CN106288879B - A kind of spiral baffle heat exchanger - Google Patents
A kind of spiral baffle heat exchanger Download PDFInfo
- Publication number
- CN106288879B CN106288879B CN201610844918.3A CN201610844918A CN106288879B CN 106288879 B CN106288879 B CN 106288879B CN 201610844918 A CN201610844918 A CN 201610844918A CN 106288879 B CN106288879 B CN 106288879B
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- China
- Prior art keywords
- heat exchanger
- helical form
- donut
- fin
- fan
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Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D7/00—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
- F28D7/16—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being arranged in parallel spaced relation
- F28D7/1607—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being arranged in parallel spaced relation with particular pattern of flow of the heat exchange media, e.g. change of flow direction
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F9/00—Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
- F28F9/24—Arrangements for promoting turbulent flow of heat-exchange media, e.g. by plates
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- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Fluid Mechanics (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
A kind of spiral baffle heat exchanger, the heat exchanger shell of tube sheet is fixedly connected with including both ends, the helical form disc and donut being installed in heat exchanger shell, through the several heat exchanger tubes for being distributed in helical form disc and donut and being connected with both ends tube sheet, it is arranged on the end cap at heat exchanger shell both ends, the liquid-inlet and liquid outlet being arranged on the side wall of heat exchanger shell both ends, through helical form disc and donut axle center and the core pipe that is connected with both ends tube sheet, the inlet and outlet being connected with heat exchanger tube and core pipe is provided with end cap, it is characterized in that it is provided with several piece fin along in the plate face of the helical form disc and donut hand of spiral.Compared with the prior art the present invention, has the advantages that the flow velocity of medium in heat exchanger shell everywhere is basically identical, effectively prevents medium from being revealed from the gap of helical baffles and intermediate cylindrical core pipe or housing.
Description
Technical field：The present invention relates to a kind of hot swapping.
Background technology：
Spiral baffle heat exchanger, generally comprises both ends and is fixedly connected with the heat exchanger shell of tube sheet, is installed in housing
Helical form disc and donut, through being distributed in the heat-exchanging tube bundle of different size quantity in helical form disc and donut, be connected with water
The water cover of mouth, oil inlet and outlet, hollow cylinder core pipe.During work, along the medium of heat exchanger helical pipe flow direction because of centrifugal force
Effect make it that the velocity of medium close to intermediate region is slower, on the one hand can cause helical baffles and intermediate cylindrical core pipe or housing
Gap location there is leakage current phenomenon, and local deposits may be caused dirt occur, on the other hand so that changing in intermediate region
Adopting heat pipes for heat transfer efficiency is low.
The content of the invention：
It is basically identical, effectively that the goal of the invention of the present invention is to provide a kind of flow velocity of medium in heat exchanger shell everywhere
Prevent medium from the spiral baffle heat exchanger of the gap of helical baffles and intermediate cylindrical core pipe or housing leakage.
The present invention, which is achieved in that, to be fixedly connected with the heat exchanger shell of tube sheet including both ends, is installed in heat exchanger shell
Internal helical form disc and donut, through the several heat exchange for being distributed in helical form disc and donut and being connected with both ends tube sheet
Manage, be arranged on the end cap at heat exchanger shell both ends, the liquid-inlet and liquid discharge that are arranged on the side wall of heat exchanger shell both ends
Mouthful, be provided with and heat exchanger tube and core pipe in helical form disc and donut axle center and the core pipe that is connected with both ends tube sheet, end cap
The inlet and outlet being connected, it is particular in that is provided with several piece along in the plate face of the helical form disc and donut hand of spiral
Fin.
During work, into the medium in heat exchanger shell along helical form disc and donut helical flow, in the stop of fin
Under, block the trend that medium is inclined to heat exchanger shell because of the effect of centrifugal force so that medium in heat exchanger shell everywhere
Flow velocity tend to consistent, and then avoid the medium of prior art from helical baffles and intermediate cylindrical core pipe or the gap of housing
The appearance of the phenomenon of leakage.
Here, helical form disc and donut by fan-shaped helical form baffling Slab element connection that several pieces helically bend and
Into.
Fin is vertically fixed in the plate face of helical form disc and donut, on the surface of fin and helical form disc and donut
The direction of the flowing of the medium of helical flow maintains an equal level.
The present invention is compared with the prior art, basically identical, effectively anti-with flow velocity of the medium in heat exchanger shell everywhere
The advantages of only medium is revealed from the gap of helical baffles and intermediate cylindrical core pipe or housing.
Brief description of the drawings：
Fig. 1 is the structure diagram of the present invention；
Fig. 2 is the structure diagram of the fan-shaped helical form baffling Slab element of spiral bending；
Fig. 3 is the structure diagram of fin；
Fig. 4 is the fan-shaped helical form baffle plate list for the spiral bending that 1 band of embodiment is useful for wearing the pore for connecing heat exchanger tube
The structure diagram of member；
Fig. 5 is the fan-shaped helical form baffle plate list for the spiral bending that 2 band of embodiment is useful for wearing the pore for connecing heat exchanger tube
The structure diagram of member；
Fig. 6 is the fan-shaped helical form baffle plate list for the spiral bending that 3 band of embodiment is useful for wearing the pore for connecing heat exchanger tube
The structure diagram of member；
Fig. 7 is the fan-shaped helical form baffle plate list for the spiral bending that 4 band of embodiment is useful for wearing the pore for connecing heat exchanger tube
The structure diagram of member.
Embodiment：
The present invention is described in further detail in conjunction with drawings and examples：
As shown in Figure 1, 2, the present invention is fixedly connected with the heat exchanger shell 7 of tube sheet 5 including both ends, is installed in heat exchanger shell
Helical form disc and donut 9 in body 7, through being distributed in helical form disc and donut 9 and what is be connected with both ends tube sheet 5 several changes
Heat pipe 8, the end cap 4 for being arranged on 7 both ends of heat exchanger shell, the liquid-inlet 6 being arranged on 7 both ends side wall of heat exchanger shell
(heat source import) and liquid outlet 12 (thermal source outlet), be connected through 9 axle center of helical form disc and donut and with both ends tube sheet 5
Core pipe 10, several heat exchanger tubes 8 and core pipe 10 together, are divided into two groups of pipes, are connected respectively with two groups of pipes wherein being provided with an end cap 4
Logical import 2 (low-temperature receiver import) and 3 (low-temperature receiver outlets) of outlet（Wherein it is provided with two chambers in an end cap, two chambers are respectively with two
Group pipe is connected, and set inlet and outlet is connected with two chambers respectively）, it is particular in that along helical form annulus baffling
Several piece fin a is provided with the plate face of 9 hand of spiral of plate.
The fan-shaped helical form baffling Slab element b that helical form disc and donut 9 are helically bent by several pieces is formed by connecting.
As shown in Fig. 2, fin a is vertically fixed in the plate face of helical form disc and donut 9, the surface of fin a with it is spiral
The direction of the flowing of the medium of helical flow maintains an equal level on shape disc and donut 9.
As shown in Fig. 2, the fan-shaped helical form baffling Slab element b helically bent is fan-shaped for 90 degree, in this way, connecting
Four fan-shaped helical form baffling Slab element b helically bent formed one it is complete spiral.
As shown in Fig. 2, the adjacent two fan-shaped helical form baffling Slab element b helically bent are fixed by rivet
Come, the bottom of fin a is fixed on a riveted plating f, and riveted plating f then rivets the fan-shaped helical form folding for being fixed on and helically bending
On the edge of flowing plate unit b（The riveting that riveting point is connected with the fan-shaped helical form baffling Slab element b that adjacent two helically bend
Point is identical）, so as to form a helical duct seamless and equipped with fin a；Helical form disc and donut 9 are wrapped in core pipe 10
On, between gap be no more than 0.5mm so that medium flows to heat source along this helical duct from heat source import 6 in tube side
Outlet 12.The heat exchanger tube 8 being applied in helical form disc and donut 9 is fixedly connected with tube sheet 5, is realized by the effect of end cap 4
Flowed into low-temperature receiver import 2 and flow out the effect for reaching heat exchange from low-temperature receiver outlet 3 again.
As shown in Figure 2,3, the cross sectional shape of fin a is the fan-shaped combination that rectangle and the length of side do not wait.Fin a edge shapes
For arc, it is to reduce flow resistance.
Fin a is located at the adjacent two fan-shaped helical form baffling Slab element b junctions helically bent and has two panels, and according to
Secondary 1/3,5/6 punishment cloth, the effect of fin a radially on the inside of the annulus c in 9 axle center of helical form disc and donut are to disturb
Stream, makes the big medium water conservancy diversion of edge flow velocity to intermediate region.
Specific fin a sizes, the height of the fin ah 11-3mm smaller than pitch or so, width between 6.5-8mm,
ThicknessmBetween 2.75-3.25mm.
As shown in figure, 5,6,7, the heat exchanger tube 8 quantity on the fan-shaped helical form baffling Slab element b helically bent
There are 4 kinds, be followed successively by 3,5,6 and 8.
Specifically, heat exchanger tube quantity is 3 in Fig. 4, as shown by arrows in FIG., wherein arrow is directed toward fin a arranged directions
, there is arc side in the circumscribed circle center of circle of heat exchanger tube duct d centers of circle composition close to baffle plate intermediate region.Similar, other implementations
The heat exchanger tube of number of cases amount, corresponding fin a arranged directions are as shown in arrow in Fig. 5,6,7.
Further, the fin a and phase radially on the inside of the annulus c in 9 axle center of helical form disc and donut 1/3
The fan-shaped helical form baffling Slab element b junctions e radial direction angles that neighbour two helically bends are between 65-72 °；It is described radially
Fin a on the inside of the annulus c in 9 axle center of helical form disc and donut at 5/6 and baffle plate junction d radial directions angle between
49—61°。
As shown in Figure 4,5, 6, set at the outer ledge of the fan-shaped helical form baffling Slab element b helically bent
There is pull rod to perforate g, connect steady brace to wear and fix the shape of whole helical form disc and donut 9.
Claims (10)
1. a kind of spiral baffle heat exchanger, including both ends are fixedly connected with the heat exchanger shell of tube sheet, are installed in heat exchanger shell
Internal helical form disc and donut, through the several heat exchange for being distributed in helical form disc and donut and being connected with both ends tube sheet
Manage, be arranged on the end cap at heat exchanger shell both ends, the liquid-inlet and liquid discharge that are arranged on the side wall of heat exchanger shell both ends
Mouthful, be provided with and heat exchanger tube and core pipe in helical form disc and donut axle center and the core pipe that is connected with both ends tube sheet, end cap
The inlet and outlet being connected, it is characterised in that be provided with several piece fin along in the plate face of the helical form disc and donut hand of spiral
Piece.
2. spiral baffle heat exchanger according to claim 1, it is characterised in that helical form disc and donut by several pieces helically
The fan-shaped helical form baffling Slab element of bending is formed by connecting.
3. spiral baffle heat exchanger according to claim 2, it is characterised in that the fan-shaped helical form helically bent
Baffling Slab element is fan-shaped for 90 degree, in this way, four the connected fan-shaped helical form baffling Slab element shapes helically bent
It is complete spiral into one.
4. according to the spiral baffle heat exchanger described in claim 1 or 2 or 3, it is characterised in that fin is vertically fixed on spiral
In the plate face of shape disc and donut, the surface and the direction of the flowing of the medium of helical flow on helical form disc and donut of fin
Maintain an equal level.
5. spiral baffle heat exchanger according to claim 4, it is characterised in that the cross sectional shape of fin is rectangle and side
The long fan-shaped combination not waited.
6. spiral baffle heat exchanger according to claim 5, it is characterised in that the bottom of fin is fixed on a riveted plating
On, riveted plating, which then rivets, to be fixed on the edge of the fan-shaped helical form baffling Slab element helically bent.
7. spiral baffle heat exchanger according to claim 5, it is characterised in that fin is helically bent positioned at adjacent two
Fan-shaped helical form baffling Slab element junction and have two panels, and successively radially apart from helical form disc and donut axle center
1/3,5/6 punishes cloth on the inside of annulus.
8. spiral baffle heat exchanger according to claim 7, it is characterised in that described radially apart from helical form annulus
Fin at 1/3 on the inside of the annulus in baffle plate axle center is connected with the fan-shaped helical form baffling Slab element that adjacent two helically bend
Locate radial direction angle between 65-72 °；The radially fin on the inside of the annulus in helical form disc and donut axle center 5/6
With baffle plate junction radial direction angle between 49-61 °.
9. according to the spiral baffle heat exchanger described in claim 5 or 6 or 7 or 8, it is characterised in that the height of the finh 1
1-3mm smaller than pitch or so, width is between 6.5-8mm, thicknessmBetween 2.75-3.25mm.
