CN205718572U - A kind of three-phase interactive mode eddy current heat exchanger - Google Patents
A kind of three-phase interactive mode eddy current heat exchanger Download PDFInfo
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- CN205718572U CN205718572U CN201620406555.0U CN201620406555U CN205718572U CN 205718572 U CN205718572 U CN 205718572U CN 201620406555 U CN201620406555 U CN 201620406555U CN 205718572 U CN205718572 U CN 205718572U
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Abstract
This utility model relates to heat exchanger and strengthening and heat transferring device technical field, particularly relates to a kind of three-phase interactive mode eddy current heat exchanger.Including cylinder, heat exchanger tube, the second phase entrance, the second phase outlet；Cylinder one end is connected by the first packing ring and the first flange bolt；Wherein the first packing ring fits tightly between cylinder and the first flange；Equidistantly it is uniformly distributed on the first circumference of flange direction and is provided with eight the first bolts；The cylinder other end is connected by the second packing ring and the second flange bolt；Wherein the second packing ring fits tightly between cylinder and the second flange；Equidistantly it is uniformly distributed on the second circumference of flange direction and is provided with eight the second bolts；Inner barrel is provided with two pieces of baffling tube sheets；One of baffling tube sheet is welded on the cylinder inboard wall of the first flange side；This utility model heat exchanger and reinforced heat exchanger, heat transfer efficiency is high, and thermal resistance is little, it is possible to carry out three-phase heat transfer, shortens heat transfer time, increases range of application and efficiency.
Description
Technical field
This utility model relates to heat exchanger and strengthening and heat transferring device technical field, particularly relates to a kind of three-phase interactive mode eddy current
Heat exchanger.
Background technology
Heat exchanger in the market has many types, mainly has plate type heat exchanger, shell-and-tube heat exchanger, pipe heat exchanger
Deng, different types of heat exchanger has respective pluses and minuses, such as heat exchange efficiency size, structure complexity, if easily tie
Dirt, if be easy to clean, if easily seepage, if string liquid, floor space size etc. can occur.Lead at heat transfer enhancement technology
Territory, in order to obtain higher heat transfer efficiency and reduce heat transfer resistance etc. and made a lot of change in terms of heat exchanger structure, but with
The design that past heat exchanger is applied to reality owing to processing and fabricating complexity and heat exchange efficiency lifting clearly result in not is considerably less.And
And the device for three-phase heat exchange is also seldom application, its heat exchange efficiency is the highest.
Utility model content
Technical problem to be solved in the utility model, is the technical deficiency for above-mentioned existence, it is provided that a kind of three-phase
Interactive eddy current heat exchanger, uses the baffling tubesheet calculation of inner barrel both sides, on the one hand can play the fixing heat exchanger tube of support
Purpose, on the other hand can realize drainage by shell-side fluid flow direction is controlled again；Heat exchanger tube uses
Corrugated tube design and heat exchanger tube outer wall weld some corrugated fin and on the one hand can increase between fluid by increasing heat exchange area
The coefficient of heat transfer, thus improve heat exchange efficiency, on the other hand corrugated fin outline uses bowl-shape divergent current Alignment Design and interior
The drainage trough that outer surface is provided with, can make the fluid of flow direction reflux along corrugated fin outer wall, thus increase fluid
Turbulent extent, increases the heat exchange between shell-side fluid and heat exchange tube fluid；Employing reinforced heat exchanger designs, it is possible to achieve fluid
After A circle groove, carry out jet further along corrugated fin flaring wall along flow direction, increase turbulent flow degree, thus
Increase heat exchange efficiency further；On the other hand, due to the modular design of corrugated fin Yu reinforced heat exchanger, can be by originally setting
The streamlined wall of meter realizes fixing drainage and causes the generation of eddy current, such that it is able to avoid the shell side worked long hours
The generation of inwall incrustation scale, decreases heat exchange thermal resistance, increases heat transfer coefficient；Additionally the design is on the basis of increasing heat transfer efficiency
Cavity will be set in reinforced heat exchanger in order to improve its range of application, be on the one hand possible not only to save material, on the other hand can
Carry out between reinforced heat exchanger and shell side after runner plate and heat exchange between the second phase fluid being passed through third phase fluid,
Improve the utilization ratio of the second phase fluid heat, and heat exchange kind and the scope of target fluid can be increased；Wherein runner plate
Use in cambered surface the design of drain flange on the one hand can by increase heat exchange area thus enhancing heat transfer thus increase heat exchange
Efficiency, on the other hand can realize the drain of fluid along stationary flowpath；And corrugated fin surfaces externally and internally has newly established drainage trough,
Not only improve heat exchange, and increase eddy current effect further, thus increase turbulent extent.
