CN206724748U - Spiral winding tube type heat exchanger - Google Patents
Spiral winding tube type heat exchanger Download PDFInfo
- Publication number
- CN206724748U CN206724748U CN201720302397.9U CN201720302397U CN206724748U CN 206724748 U CN206724748 U CN 206724748U CN 201720302397 U CN201720302397 U CN 201720302397U CN 206724748 U CN206724748 U CN 206724748U
- Authority
- CN
- China
- Prior art keywords
- heat exchanger
- tube
- layer
- spiral winding
- drain pipe
- 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
Landscapes
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
A kind of this disclosure relates to spiral winding tube type heat exchanger.The spiral winding tube type heat exchanger include positioned at the spiral winding tube type heat exchanger length direction one end feed tube, positioned at the spiral winding tube type heat exchanger length direction the other end drain pipe and be connected between the feed tube and drain pipe five layers of coaxial spiral winding heat exchanger tube, wherein, along the direction of ecto-entad, first layer (A) includes the heat exchanger tube of two articles of wound in parallel to the 4th layer of (D) described heat exchanger tube, and layer 5 (E) described heat exchanger tube includes a heat exchanger tube.The spiral winding tube type heat exchanger that the disclosure provides has new structure and excellent heat exchange property.
Description
Technical field
This disclosure relates to technical field of heat exchangers, in particular it relates to a kind of spiral winding tube type heat exchanger.
Background technology
Heat exchanger can be used as heater, cooler, condenser, evaporator and reboiler etc., in the industrial production using model
Enclose quite varied.
The heat exchange tube design of traditional shell-and-tube heat exchanger is all using straight tube either U-tube.But this shell-and-tube
The heat exchange area of heat exchanger is smaller, and heat exchange efficiency is low.With industrial development, spiral winding tube type heat exchanger have developed.Make
For one kind in heat exchanger, spiral winding tube type heat exchanger can be used in gas-gas, solution-air, liquid-liquid heat exchange.It is different from conventional straight
Pipe type heat transfer pipe, arranged in view of heat-exchanging tube bundle spiral winding in spiral winding tube type heat exchanger, its heat exchange efficiency and heat transfer energy
Power is all higher than conventional straight pipe type heat exchanger tube.
Utility model content
The purpose of the disclosure is to provide a kind of spiral winding tube type heat exchanger, and the spiral winding tube type heat exchanger has new
Structure and excellent heat exchange property.
To achieve these goals, the disclosure provides a kind of spiral winding tube type heat exchanger, wherein, the spiral winding pipe
Formula heat exchanger includes the feed tube of one end of the length direction positioned at the spiral winding tube type heat exchanger, twined positioned at the spiral
The drain pipe of the other end of the length direction of wound tube heat exchanger and be connected between the feed tube and drain pipe five layers
The heat exchanger tube of coaxial spiral winding, wherein, along the direction of ecto-entad, first layer to the 4th layer of heat exchanger tube includes two articles
The heat exchanger tube of wound in parallel, heat exchanger tube described in layer 5 include a heat exchanger tube.
Alternatively, the feed tube includes the first feed liquor extended along the radial direction of the spiral winding tube type heat exchanger
Pipe and the second feed tube, the drain pipe include going out liquid along the first of the radial direction extension of the spiral winding tube type heat exchanger
Manage with the second drain pipe, in each layer in the first layer to the 4th layer, wherein the both ends of a heat exchanger tube connect respectively
In first feed tube and the first drain pipe, the both ends of another heat exchanger tube are connected to second feed tube and second
Drain pipe.
Alternatively, first feed tube and the second feed tube are substantially conllinear, the flowing of liquid in first feed tube
The flow direction of direction and liquid in second feed tube is on the contrary, first drain pipe and second drain pipe are substantially common
Line, in first drain pipe flow direction of liquid with the flow direction of liquid in second drain pipe on the contrary, with wherein
Liquid flow direction on the basis of,
In each layer in the first layer to the 4th layer, the liquid feeding end of two heat exchanger tubes is respectively described first
Feed tube, the same side of second feed tube are connected correspondingly to first feed tube, second feed tube, outlet end
First drain pipe, the second drain pipe are connected correspondingly in the same side of first drain pipe, the second drain pipe.
Alternatively, along the length direction, first feed tube is right against first drain pipe, second feed liquor
Pipe is right against second drain pipe.
Alternatively, the hand of spiral of two layers adjacent of heat exchanger tube is opposite.
Alternatively, in the caliber of heat exchanger tube all in five layers of heat exchanger tube, maximum caliber is 17.6mm~18.4mm,
Minimum pipe is 11.6mm~12.4mm.
Alternatively, the first layer is 30 °~50 ° to the helix angle all same of described 4th layer of heat exchanger tube；It is described
The helix angle of the heat exchanger tube of layer 5 is 30 °~50 °.
Alternatively, the first layer is 1.6mm~2.0mm to the pipe thickness all same of described 4th layer of heat exchanger tube；
The pipe thickness of the heat exchanger tube of the layer 5 is 1.3mm~1.7mm.
Alternatively, in the first layer into the 4th layer of heat exchanger tube, the interlayer between every two layers adjacent of heat exchanger tube
Away from successively decreasing successively, maximum interlamellar spacing is 75mm~55mm, and minimum interlamellar spacing is 55mm~35mm, and described 4th layer is changed with layer 5
Spacing between heat pipe is equal with the spacing between the third layer and the 4th layer.
Alternatively, the spiral winding tube type heat exchanger includes housing, and the heat exchanger tube is located in the housing, it is described enter
Liquid pipe is stretched out from the housing, and the drain pipe stretches out from the housing.
Pass through above-mentioned technical proposal, on the basis of this five layers, the structures of nine pipes, by designing heat exchanger tube and feed tube
A series of parameters for influenceing heat exchanger heat exchange property such as attachment structure, winding direction, helix angle, interlamellar spacing with drain pipe,
There is provided enough flows makes material circulate wherein and fully heat exchange, while the pressure balance maintained the fluid in shell side,
Average heat energy distribution so that heat exchanger has excellent heat exchange property.
Other feature and advantage of the disclosure will be described in detail in subsequent specific embodiment part.
Brief description of the drawings
Accompanying drawing is for providing further understanding of the disclosure, and a part for constitution instruction, with following tool
Body embodiment is used to explain the disclosure together, but does not form the limitation to the disclosure.In the accompanying drawings：
Fig. 1 is a kind of schematic front view of embodiment of the spiral winding tube type heat exchanger provided according to the disclosure；
Fig. 2 is the solid of the heat exchanger tube in a kind of embodiment of the spiral winding tube type heat exchanger provided according to the disclosure
Figure；
Fig. 3 is the top view of the heat exchanger tube shown in Fig. 2；
Fig. 4 is the sectional view along Fig. 3 center line A-A cuttings；
Fig. 5 is a kind of another stereogram of embodiment of the spiral winding tube type heat exchanger provided according to the disclosure, its
In, the first feed tube and the second feed tube is not shown；
Fig. 6 is the first layer heat exchanger tube in a kind of embodiment of the spiral winding tube type heat exchanger provided according to the disclosure
Stereogram；
Fig. 7 is the heat exchanger tube in the another embodiment of the spiral winding tube type heat exchanger provided according to the disclosure
Stereogram；
Fig. 8 is the top view of the heat exchanger tube shown in Fig. 7；
Fig. 9 is the sectional view along Fig. 8 center line A-A cuttings.
Description of reference numerals
10 feed tubes；11 first feed tubes；12 second feed tubes；20 drain pipes；21 first drain pipes；22 second go out liquid
Pipe；3 housings；
A first layers；The B second layers；C third layer；The 4th layer of D；E layer 5s；
A, b, c, d, e heat exchanger tube.
Embodiment
The embodiment of the disclosure is described in detail below in conjunction with accompanying drawing.It should be appreciated that this place is retouched
The embodiment stated is merely to illustrate and explained the disclosure, is not limited to the disclosure.
In the disclosure, in the case where not making opposite explanation, the noun of locality such as " inside and outside " used refers to relative to part
Itself inside and outside.The above-mentioned noun of locality is only used for the explanation and illustration disclosure, is not limited to the scope of the present disclosure.
The utility model is directed to providing a kind of spiral winding pipe type with new structure and excellent heat exchange property
Heat exchanger.By design heat exchanger tube the number of plies, every layer tube bank quantity, heat exchanger tube and feed tube and drain pipe attachment structure,
A series of parameters for influenceing heat exchanger heat exchange property such as winding direction, helix angle, tube pitch, there is provided enough flows make material
Circulation and fully heat exchange wherein, while the pressure balance maintained the fluid in shell side, average heat energy distribution so that heat exchange
Utensil has excellent heat exchange property.Here, it should be noted that used term " feed tube ", " drain pipe " " liquid feeding end ",
The flow morphology in " liquid " limitation respective line in " outlet end " etc., can be liquid, such as glass precursor solution or gas
Body, such as steam.
Fig. 1 to Fig. 6 shows a kind of embodiment of the spiral winding tube type heat exchanger provided according to the disclosure.Wherein,
The feed tube of the one end of the spiral winding tube type heat exchanger including the length direction positioned at the spiral winding tube type heat exchanger,
Positioned at the other end of the length direction of the spiral winding tube type heat exchanger drain pipe and be connected to the feed tube and to go out
Five layers of heat exchanger tube coaxially wound between liquid pipe, wherein, along the direction of ecto-entad, heat exchange described in first layer A to the 4th layers of D
Guan Jun includes the heat exchanger tube of two wound in parallel, and heat exchanger tube described in layer 5 E includes a heat exchanger tube.
The feed tube can include the first feed tube extended along the radial direction of the spiral winding tube type heat exchanger
11 and second feed tube 12, what the drain pipe included extending along the radial direction of the spiral winding tube type heat exchanger first goes out
The drain pipe 22 of liquid pipe 21 and second, in each layer in the first layer A to the 4th layers of D, wherein the both ends of a heat exchanger tube
The drain pipe 12 of the first feed tube 11 and first is connected to, the both ends of another heat exchanger tube are connected to described second
The drain pipe 22 of feed tube 21 and second, with reference to shown in figure 5, two in two heat exchanger tube a, second layer B in first layer A change
A heat exchanger tube e in two heat exchanger tube d, the layer 5 E in two heat exchanger tube c, the 4th layer of D in heat pipe b, third layer C.Its
In, different liquid can be flowed in the first feed tube 11 and the second feed tube 12, identical liquid can also be flowed.In addition,
The setting of two feed tubes and drain pipe, it is easy to control the pressure value in nine heat exchanger tubes in required scope.
Selectively, the feed tube 12 of the first feed tube 11 and second is substantially conllinear, liquid in first feed tube 11
The flow direction of liquid is on the contrary, first drain pipe 21 and described second in the flow direction of body and second feed tube 12
Drain pipe 22 is substantially conllinear, the flow direction of liquid and the stream of liquid in second drain pipe 22 in first drain pipe 21
It is dynamic in opposite direction, on the basis of liquid flow direction therein, in each layer in the first layer A to the 4th layers of D, two
The liquid feeding end of the heat exchanger tube is connected correspondingly in the same side of first feed tube 11, second feed tube 21 respectively
First feed tube 11, second feed tube 12, may be referred to shown in Fig. 5, outlet end first drain pipe 21,
The same side of second drain pipe 22 is connected correspondingly to first drain pipe 21, the second drain pipe 22.
Selectively, along the length direction, first feed tube 11 is right against first drain pipe 21, and described
Two feed tubes 12 are right against second drain pipe 22, may be referred to shown in Fig. 6, in order to clearly illustrate the end of heat exchanger tube
End, omission show feed tube and drain pipe.
Selectively, the hand of spiral of two layers adjacent of heat exchanger tube can be conversely (with reference to shown in figure 4) so that heat exchanger
Housing 3 in fluid being capable of preferably turbulent flow.