10. according to the spiral baffle heat exchanger described in claim 5 or 6 or 7 or 8, it is characterised in that the heat exchanger tube in
Quantity has 4 kinds on the fan-shaped helical form baffling Slab element of spiral bending, is followed successively by 3,5,6 and 8.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610844918.3A CN106288879B (en) | 2016-09-23 | 2016-09-23 | A kind of spiral baffle heat exchanger |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610844918.3A CN106288879B (en) | 2016-09-23 | 2016-09-23 | A kind of spiral baffle heat exchanger |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN106288879A CN106288879A (en) | 2017-01-04 |
| CN106288879B true CN106288879B (en) | 2018-05-08 |
Family
ID=57711600
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610844918.3A Active CN106288879B (en) | 2016-09-23 | 2016-09-23 | A kind of spiral baffle heat exchanger |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106288879B (en) |
Citations (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR1596232A (en) * | 1968-03-22 | 1970-06-15 | ||
| CN2339964Y (en) * | 1998-05-12 | 1999-09-22 | 杨杰辉 | Spiral baffle heat-exchanger |
| CN1804528A (en) * | 2006-01-20 | 2006-07-19 | 华南理工大学 | Heat exchanger with complex flowfield helical baffle and its drag-conduction enhanced heat transfer method |
| CN2903886Y (en) * | 2005-11-17 | 2007-05-23 | 江苏工业学院 | Lap screw baffle heat exchanger |
| CN101329143A (en) * | 2008-08-01 | 2008-12-24 | 东南大学 | Trisection ellipse spiral traverse baffle shell type heat exchanger |
| CN201476662U (en) * | 2009-04-30 | 2010-05-19 | 昆山市德准精密模具有限公司 | Radiating fin, radiating fin group and heat sink |
| CN201852513U (en) * | 2010-11-02 | 2011-06-01 | 南京德邦金属装备工程有限公司 | Variable-inclination angle baffle plate heat exchanger |
| CN204666021U (en) * | 2015-05-27 | 2015-09-23 | 郑州大学 | A kind of spiral baffle heat exchanger of flow leakage prevention |
| CN105823358A (en) * | 2016-05-20 | 2016-08-03 | 四平市东升换热器制造有限公司 | Self-sewage-cleaning type spiral plate sewage heat exchanger |
| CN206037784U (en) * | 2016-09-23 | 2017-03-22 | 佛山神威热交换器有限公司 | Heat exchanger with helical flow baffle |
-
2016
- 2016-09-23 CN CN201610844918.3A patent/CN106288879B/en active Active
Patent Citations (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR1596232A (en) * | 1968-03-22 | 1970-06-15 | ||
| CN2339964Y (en) * | 1998-05-12 | 1999-09-22 | 杨杰辉 | Spiral baffle heat-exchanger |
| CN2903886Y (en) * | 2005-11-17 | 2007-05-23 | 江苏工业学院 | Lap screw baffle heat exchanger |
| CN1804528A (en) * | 2006-01-20 | 2006-07-19 | 华南理工大学 | Heat exchanger with complex flowfield helical baffle and its drag-conduction enhanced heat transfer method |
| CN101329143A (en) * | 2008-08-01 | 2008-12-24 | 东南大学 | Trisection ellipse spiral traverse baffle shell type heat exchanger |
| CN201476662U (en) * | 2009-04-30 | 2010-05-19 | 昆山市德准精密模具有限公司 | Radiating fin, radiating fin group and heat sink |
| CN201852513U (en) * | 2010-11-02 | 2011-06-01 | 南京德邦金属装备工程有限公司 | Variable-inclination angle baffle plate heat exchanger |
| CN204666021U (en) * | 2015-05-27 | 2015-09-23 | 郑州大学 | A kind of spiral baffle heat exchanger of flow leakage prevention |
| CN105823358A (en) * | 2016-05-20 | 2016-08-03 | 四平市东升换热器制造有限公司 | Self-sewage-cleaning type spiral plate sewage heat exchanger |
| CN206037784U (en) * | 2016-09-23 | 2017-03-22 | 佛山神威热交换器有限公司 | Heat exchanger with helical flow baffle |
Also Published As
| Publication number | Publication date |
|---|---|
| CN106288879A (en) | 2017-01-04 |
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