For solve above-mentioned technical problem, this utility model be the technical scheme is that include cylinder, heat exchanger tube, second
Phase entrance, the second phase outlet；Cylinder one end is connected by the first packing ring and the first flange bolt；Wherein the first packing ring closely pastes
Together between cylinder and the first flange；Equidistantly it is uniformly distributed on the first circumference of flange direction and is provided with eight the first bolts；Cylinder
The body other end is connected by the second packing ring and the second flange bolt；Wherein the second packing ring fit tightly in cylinder and the second flange it
Between；Equidistantly it is uniformly distributed on the second circumference of flange direction and is provided with eight the second bolts；Inner barrel is provided with two pieces of baffle pipes
Plate；One of baffling tube sheet is welded on the cylinder inboard wall of the first flange side；Second piece of baffling tube sheet is welded in the second method
On the cylinder inboard wall of blue side；And baffling tube sheet is provided with a circular ports；Inner barrel is located at by heat exchanger tube；Heat exchanger tube edge
And on barrel lenght direction, sequentially pass through the first flange, circular ports, the second flange；And the heat exchange near the first flange side
The pipe mouth of pipe is the first phase entrance；The heat exchanger tube mouth of pipe near the second flange side is the first phase outlet；Second phase entrance is located at
On the second end face of flange on the downside of one phase outlet；Second phase outlet is provided close on the cylinder body outer wall of the first phase inlet side；Change
Heat pipe outer wall has corrugated fin along uniform welding equidistant on heat exchanger tube length direction；And it is provided with one between each corrugated fin
Individual reinforced heat exchanger；Closely weld between reinforced heat exchanger outer wall and cylinder inboard wall；Reinforced heat exchanger uses thin-walled empty
Chamber is designed；And the reinforced heat exchanger near the first phase inlet side is provided with B circle groove；B circle groove is by third phase
Inlet tube runs through；The right wall of reinforced heat exchanger on the downside of B circle groove is provided with flow path groove；Near the first phase outlet side
Reinforced heat exchanger is provided with C circle groove；C circle groove is run through by third phase outlet；Strengthening on the downside of C circle groove is changed
Thermal left wall face is provided with flow path groove；And set respectively on the reinforced heat exchanger between the reinforced heat exchanger of above both sides
There are two flow path grooves and are distributed up and down；And it is provided with runner plate between the flow path groove that level is corresponding；Runner plate fills with enhanced heat exchange
Put closely welding.
Optimizing the technical program further, described cylinder body outer wall is provided with one layer of heat preservation material.
Optimizing the technical program further, described heat exchanger tube uses corrugated tube design；And heat exchanger tube passes through round tube
After Kou, its outer wall uses expanded joint design with the Type of Welding of baffling tube sheet.
Optimizing the technical program further, described corrugated fin profile uses the design of bowl-shape shape；Appearance in corrugated fin
Face is equidistantly uniformly provided with drainage trough along corrugated fin circumferencial direction；And corrugated fin uses hollow Thin Disk through rolling after heat
Make after processing cooling；Reinforced heat exchanger center uses after hollowing out design and forms an A circle groove；A circle groove straight
Footpath value is more than the external diameter value of heat exchanger tube；And the reinforced heat exchanger end face of A circle groove both sides uses outside divergent current line style
Design；Wherein the radian that tilts near the reinforced heat exchanger end face of the first phase inlet side is less than the inclination arc of other end
Degree.
Optimizing the technical program further, described runner plate outline uses arc design；And runner plate is upper and lower
Cambered surface is equipped with drain flange；Drain flange uses airflow design.
Compared with prior art, this utility model has the advantage that
1, use the baffling tubesheet calculation of inner barrel both sides, on the one hand can play the purpose supporting fixing heat exchanger tube,
On the other hand drainage can be realized by shell-side fluid flow direction is controlled again；
2, heat exchanger tube uses corrugated tube design and the heat exchanger tube outer wall some corrugated fin of welding on the one hand can pass through to increase
Heat exchange area and increase the coefficient of heat transfer between fluid, thus improve heat exchange efficiency, on the other hand corrugated fin outline uses bowl
The drainage trough that shape divergent current Alignment Design and surfaces externally and internally are provided with, can make the fluid of flow direction enter along corrugated fin outer wall
Row backflow, thus increase fluid turbulent degree, increase the heat exchange between shell-side fluid and heat exchange tube fluid；
3, use reinforced heat exchanger design, it is possible to achieve fluid along flow direction after A circle groove further along ripple
Shape fin flaring wall carries out jet, increases turbulent flow degree, thus increases heat exchange efficiency further；
4, on the other hand, due to the modular design of corrugated fin Yu reinforced heat exchanger, can be by the streamline of the design
Type wall realizes fixing drainage and causes the generation of eddy current, such that it is able to avoid the shell side inwall incrustation scale worked long hours
Generation, decrease heat exchange thermal resistance, increase heat transfer coefficient；
5, other the design is increasing on the basis of heat transfer efficiency to improve its range of application by reinforced heat exchanger
It is set to cavity, is on the one hand possible not only to save material, on the other hand can be passed through third phase fluid after runner plate in strengthening
Carry out between heat-exchanger rig and shell side and heat exchange between the second phase fluid, improve the utilization ratio of the second phase fluid heat, and
Heat exchange kind and the scope of target fluid can be increased；
6, the design of drain flange is wherein used in runner plate cambered surface on the one hand can to increase by increasing heat exchange area
Heat transfer coefficient thus increase heat exchange efficiency, on the other hand can realize the drain of fluid along stationary flowpath；
7 and corrugated fin surfaces externally and internally has newly established drainage trough, not only improve heat exchange, and increase eddy current further
Effect, thus increase turbulent extent.
Accompanying drawing explanation
Fig. 1 is a kind of three-phase interactive mode eddy current heat exchanger side block diagram.
Fig. 2 is a kind of three-phase interactive mode eddy current heat exchanger sectional structure chart.
Fig. 3 is a kind of three-phase interactive mode eddy current heat exchanger cross sectional front view.
Fig. 4 is a kind of three-phase interactive mode eddy current heat exchanger cutaway view Amplified image.
Fig. 5 is that the reinforced heat exchanger amplification of the third phase inlet tube side in a kind of three-phase interactive mode eddy current heat exchanger regards
Figure.
Fig. 6 is the middle reinforced heat exchanger zoomed-in view in a kind of three-phase interactive mode eddy current heat exchanger.
Fig. 7 is that the reinforced heat exchanger amplification of the third phase outlet side in a kind of three-phase interactive mode eddy current heat exchanger regards
Figure.
Fig. 8 is a kind of three-phase interactive mode eddy current heat exchanger runner plate zoomed-in view.
Fig. 9 is a kind of three-phase interactive mode eddy current heat exchanger corrugated fin zoomed-in view.
Figure 10 is a kind of three-phase interactive mode eddy current heat exchanger multi-tube heat transfer device view.
Figure 11 is that in a kind of three-phase interactive mode eddy current heat exchanger multi-tube heat transfer, heat exchanger tube regards with the amplification of corrugated fin junction
Figure.
In figure, 1, cylinder；2, heat exchanger tube；3, the second phase entrance；4, the second phase outlet；5, the first packing ring；6, the first flange；
7, the first bolt；8, the second packing ring；9, the second flange；10, the second bolt；11, baffling tube sheet；12, circular ports；13, first
Phase entrance；14, the first phase outlet；15, corrugated fin；16, reinforced heat exchanger；17, drainage trough；18, A circle groove；19、B
Circular groove；20, third phase inlet tube；21, flow path groove；22, C circle groove；23, third phase outlet；24, runner plate；25、
Drain flange.
Detailed description of the invention
For making the purpose of this utility model, technical scheme and advantage of greater clarity, below in conjunction with detailed description of the invention
And referring to the drawings, this utility model is further described.It should be understood that these describe the most exemplary, and do not really want
Limit scope of the present utility model.Additionally, in the following description, the description to known features and technology is eliminated, to avoid not
Obscure concept of the present utility model necessarily.
Detailed description of the invention one: combine shown in Fig. 1-11, goes out including cylinder 1, heat exchanger tube the 2, second phase entrance the 3, second phase
Mouth 4；Cylinder 1 one end is connected with the first flange 6 bolt by the first packing ring 5；Wherein the first packing ring 5 fit tightly in cylinder 1 with
Between first flange 6；Equidistantly it is uniformly distributed on the first flange 6 circumferencial direction and is provided with eight the first bolts 7；Cylinder 1 another
End is connected with the second flange 9 bolt by the second packing ring 8；Wherein the second packing ring 8 fit tightly in cylinder 1 and the second flange 9 it
Between；Equidistantly it is uniformly distributed on the second flange 9 circumferencial direction and is provided with eight the second bolts 10；Cylinder 1 is internal is provided with two pieces of foldings
Flow tube plate 11；One of baffling tube sheet 11 is welded on cylinder 1 inwall of the first flange 6 side；Second piece of baffling tube sheet 11
It is welded on cylinder 1 inwall of the second flange 9 side；And baffling tube sheet 11 is provided with a circular ports 12；Heat exchanger tube 2 sets
Internal in cylinder 1；Heat exchanger tube 2 sequentially passes through the first flange 6, circular ports the 12, second flange 9 on cylinder 1 length direction；
And heat exchanger tube 2 mouth of pipe near the first flange 6 side is the first phase entrance 13；Heat exchanger tube 2 near the second flange 9 side is managed
Mouth is the first phase outlet 14；Second phase entrance 3 is located on the second flange 9 end face on the downside of the first phase outlet 14；Second phase outlet 4
It is provided close on cylinder 1 outer wall of the first phase entrance 13 side；Heat exchanger tube 2 outer wall is along equidistant equal on heat exchanger tube 2 length direction
Even it is welded with corrugated fin 15；And it is provided with a reinforced heat exchanger 16 between each corrugated fin 15；Reinforced heat exchanger
Closely weld between 16 outer walls with cylinder 1 inwall；Cylinder 1 outer wall is provided with one layer of heat preservation material；Heat exchanger tube 2 uses corrugated tube to set
Meter；And heat exchanger tube 2 uses expanded joint to design by the Type of Welding of its outer wall after circular ports 12 with baffling tube sheet 11；Wavy wing
Sheet 15 profile uses the design of bowl-shape shape；Corrugated fin 15 surfaces externally and internally is equidistantly uniformly provided with along corrugated fin 15 circumferencial direction and draws
Chute 17；And corrugated fin 15 uses hollow Thin Disk to make after rolling after-baking cooling；In reinforced heat exchanger 16
The heart uses after hollowing out design and forms an A circle groove 18；The diameter value of A circle groove 18 is more than the external diameter value of heat exchanger tube 2；And
And reinforced heat exchanger 16 end face of A circle groove 18 both sides uses outside divergent current Alignment Design；Wherein enter near the first phase
The radian that tilts of reinforced heat exchanger 16 end face of mouth 13 sides is less than the inclination radian of other end；Reinforced heat exchanger 16 is adopted
Design with thin wall cavity；And the reinforced heat exchanger 16 near the first phase entrance 13 side is provided with B circle groove 19；B circle
Shape groove 19 is run through by third phase inlet tube 20；The right wall of reinforced heat exchanger 16 on the downside of B circle groove 19 is provided with runner
Groove 21；The reinforced heat exchanger 16 exporting 14 sides near the first phase is provided with C circle groove 22；C circle groove 22 is by the 3rd
Phase outlet 23 runs through；Reinforced heat exchanger 16 left wall face on the downside of C circle groove 22 is provided with flow path groove 21；And it is positioned at above
It is respectively equipped with two flow path grooves 21 on reinforced heat exchanger 16 between both sides reinforced heat exchanger 16 and is distributed up and down；And
It is provided with runner plate 24 between the flow path groove 21 that level is corresponding；Runner plate 24 closely welds with reinforced heat exchanger 16；Runner plate 24
Outline uses arc design；And lower camber side is equipped with drain flange 25 on runner plate 24；Drain flange 25 uses streamline
Type designs.
Seeing accompanying drawing 2-4, this utility model heat exchanger three-phase fluid can carry out the heat exchange between gas-liquid, carries out three
Phase heat exchange, heat exchange work is when carrying out, from the first phase entrance 13 toward heat exchanger tube 2 in be passed through cold flow body, cold flow body exports through the first phase
14 discharge, the second phase entrance 3 be passed through hot fluid in shell side, from third phase inlet tube 20 toward the cavity of reinforced heat exchanger 16
Inside it is passed through another cold flow body, with heat exchanger tube 2 in the runner that hot fluid is formed between corrugated fin 15 and reinforced heat exchanger 16
Cold flow body in interior cold flow body and reinforced heat exchanger 16 carries out heat exchange.
Detailed description of the invention two, carries out biphase heat exchange, interior by hot fluid/cold flow from the first phase entrance 13 toward heat exchanger tube 2
Body, from the second phase entrance 3 toward shell side in by cold flow body/hot fluid.
Detailed description of the invention three, carries out biphase heat exchange, from the second phase entrance 3 toward shell side in be passed through hot fluid/cold flow body, by
Third phase inlet tube 20 is passed through cold flow body/hot fluid in the cavity of reinforced heat exchanger.
Detailed description of the invention four, during cleaning operation, under the effect of additional pump and vacuum pump set, is passed through by corresponding entrance
Cleanout fluid is carried out operation.
Detailed description of the invention five, sees accompanying drawing 10-11, and above detailed description of the invention one to four, when needs bigger heat exchange stream
During flux, heat exchanger tube 2 can be changed into many and carry out heat exchange again, and select the baffling tube sheet 11 with multiple circular ports 12
Heat exchanger tube 2 is fixed, carries out expanded joint with the baffling plectane equal with corrugated fin 15 internal diameter the most again, so that heat exchange
Pipe 2 passes baffling plectane to realize the heat exchange of the big flow of multitube.
