CN205642111U - Heat exchanger and water heater with same - Google Patents

Heat exchanger and water heater with same Download PDF

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Publication number
CN205642111U
CN205642111U CN201620429355.7U CN201620429355U CN205642111U CN 205642111 U CN205642111 U CN 205642111U CN 201620429355 U CN201620429355 U CN 201620429355U CN 205642111 U CN205642111 U CN 205642111U
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CN
China
Prior art keywords
heat exchanger
heat
passage
water tank
inwall
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
Application number
CN201620429355.7U
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Chinese (zh)
Inventor
梁家林
闫克江
寇颖举
钟文朝
史帆
欧阳光
白国建
宋江涛
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Gree Electric Appliances Inc of Zhuhai
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Gree Electric Appliances Inc of Zhuhai
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Publication date
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Priority to CN201620429355.7U priority Critical patent/CN205642111U/en
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Publication of CN205642111U publication Critical patent/CN205642111U/en
Expired - Fee Related legal-status Critical Current
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Abstract

The utility model relates to a heat exchanger and have water heater of this heat exchanger. A heat exchanger, comprising: a body and at least one channel disposed on the body; the inner wall of the channel is provided with a concave-convex structure, and the heat exchange medium in the channel exchanges heat with the outside through the channel wall. A water heater comprising: the heat exchanger described above; the heat exchanger is attached to the outer wall of the water tank inner container; the heat exchanger exchanges heat with water in the water tank. The technical scheme of the utility model the heat exchange efficiency has been improved.

Description

A kind of heat exchanger and there is the water heater of this heat exchanger
Technical field
This utility model relates to a kind of technical field of heat exchange, particularly relates to a kind of heat exchanger and has this The water heater of heat exchanger.
Background technology
Existing water tank micro-channel heat exchanger is fixed on outside inner water tank by fixed support, flat tube with Inner water tank plane contact.Current micro-channel heat exchanger is to utilize the coolant in microchannel and microchannel Wall carries out heat exchange, more directly or indirectly carries out heat exchange by microchannel wall with the water in water tank.By It is usually square smooth structure in microchannel interior walls, therefore, cold with in microchannel of microchannel interior walls The heat exchange area of matchmaker is limited, and heat exchange efficiency is low.
Utility model content
In view of this, this utility model provides a kind of heat exchanger and has the water heater of this heat exchanger, main The heat exchange area being to increase vias inner walls with coolant of syllabus, improves heat exchange efficiency.
For reaching above-mentioned purpose, this utility model mainly provides following technical scheme:
On the one hand, embodiment of the present utility model provides a kind of heat exchanger, including:
Body and setting at least one passage on the body;
Wherein, the inwall of described passage has concaveconvex structure, and the heat transferring medium of described channel interior passes through Heat exchange is there is in conduit wall with extraneous.
The purpose of this utility model and solve its technical problem techniques below measure also can be used real further Existing.
Preferably, described concaveconvex structure is evenly provided on the inwall of described passage.
Preferably, the cross section of inboard wall of described passage is circular, oval or rectangle.
Preferably, described concaveconvex structure is the female thread structure along described channel-length direction, fin knot Structure, tongue and groove structure or spline structure.
Preferably, described passage is multiple, and multiple described passages are parallel and are arranged in order.
Preferably, multiple described passages are microchannel.
Preferably, multiple described passages are evenly distributed in yi word pattern, and described body is yi word pattern.
Preferably, the material of described body is aluminum or aluminum alloy.
On the other hand, embodiment of the present utility model provides a kind of water heater, including:
Above-mentioned heat exchanger;And
Water tank, described heat exchanger is attached on the outer wall of inner water tank;
Described heat exchanger directly or indirectly carries out heat exchange with the water in described water tank.
The purpose of this utility model and solve its technical problem techniques below measure also can be used real further Existing.
Preferably, Heat Conduction Material it is coated with described inner water tank between the part that described heat exchanger contacts.
Preferably, described Heat Conduction Material is heat-conducting silicone grease.
By technique scheme, a kind of heat exchanger of this utility model and there is the water heater of this heat exchanger At least have the advantage that
The technical solution of the utility model, by arranging concaveconvex structure at the inwall of described passage, increases The surface area of the inwall of described passage, makes the inwall of the heat transferring medium in described passage and described passage Contact area increases, thus accelerates the heat transfer rate of heat transferring medium and vias inner walls, improves heat exchange Efficiency.
Further, since the contact area of the inwall of heat transferring medium and described passage increases, it is possible to effectively divide Solve the pressure that described heat transferring medium is added on the inwall of described passage, enhance the inwall of described passage Resistance to pressure, thus described passage is unlikely to deform.
Preferably, when passage is circular inner wall, described concaveconvex structure could be arranged to female thread structure, Easily make heat transferring medium in the action of turbulent flow that is internally formed of described passage, thus enhance described heat exchange be situated between Heat exchange between the molecule of matter, further increases heat exchange efficiency.
Described above is only the general introduction of technical solutions of the utility model, in order to better understand this reality By novel technological means, and can be practiced according to the content of description, below with this utility model Preferred embodiment and coordinate accompanying drawing describe in detail as after.
Accompanying drawing explanation
Fig. 1 is a kind of form of a kind of heat exchanger channel that an embodiment of the present utility model provides Cross-sectional view;
Fig. 2 is the another kind of form of a kind of heat exchanger channel that an embodiment of the present utility model provides Cross-sectional view;
Fig. 3 is another form of a kind of heat exchanger channel that an embodiment of the present utility model provides Cross-sectional view;
Fig. 4 is the 4th kind of form of a kind of heat exchanger channel that an embodiment of the present utility model provides Cross-sectional view;
Fig. 5 is the section of a kind of form of a kind of heat exchanger that an embodiment of the present utility model provides Structural representation;
Fig. 6 is the knot of a kind of form of a kind of water heater that another embodiment of the present utility model provides Structure schematic diagram (only provides the signal of upper part heat exchanger channel).
Detailed description of the invention
By further illustrating that this utility model is by reaching the technology hands that predetermined utility model purpose is taked Section and effect, below in conjunction with accompanying drawing and preferred embodiment, to the concrete reality according to this utility model application Execute mode, structure, feature and effect thereof, after describing in detail such as.In the following description, different " one Embodiment " or " embodiment " refer to be not necessarily same embodiment.Additionally, in one or more embodiment Special characteristic, structure or feature can be combined by any suitable form.
As shown in Figure 1 to 4, an embodiment of the present utility model proposes a kind of heat exchanger, including:
Body 10 and at least one passage 20 being arranged on described body 10.Wherein, described passage The inwall of 20 has concaveconvex structure 21, and the heat transferring medium within described passage 20 passes through conduit wall with outer There is heat exchange in boundary.Described concaveconvex structure 21 can be the convex shaped in described passage 20 inner wall surface Become, or described concaveconvex structure 21 can be that the groove in described passage 20 inner wall surface is formed, Or described concaveconvex structure 21 can also be groove shape together with projection of described passage 20 inner wall surface Become.Wherein, the inwall that Fig. 1 show from described passage 20 had both included to the projection of channel center also The tongue and groove structure formed including the depression of outer wall.Fig. 2 show from the inwall of described passage 20 to The concaveconvex structure that channel center convexes to form, in Fig. 2, protruding in the inwall that long limit is passage 20 to logical The rectangle at center, road, forms rib structure.Fig. 3 and Fig. 4 show from the inwall of described passage 20 to The concaveconvex structure that outer wall depression is formed, specifically, the channel cross-section of Fig. 3 and Fig. 4 is substantially round in shape, Fig. 3 show the female thread structure along described channel-length direction, and Fig. 4 show spline structure.
The technical solution of the utility model, by arranging concaveconvex structure at the inwall of described passage, increases The surface area of the inwall of described passage, makes heat transferring medium in described passage connect with the inwall of described passage Contacting surface is long-pending to be increased, thus accelerates the heat transfer rate of heat transferring medium and vias inner walls, improves heat exchange effect Rate.Further, since the contact area of the inwall of heat transferring medium and described passage increases, it is possible to effectively divide Solve the pressure that described heat transferring medium is added on the inwall of described passage, enhance the inwall of described passage Resistance to pressure, thus described passage is unlikely to deform.
Preferably, as shown in Figure 1 to 4, described concaveconvex structure 21 is evenly provided on described passage On the inwall of 20 so that the inwall of described passage 20 is everywhere by the pressure from described heat transferring medium to the greatest extent Amount uniformly, and makes heat transfer rate everywhere essentially identical.
Preferably, as shown in Figure 1 to 4, the cross section of inboard wall of described passage 20 can be circular, ellipse Circle or rectangle.Described concaveconvex structure can be arranged at described vias inner walls tongue and groove structure (as Shown in Fig. 1), rib structure (as shown in Figure 2), female thread structure (as shown in Figure 3) or spline Groove structure (as shown in Figure 4) etc..
Wherein, circular cross-section makes the inwall of described passage 20 be more uniformly stressed, the pressure-bearing property of heat exchanger Can be higher.Such as, as it is shown on figure 3, I.S.S can be arranged in the passage 20 of circular cross-section Concaveconvex structure increases heat exchange area.Female thread has arrangement the most uniformly, easily the feature of processing.Logical Cross the inwall at described passage 20 and the concaveconvex structure of described I.S.S is set so that bright finish is logical originally Road inwall forms some, certain spiral angle and the female thread groove of tooth depth, significantly improves and changes Hot device and the contact area of heat transferring medium (such as coolant).Passage 20 inner wall area of I.S.S is maximum 2~3 times of bright finish vias inner walls area can be reached, thus considerably increase heat exchange area, improve Heat exchange efficiency.And owing to female thread structure makes the heat transferring medium in passage 20 in the inside of described passage Easily form action of turbulent flow, improve the heat transfer rate between heat transferring medium inside, so that heat exchange efficiency 20%~30% can be improved, and can save energy 15%.It addition, micropore design female thread in microchannel is Circular inner wall, the load performance making heat exchanger is higher, and the concaveconvex structure 21 of I.S.S makes heat transferring medium Increase with the contact area of the inwall of described passage, it is possible to effectively decompose described heat transferring medium and be added in described Pressure on the inwall of passage, enhances the resistance to pressure of the inwall of described passage, thus described passage is not It is easily generated deformation, makes the load performance with the water heater of this heat exchanger higher simultaneously.
In addition to the concaveconvex structure of above-mentioned I.S.S, when the cross section of described passage is circular, also may be used The concaveconvex structure of spline (as shown in Figure 4) is set with the inside at described passage 20.
Preferably, as it is shown in figure 5, described passage 20 can be multiple, multiple described passages 20 are flat Go and be arranged in order.Such as, described body 10 is in yi word pattern flat tube, and multiple described passages 20 are permissible It is evenly arranged into yi word pattern.Now, the outer surface of described body 10 can be attached to described equipment completely On heat exchange surface, improve heat exchange efficiency.