Selectively, in the caliber of heat exchanger tube all in five layers of heat exchanger tube, maximum caliber be 17.6mm~
18.4mm, minimum pipe are 11.6mm~12.4mm, for example, first layer A, the caliber of second layer B heat exchanger tubes be 17.6~
18.4mm, for example, the caliber of first layer A, second layer B heat exchanger tubes is 18.0mm；Third layer C, the caliber of the 4th layer of D heat exchanger tube are
15.6~16.4mm, for example, third layer C, the caliber of the 4th layer of D heat exchanger tube are 16.3mm, the caliber of layer 5 E heat exchanger tubes is
11.6mm~12.4mm, for example, 12.0mm.
Selectively, the first layer A to the heat exchanger tube of the 4th layer of D helix angle all same, can be 30 °~
50 °, such as 35 °, 38 °, 42 °, 46 ° etc.；The helix angle of the heat exchanger tube of the layer 5 E can be 30 °~50 °, such as
35 °, 38 °, 42 °, 46 ° etc..
Selectively, along the direction of ecto-entad, the first layer A to the heat exchanger tube of the 4th layer of D pipe thickness
It is identical, can be 1.6mm~2.0mm, such as 1.8mm；The pipe thickness of the heat exchanger tube of the layer 5 E can be 1.3mm~
1.7mm, such as 1.5mm.
Selectively, in the first layer A to the 4th layers of D heat exchanger tube, between every two layers adjacent of heat exchanger tube
Interlamellar spacing is successively decreased successively, and maximum interlamellar spacing can be 75mm~55mm, for example, 60mm；Minimum interlamellar spacing can be 55mm~
35mm, for example, 45mm；Between spacing and third layer C and the 4th layer of D between the 4th layer of D and layer 5 E heat exchanger tubes
Spacing it is equal.For example, each heat exchanger tube can be 8~9 circles in first layer A heat exchanger tubes, layer diameter can be 265~270mm；
Each heat exchanger tube can be 8~9 circles in second layer B heat exchanger tubes, and layer diameter can be 205~210mm；It is every in 3rd layer of heat exchanger tube
Individual heat exchanger tube can be 9~10 circles, and layer diameter can be 150~155mm；Each heat exchanger tube can be 9 in 4th layer of D heat exchanger tube
~10 circles, layer diameter can be 105~110mm；Layer 5 heat exchanger tube can be 21~22 circle, layer diameter can be 60~
65mm。
In addition, with reference to shown in figure 1, the spiral winding tube type heat exchanger includes housing 3, and the heat exchanger tube is positioned at described
In housing 3, the feed tube stretches out from the housing 3, and the drain pipe stretches out from the housing.
Fig. 7 to Fig. 9 shows a kind of another embodiment for spiral winding tube type heat exchanger that the disclosure provides.Its
In, the spiral winding tube type heat exchanger includes the feed liquor of one end of the length direction positioned at the spiral winding tube type heat exchanger
Pipe 10, positioned at the spiral winding tube type heat exchanger length direction the other end drain pipe 20 and be connected to the feed liquor
Four layers of heat exchanger tube coaxially wound between pipe 10 and drain pipe 20, accordingly for：First layer A, second layer B, third layer C and
Four layers of D, wherein, every layer includes a heat exchanger tube.
Selectively, the feed tube 10 and the drain pipe 10 are along the radial direction side of the spiral winding tube type heat exchanger
To extension, on the basis of liquid flow direction therein, each the liquid feeding end of the heat exchanger tube, outlet end are in the feed tube
10th, the same side of drain pipe 20 is connected correspondingly to the feed tube 10, drain pipe 20.
Selectively, in two adjacent heat exchanger tubes, the liquid feeding end positioned at the heat exchanger tube in outside is connected to institute
One end of feed tube 10 is stated, outlet end is connected to corresponding one end of the drain pipe 20, the heat exchanger tube positioned at inner side
Liquid feeding end is connected to the other end of the feed tube 10, and outlet end is connected to corresponding one end of the drain pipe 20.That is, edge is entered
The flow direction of liquid in liquid pipe 20, in feed tube 20, the rear of the liquid feeding end of the 4th layer of D heat exchanger tube is second layer B heat exchange
The liquid feeding end of pipe, front are the liquid feeding end of third layer C heat exchanger tubes and the liquid feeding end of first layer A heat exchanger tubes successively.
Wherein, heat exchanger tube described in outermost layer, that is, first layer D heat exchanger tubes, liquid feeding end be connected to the feed tube 10
End, on the basis of the flow direction of liquid in feed tube 10, the end corresponds to front end.
Selectively, successively decrease along the direction of ecto-entad, the caliber of four layers of heat exchanger tube, for example, outermost heat exchange
The caliber of pipe can be 17.6~18.4mm, such as 18.0mm；The caliber of the heat exchanger tube of innermost layer can be 11.6~12.4mm,
Such as 12.0mm.
Selectively, the hand of spiral of heat exchanger tube described in adjacent two layers can with identical, when four layers of heat exchanger tube caliber along by
When direction outside to inside is successively decreased, the fluid that is flowed in the housing of heat exchanger being capable of preferably turbulent flow.
Selectively, the helix angle all same of four layers of heat exchanger tube, can be 30 °~50 °, such as 35 °, 38 °,
42 °, 46 ° etc..
Selectively, along the direction of ecto-entad, the first layer A to the heat exchanger tube of third layer C pipe thickness
It is identical, can be 1.6mm~2.0mm, such as 1.8mm；The pipe thickness of the heat exchanger tube of the 4th layer of D can be 1.3mm~
1.7mm, such as 1.5mm.
Selectively, the interlamellar spacing between first layer A and second layer B, second layer B and third layer C heat exchanger tubes is identical, can be with
For 40mm~50mm, such as 45mm；Interlamellar spacing between third layer C and the 4th layer of D heat exchanger tube can be 30mm~40mm, such as
35mm。
In the another embodiment that the disclosure provides, first layer A heat exchanger tubes can have 12~13 circles, the length of heat exchanger tube
Degree can be 11m, and layer diameter can be 185~190mm；Second layer heat exchanger tube can have 14~15 circles, and the length of heat exchanger tube can
Think 9m, layer diameter can be 140~145mm；Third layer C can have 15~16 circles, and the length of heat exchanger tube can be 7.5m, layer
Diameter can be 95~100mm；4th layer of D can have 16~17 circles, and the length of heat exchanger tube can be 6.5m, and layer diameter can be
60~65mm.
In the embodiment shown in Fig. 7 to Fig. 9, the spiral winding tube type heat exchanger include housing (be not shown,
May be referred to the housing 3 in Fig. 1), the heat exchanger tube is located in the housing, and the feed tube 10 stretches out from the housing,
The drain pipe 20 stretches out from the housing.
The preferred embodiment of the disclosure is described in detail above in association with accompanying drawing, still, the disclosure is not limited to above-mentioned reality
The detail in mode is applied, in the range of the technology design of the disclosure, a variety of letters can be carried out to the technical scheme of the disclosure
Monotropic type, these simple variants belong to the protection domain of the disclosure.
It is further to note that each particular technique feature described in above-mentioned embodiment, in not lance
In the case of shield, it can be combined by any suitable means.In order to avoid unnecessary repetition, the disclosure to it is various can
The combination of energy no longer separately illustrates.
In addition, it can also be combined between a variety of embodiments of the disclosure, as long as it is without prejudice to originally
Disclosed thought, it should equally be considered as disclosure disclosure of that.
Claims (10)
1. a kind of spiral winding tube type heat exchanger, it is characterised in that the spiral winding tube type heat exchanger includes being located at the spiral shell
Revolve the feed tube, the length direction positioned at the spiral winding tube type heat exchanger of one end of the length direction of wrap-round tubular heat exchanger
The other end drain pipe and be connected between the feed tube and drain pipe five layers of coaxial spiral winding heat exchanger tube, its
In, along the direction of ecto-entad, first layer (A) to the 4th layer of (D) described heat exchanger tube includes the heat exchanger tube of two articles of wound in parallel,
Layer 5 (E) described heat exchanger tube includes a heat exchanger tube.