This utility model, by using the baffling tube sheet 11 of the internal both sides of cylinder 1 to design, on the one hand can play support solid
Determine the purpose of heat exchanger tube 2, on the other hand can realize drainage by shell-side fluid flow direction is controlled again；Change
Heat pipe 2 uses corrugated tube design and heat exchanger tube 2 outer wall to weld some corrugated fin 15 1 aspects can be by increasing heat exchange area
And increase the coefficient of heat transfer between fluid, thus improve heat exchange efficiency, on the other hand corrugated fin 15 outline uses bowl-shape flaring
The drainage trough 17 that airflow design and surfaces externally and internally are provided with, can make the fluid of flow direction carry out along corrugated fin 15 outer wall
Backflow, thus increases fluid turbulent degree, increases the heat exchange between fluid in shell-side fluid and heat exchanger tube 2；Employing enhanced heat exchange fills
Put 16 designs, it is possible to achieve fluid is carried out further along corrugated fin 15 flaring wall after A circle groove 18 along flow direction
Jet, increases turbulent flow degree, thus increases heat exchange efficiency further；On the other hand, change with strengthening due to corrugated fin 15
The modular design of thermal 16, can realize fixing drainage by the streamlined wall of the design and cause the product of eddy current
Raw, such that it is able to avoid the generation of the shell side inwall incrustation scale worked long hours, decrease heat exchange thermal resistance, increase heat transfer coefficient；
Additionally the design increase on the basis of heat transfer efficiency in order to improve its range of application by reinforced heat exchanger 16 in be set to cavity,
On the one hand it is possible not only to save material, on the other hand can be passed through third phase fluid after runner plate 24 at reinforced heat exchanger
Carry out between 16 and shell side and heat exchange between the second phase fluid, improve the utilization ratio of the second phase fluid heat, and can increase
Add heat exchange kind and the scope of target fluid；Wherein use drain flange 25 design on the one hand can lead in runner plate 24 cambered surface
Cross increase heat exchange area thus enhancing heat transfer thus increase heat exchange efficiency, on the other hand can realize stream along stationary flowpath
The drain of body；And corrugated fin 15 surfaces externally and internally has newly established drainage trough 17, not only improve heat exchange, and increase whirlpool further
Stream effect, thus increase turbulent extent；Comprehensive described, this utility model heat exchanger and reinforced heat exchanger, heat transfer efficiency is high,
Thermal resistance is little, it is possible to carry out three-phase heat transfer, shortens heat transfer time, increases range of application and efficiency, is worthy of popularization.
It should be appreciated that above-mentioned detailed description of the invention of the present utility model is used only for exemplary illustration or explains this reality
By novel principle, and do not constitute restriction of the present utility model.Therefore, without departing from spirit and scope of the present utility model
In the case of any modification, equivalent substitution and improvement etc. done, within should be included in protection domain of the present utility model.Additionally,
This utility model claims are intended to fall into scope and border or this scope and border
Whole in equivalents change and modifications example.
Claims (5)
1. a three-phase interactive mode eddy current heat exchanger, it is characterised in that: include cylinder (1), heat exchanger tube (2), the second phase entrance
(3), the second phase outlet (4)；Cylinder (1) one end is connected with the first flange (6) bolt by the first packing ring (5)；Wherein the first pad
Circle (5) fits tightly between cylinder (1) and the first flange (6)；Equidistantly it is uniformly distributed on the first flange (6) circumferencial direction
It is provided with eight the first bolts (7)；Cylinder (1) other end is connected with the second flange (9) bolt by the second packing ring (8)；Wherein
Two packing rings (8) fit tightly between cylinder (1) and the second flange (9)；On the second flange (9) circumferencial direction the most uniformly
It is distributed with eight the second bolts (10)；Cylinder (1) is internal is provided with two pieces of baffling tube sheets (11)；One of baffling tube sheet (11)
It is welded on cylinder (1) inwall of the first flange (6) side；Second piece of baffling tube sheet (11) is welded in the second flange (9) side
Cylinder (1) inwall on；And baffling tube sheet (11) is provided with a circular ports (12)；Heat exchanger tube (2) is located in cylinder (1)
Portion；Heat exchanger tube (2) sequentially passes through the first flange (6), circular ports (12), the second flange on cylinder (1) length direction
(9)；And heat exchanger tube (2) mouth of pipe near the first flange (6) side is the first phase entrance (13)；Near the second flange (9)
Heat exchanger tube (2) mouth of pipe of side is the first phase outlet (14)；Second phase entrance (3) is located at the second method of the first phase outlet (14) downside
On blue (9) end face；Second phase outlet (4) is provided close on cylinder (1) outer wall of the first phase entrance (13) side；Heat exchanger tube (2)
Outer wall has corrugated fin (15) along uniform welding equidistant on heat exchanger tube (2) length direction；And each corrugated fin (15) it
Between be provided with a reinforced heat exchanger (16)；Closely weld between reinforced heat exchanger (16) outer wall with cylinder (1) inwall；Strengthening
Heat-exchanger rig (16) uses thin wall cavity design；And set on the reinforced heat exchanger (16) of the first phase entrance (13) side
There is B circle groove (19)；B circle groove (19) is run through by third phase inlet tube (20)；The strengthening of B circle groove (19) downside is changed
Thermal (16) right wall is provided with flow path groove (21)；Set on the reinforced heat exchanger (16) of first phase outlet (14) side
There is C circle groove (22)；C circle groove (22) is run through by third phase outlet (23)；The strengthening of C circle groove (22) downside is changed
Thermal (16) left wall face is provided with flow path groove (21)；And it is positioned at the enhanced heat exchange between above both sides reinforced heat exchanger (16)
It is respectively equipped with two flow path grooves (21) on device (16) and is distributed up and down；And it is provided with stream between the flow path groove (21) that level is corresponding
Guidance tape (24)；Runner plate (24) closely welds with reinforced heat exchanger (16).