Preferably, multiple described passages 20 can be microchannel.Microchannel, refers to that passage equivalent is straight Footpath is at the heat exchanger channels of 10-1000 μm.In terms of domestic air conditioning applications, when heat exchanger channels is smaller in size than During 3mm, gas liquid two-phase flow and phase-change heat transfer rule will differ from conventional large-size, heat exchanger channels The least, this dimensional effect is the most obvious.When heat exchanger channels internal diameter little to 0.5~1mm time, heat convection Coefficient can increase 50%~100%.This heat transfer enhancement technology is used for air conditioner and water heater, suitably changes The augmentation of heat transfer measure of water heater structure, technique and air side, can effectively strengthen the biography of air conditioner and water heater Heat, improve its energy-saving horizontal.Compared with conventional hot water's device, the little heat exchange of micro channel heat hydrophone not only volume Coefficient is big, and heat exchange efficiency is high, can meet higher Energy Efficiency Standard, and have excellent pressure performance.
Water tank micro-channel heat exchanger is fixed on outside inner water tank by fixed support, in flat tube and water tank Gallbladder plane contact, the interior microcellular structure of micro-channel heat exchanger makes it have bigger area-volume ratio, with The contact area of coolant is greatly increased, it is possible to effectively decompose pressure, has the strongest resistance to pressure, is more than Also will not be deformed under 4.2MPa pressure.
Owing to the heat conductivility of aluminum or aluminum alloy is good, the material of described body 10 can be aluminum or aluminum conjunction Gold, to further speed up heat transfer rate, improves heat exchange efficiency.Simultaneously as aluminum or aluminum alloy material Density is little, lightweight, therefore has efficient material-saving, light weight environmental protection, the feature such as with low cost.
As shown in Figure 6, another embodiment of the present utility model provides a kind of water heater, including above-mentioned Heat exchanger 1 and inner water tank 2.
Preferably, described heat exchanger 1 is close on the outer wall of described inner water tank 2, indirectly with described Liquid heat exchange in inner water tank 2, as shown in Figure 6.Concrete heat transfer process is, described heat exchanger 1 The first body with described heat exchanger 1 of heat transferring medium in passage carries out heat exchange, the most described heat exchanger 1 Body outer wall with described inner water tank 2 again carry out heat exchange, outside last described inner water tank 2 Wall carries out heat exchange with the water within described inner water tank 2.Heat exchanger 1 can by fixed support or Alternate manner (such as screw fastening etc.) be fixed on as described in the outside of inner water tank 2, the basis of heat exchanger 1 Surface is plane contact with the outer surface of inner water tank.
Wherein, heat exchanger, including:
Body and setting at least one passage on the body;
Wherein, the inwall of described passage has concaveconvex structure, and the heat transferring medium of described channel interior passes through Heat exchange is there is in conduit wall with extraneous.
The detailed description of the invention of described heat exchanger refers to the detailed description of the invention in previous embodiment, here Do not repeat.
Preferably, can be coated with between the part that described heat exchanger 1 contacts with described inner water tank 2 and lead Hot material, can eliminate the air gap between the part that heat exchanger 1 contacts with described inner water tank 2, Increase type of thermal communication, reduce thermal resistance, accelerate heat transfer rate, improve heat exchange efficiency.
Preferably, described Heat Conduction Material can be heat-conducting silicone grease.Heat-conducting silicone grease have good heat conduction, Heatproof, insulating properties, and stable performance, in use will not produce etchant gas, will not be to institute The metal of contact produces impact.
Specifically, water tank outer disk microchannel condensing heat-exchange includes the condensation heat transfer of medium side, flat tube wall Heat conduction, silicone grease heat conduction, inner bag heat conduction and the heat transfer free convection of water side water.In the micropore of microchannel The concaveconvex structure design of wall makes the condensation heat transfer efficiency of medium side be greatly improved, thus promotes flat tube wall The heat exchange efficiency of the heat transfer free convection of face heat conduction, silicone grease heat conduction, inner bag heat conduction and water side water is significantly Improving, the overall structure of micro-channel heat exchanger can be made more compact efficient, improves whole unit Performance.On the premise of same performance, micro-channel heat exchanger structure can be optimized, cost-effective.
The technical solution of the utility model, by arranging concaveconvex structure at the inwall of described passage, increases The surface area of the inwall of described passage, makes heat transferring medium in described passage connect with the inwall of described passage Contacting surface is long-pending to be increased, thus accelerates the heat transfer rate of heat transferring medium and vias inner walls, improves heat exchange effect Rate.Further, since the contact area of the inwall of heat transferring medium and described passage increases, it is possible to effectively divide Solve the pressure that described heat transferring medium is added on the inwall of described passage, enhance the inwall of described passage Resistance to pressure, thus described passage is unlikely to deform.
When passage has circular inner wall, employing arranges female thread structure can make heat transferring medium described Passage be internally formed action of turbulent flow, thus enhance the heat exchange between the molecule of described heat transferring medium, Further increase heat exchange efficiency.
In sum, skilled addressee readily understands that, on the premise of not conflicting, above-mentioned Each advantageous manner can freely combine, superposition.
The above, be only preferred embodiment of the present utility model, not makees this utility model Any pro forma restriction, according to technical spirit of the present utility model above example is made any Simple modification, equivalent variations and modification, all still fall within the range of technical solutions of the utility model.

Claims (11)

1. a heat exchanger, it is characterised in that including: body and setting at least one passage on the body;Wherein, the inwall of described passage has concaveconvex structure, and the heat transferring medium of described channel interior occurs heat exchange by conduit wall with extraneous.
Heat exchanger the most according to claim 1, it is characterised in that described concaveconvex structure is evenly provided on the inwall of described passage.
Heat exchanger the most according to claim 1, it is characterised in that the cross section of inboard wall of described passage is circular, oval or rectangle.
Heat exchanger the most according to claim 1, it is characterised in that described concaveconvex structure is the female thread structure along described channel-length direction, rib structure, tongue and groove structure or spline structure.
5., according to the heat exchanger described in any one in Claims 1 to 4, it is characterised in that described passage is multiple, multiple described passages are parallel and are arranged in order.
Heat exchanger the most according to claim 5, it is characterised in that multiple described passages are microchannel.
Heat exchanger the most according to claim 5, it is characterised in that multiple described passages are evenly distributed in yi word pattern, and described body is yi word pattern.
Heat exchanger the most according to claim 1, it is characterised in that the material of described body is aluminum or aluminum alloy.
9. a water heater, it is characterised in that including: the heat exchanger described in any one in the claims 1~8;And water tank, described heat exchanger is attached on the outer wall of inner water tank;Described heat exchanger carries out heat exchange with the water in described water tank.
Water heater the most according to claim 9, it is characterised in that be coated with Heat Conduction Material with described inner water tank between the part that described heat exchanger contacts.
11. water heaters according to claim 10, it is characterised in that described Heat Conduction Material is heat-conducting silicone grease.
CN201620429355.7U 2016-05-11 2016-05-11 Heat exchanger and water heater with same Expired - Fee Related CN205642111U (en)

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Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105841541A (en) * 2016-05-11 2016-08-10 珠海格力电器股份有限公司 Heat exchanger and water heater with same
CN108309769A (en) * 2018-01-31 2018-07-24 路景顺 Sky dragon yang-tonifying fiber crops moxibustion venting medicine stick and preparation method thereof
CN109797093A (en) * 2019-03-11 2019-05-24 中国科学院苏州生物医学工程技术研究所 A kind of consumptive material, device and method for extracting nucleic acid for nucleic acid extraction
CN110657536A (en) * 2019-11-11 2020-01-07 华泉汇投资(广州)有限公司 Heat pipe heat exchange system suitable for computer lab
CN111397425A (en) * 2020-03-16 2020-07-10 南京理工大学 Composite heat exchange device with distributed grooves, convex spherical surfaces and fins

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105841541A (en) * 2016-05-11 2016-08-10 珠海格力电器股份有限公司 Heat exchanger and water heater with same
CN108309769A (en) * 2018-01-31 2018-07-24 路景顺 Sky dragon yang-tonifying fiber crops moxibustion venting medicine stick and preparation method thereof
CN109797093A (en) * 2019-03-11 2019-05-24 中国科学院苏州生物医学工程技术研究所 A kind of consumptive material, device and method for extracting nucleic acid for nucleic acid extraction
CN109797093B (en) * 2019-03-11 2023-09-29 中国科学院苏州生物医学工程技术研究所 Consumable, device and nucleic acid extraction method for nucleic acid extraction
CN110657536A (en) * 2019-11-11 2020-01-07 华泉汇投资(广州)有限公司 Heat pipe heat exchange system suitable for computer lab
CN111397425A (en) * 2020-03-16 2020-07-10 南京理工大学 Composite heat exchange device with distributed grooves, convex spherical surfaces and fins

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C14 Grant of patent or utility model
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CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20161012

CF01 Termination of patent right due to non-payment of annual fee