2. spiral winding tube type heat exchanger according to claim 1, it is characterised in that the feed tube is included along the spiral shell
The first feed tube (11) and the second feed tube (12), the drain pipe of the radial direction extension of rotation wrap-round tubular heat exchanger include
The first drain pipe (21) and the second drain pipe (22) extended along the radial direction of the spiral winding tube type heat exchanger, described
In each layer in first layer (A) to the 4th layer (D), wherein the both ends of a heat exchanger tube are connected to first feed tube
(11) it is connected to second feed tube (21) and second with the first drain pipe (12), the both ends of another heat exchanger tube and goes out liquid
Manage (22).
3. spiral winding tube type heat exchanger according to claim 2, it is characterised in that first feed tube (11) and
Two feed tubes (12) are substantially conllinear, in first feed tube (11) in the flow direction of liquid and second feed tube (12)
On the contrary, first drain pipe (21) is substantially conllinear with second drain pipe (22), described first goes out for the flow direction of liquid
In liquid pipe (21) in the flow direction of liquid and second drain pipe (22) flow direction of liquid on the contrary, with liquid therein
On the basis of flow direction,
In each layer in the first layer (A) to the 4th layer (D), the liquid feeding end of two articles of heat exchanger tubes is respectively described
One feed tube (11), the same side of second feed tube (21) are connected correspondingly to first feed tube (11), described
Two feed tubes (12), outlet end are connected correspondingly to institute in the same side of first drain pipe (21), the second drain pipe (22)
State the first drain pipe (21), the second drain pipe (22).
4. spiral winding tube type heat exchanger according to claim 3, it is characterised in that along the length direction, described
One feed tube (11) is right against first drain pipe (21), and second feed tube (12) is right against second drain pipe
(22)。
5. spiral winding tube type heat exchanger according to claim 1, it is characterised in that the spiral of two layers adjacent of heat exchanger tube
In the opposite direction.
6. spiral winding tube type heat exchanger according to claim 1, it is characterised in that all in five layers of heat exchanger tube
In the caliber of heat exchanger tube, maximum caliber is 17.6mm~18.4mm, and minimum pipe is 11.6mm~12.4mm.
7. spiral winding tube type heat exchanger according to claim 1, it is characterised in that the first layer (A) to described the
The helix angle all same of the heat exchanger tube of four layers (D), it is 30 °~50 °；The helix angle of the heat exchanger tube of the layer 5 (E) is
30 °~50 °.
8. spiral winding tube type heat exchanger according to claim 1, it is characterised in that the first layer (A) to described the
The pipe thickness all same of the heat exchanger tube of four layers (D), it is 1.6mm~2.0mm；The thickness of pipe wall of the heat exchanger tube of the layer 5 (E)
Spend for 1.3mm~1.7mm.
9. spiral winding tube type heat exchanger according to claim 1, it is characterised in that in the first layer (A) to the 4th
In layer (D) heat exchanger tube, successively decrease successively per the interlamellar spacing between two layers adjacent of heat exchanger tube, maximum interlamellar spacing be 75mm~
55mm, minimum interlamellar spacing are 55mm~35mm, spacing and third layer between the 4th layer (D) and layer 5 (E) heat exchanger tube
(C) spacing between the 4th layer (D) is equal.
10. spiral winding tube type heat exchanger according to claim 1, it is characterised in that the spiral winding pipe type heat exchange
Device includes housing (3), and the heat exchanger tube is located in the housing (3), and the feed tube stretches out from the housing (3), described
Drain pipe stretches out from the housing.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720302397.9U CN206724748U (en) | 2017-03-24 | 2017-03-24 | Spiral winding tube type heat exchanger |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720302397.9U CN206724748U (en) | 2017-03-24 | 2017-03-24 | Spiral winding tube type heat exchanger |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206724748U true CN206724748U (en) | 2017-12-08 |
Family
ID=60501453
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720302397.9U Active CN206724748U (en) | 2017-03-24 | 2017-03-24 | Spiral winding tube type heat exchanger |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206724748U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108954360A (en) * | 2018-06-08 | 2018-12-07 | 浙江涌原新能科技股份有限公司 | A kind of novel energy-saving environment-friendly device |
| CN109141070A (en) * | 2018-09-17 | 2019-01-04 | 北京航空航天大学 | A kind of hexagon helical duct compact heat exchanger |
| CN110822942A (en) * | 2019-11-29 | 2020-02-21 | 陕西益信伟创智能科技有限公司 | Three-dimensional cobweb laminated tube type heat exchanger based on bionics |
-
2017
- 2017-03-24 CN CN201720302397.9U patent/CN206724748U/en active Active
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108954360A (en) * | 2018-06-08 | 2018-12-07 | 浙江涌原新能科技股份有限公司 | A kind of novel energy-saving environment-friendly device |
| CN109141070A (en) * | 2018-09-17 | 2019-01-04 | 北京航空航天大学 | A kind of hexagon helical duct compact heat exchanger |
| CN109141070B (en) * | 2018-09-17 | 2020-07-28 | 北京航空航天大学 | Hexagonal spiral channel compact heat exchanger |
| CN110822942A (en) * | 2019-11-29 | 2020-02-21 | 陕西益信伟创智能科技有限公司 | Three-dimensional cobweb laminated tube type heat exchanger based on bionics |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN206724748U (en) | Spiral winding tube type heat exchanger | |
| CN105823348B (en) | Bifilar stream mixed tube bundle shell-and-tube heat exchanger | |
| EP2351979B1 (en) | Heat Exchanger comprising three concentric tubes | |
| KR20110083996A (en) | Double-piped heat exchanger | |
| ATE538352T1 (en) | TUBES WITH EXTENDED CROSS SECTION FOR FLOODED EVAPORATORS AND CONDENSER | |
| CN206724747U (en) | Spiral winding tube type heat exchanger | |
| CN107255422A (en) | Shell side multiple flow wound tube heat exchanger | |
| CN206944768U (en) | Double pipe heat exchanger | |
| CN202532953U (en) | Jet flow pipe and jet flow heat exchanger with same | |
| CN109506497A (en) | A kind of high-efficiency compact capillary heat exchange of heat pipe | |
| CN206094990U (en) | Multilayer bushing type pre -heater | |
| CN209279723U (en) | A kind of spherical heat exchanger with Dual heat exchange effect | |
| CN107270741A (en) | Multiple flow reduced pipe wound tube heat exchanger | |
| CN207147275U (en) | Multiple flow reduced pipe wound tube heat exchanger | |
| CN206974236U (en) | Shell side multiple flow wound tube heat exchanger | |
| CN110849184A (en) | Full-cyclone shell-and-tube heat exchanger | |
| CN212205796U (en) | Combined baffle plate structure for graphite tube array type heat exchanger | |
| CN212645450U (en) | Horizontal stacked multi-tube pass heat exchanger | |
| CN105823349B (en) | Two-tube-pass mixed tube bundle heat exchanger | |
| CN109253636A (en) | A kind of three runner spiral wound tube type heat exchangers | |
| CN102486353A (en) | Energy-saving high efficiency rapid condenser | |
| CN104623917B (en) | A kind of little temperature difference shell journey becomes the no baffle plate high-efficiency energy-saving evaporator in space | |
| CN203719489U (en) | Double-phase-change latent heat exchanger | |
| CN205090852U (en) | Shell and tube type heat exchanger and shell and tube type heat exchanger group thereof | |
| CN209279737U (en) | A kind of three runner spiral wound tube type heat exchangers |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20210204 Address after: Building 1, 20 Baiziwan Road, Chaoyang District, Beijing Patentee after: BEIJING GLASS GROUP Co.,Ltd. Address before: 100121 nandugezhuang, Chaoyang District, Beijing (Beijing fluorescent lamp factory) Patentee before: BEIJING BOMEI HUAKE GLASS Co.,Ltd. |
|
| CP03 | Change of name, title or address | ||
| CP03 | Change of name, title or address |
Address after: 100124 Building 1, No. 20, Baiziwan Road, Chaoyang District, Beijing Patentee after: Beijing Glass Group Co.,Ltd. Address before: Building 1, 20 Baiziwan Road, Chaoyang District, Beijing Patentee before: BEIJING GLASS GROUP Co.,Ltd. |