A kind of three-phase interactive mode eddy current heat exchanger the most according to claim 1, it is characterised in that: cylinder (1) outer wall is provided with
One layer of heat preservation material.
A kind of three-phase interactive mode eddy current heat exchanger the most according to claim 1, it is characterised in that: heat exchanger tube (2) uses ripple
Stricture of vagina pipe designs；And heat exchanger tube (2) uses swollen by circular ports (12) its outer wall afterwards with the Type of Welding of baffling tube sheet (11)
Connect design.
A kind of three-phase interactive mode eddy current heat exchanger the most according to claim 1, it is characterised in that: corrugated fin (15) profile
Bowl-shape shape is used to design；Corrugated fin (15) surfaces externally and internally is equidistantly uniformly provided with drainage trough along corrugated fin (15) circumferencial direction
(17)；And corrugated fin (15) uses hollow Thin Disk to make after rolling after-baking cooling；Reinforced heat exchanger (16)
Center uses after hollowing out design and forms A circle groove (18)；The diameter value of A circle groove (18) is more than heat exchanger tube (2)
External diameter value；And reinforced heat exchanger (16) end face of A circle groove (18) both sides uses outside divergent current Alignment Design；Wherein
The radian that tilts of reinforced heat exchanger (16) end face near the first phase entrance (13) side is less than the inclination radian of other end.
A kind of three-phase interactive mode eddy current heat exchanger the most according to claim 1, it is characterised in that: runner plate (24) outline
Employing arc designs；And the upper lower camber side of runner plate (24) is equipped with drain flange (25)；Drain flange (25) uses streamline
Type designs.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620406555.0U CN205718572U (en) | 2016-05-09 | 2016-05-09 | A kind of three-phase interactive mode eddy current heat exchanger |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620406555.0U CN205718572U (en) | 2016-05-09 | 2016-05-09 | A kind of three-phase interactive mode eddy current heat exchanger |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205718572U true CN205718572U (en) | 2016-11-23 |
Family
ID=57303780
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620406555.0U Withdrawn - After Issue CN205718572U (en) | 2016-05-09 | 2016-05-09 | A kind of three-phase interactive mode eddy current heat exchanger |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205718572U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105783554A (en) * | 2016-05-09 | 2016-07-20 | 河北科技大学 | Three-phase interactive vortex heat exchanger and strengthened heat transfer device |
| CN114738586A (en) * | 2021-01-07 | 2022-07-12 | 中国石油天然气股份有限公司 | Pipeline heating device |
-
2016
- 2016-05-09 CN CN201620406555.0U patent/CN205718572U/en not_active Withdrawn - After Issue
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105783554A (en) * | 2016-05-09 | 2016-07-20 | 河北科技大学 | Three-phase interactive vortex heat exchanger and strengthened heat transfer device |
| CN114738586A (en) * | 2021-01-07 | 2022-07-12 | 中国石油天然气股份有限公司 | Pipeline heating device |
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