-07-14 | 南京航空航天大学 | Small micro-channel heat exchanger and heat-exchange method |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN101672553B (en) | Parallel stream heat exchanger integrated with microchannel and outer fin | |
| CN101846467B (en) | Shell-tube heat exchanger | |
| CN201145504Y (en) | Heat exchange tube with special cross-section | |
| CN201476625U (en) | Micro-channel condenser | |
| CN106949754A (en) | Small micro-channel heat exchanger and heat-exchange method | |
| CN102374799A (en) | Shell and tube heat exchanger | |
| CN204165288U (en) | A kind of automotive air-conditioning condenser | |
| CN101871738A (en) | Thermal-load adjustable high-efficiency heat exchanger | |
| CN102788523A (en) | Multi-cold water pipe and multichannel heat absorption open-type communicating heat exchanger and manufacturing process thereof | |
| CN206724755U (en) | Small micro-channel heat exchanger | |
| CN211084569U (en) | Cooling device of biomass boiler | |
| CN205718555U (en) | A kind of micro-channel heat exchanger | |
| CN101696862B (en) | Full welded plate bundle with reinforced structures | |
| CN203249530U (en) | Microchannel flat tube and heat exchanger with same | |
| CN202216452U (en) | Microchannel heat exchanger with serpentine heat exchange tube | |
| CN201867091U (en) | Rectangular all-welded tube and shell type heater for heating network | |
| CN204665982U (en) | A kind of water-cooled shell oil cooler | |
| CN106382831A (en) | Water cooled type parallel flow heat exchanger | |
| CN202254521U (en) | Microchannel condenser for heat pump water heater | |
| CN203837334U (en) | Parallel flow heat exchanger of double-row flat pipes | |
| CN201748826U (en) | Shell and tube heat exchanger | |
| CN201497419U (en) | EGR cooler and spiral deflector thereof | |
| CN106440528A (en) | Parallel flow micro-channel heat exchanger | |
| CN206160774U (en) | Two shell side winding heats exchange of heat pipe of high -efficient shell -and -tube | |
| CN205718634U (en) | A kind of micro-channel heat exchanger of single header |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |