CN206739957U - Strake heat exchanger - Google Patents
Strake heat exchanger Download PDFInfo
- Publication number
- CN206739957U CN206739957U CN201720348915.0U CN201720348915U CN206739957U CN 206739957 U CN206739957 U CN 206739957U CN 201720348915 U CN201720348915 U CN 201720348915U CN 206739957 U CN206739957 U CN 206739957U
- Authority
- CN
- China
- Prior art keywords
- cavity
- heat exchanger
- plate
- strake
- low head
- 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.)
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- 238000005192 partition Methods 0.000 claims abstract description 15
- 238000005096 rolling process Methods 0.000 claims abstract description 6
- 238000003466 welding Methods 0.000 claims abstract 2
- 230000000694 effects Effects 0.000 abstract description 8
- 238000005406 washing Methods 0.000 abstract description 2
- 238000004140 cleaning Methods 0.000 description 6
- 239000012530 fluid Substances 0.000 description 4
- 239000007788 liquid Substances 0.000 description 4
- 239000000463 material Substances 0.000 description 3
- 238000007789 sealing Methods 0.000 description 2
- 238000004220 aggregation Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 230000000739 chaotic Effects 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000003670 easy-to-clean Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000002360 explosive Substances 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 230000001376 precipitating Effects 0.000 description 1
Abstract
It the utility model is related to technical field of heat exchangers, a kind of more particularly to strake heat exchanger, including tubular shell, the spiral plate for rolling into cylinder is provided with described housing, uniform welding has branch chapelet on described spiral plate, described spiral plate is internally formed cavity, it is provided with the central partition plate of cavity dimidiation in described cavity, support ring is welded with described central partition plate, the described half cavity upper and lower ends separated by central partition plate are provided with semicircle shrouding, the inlet duct connected with spiral plate is provided with described housing, the outlet conduit connected with the semicircle shrouding of cavity bottom, upper cover is provided with described housing, low head, described upper cover and low head are ellipticity, described upper cover is with being provided with the pipeline connected with cavity on low head；The utility model, can be with turbulization when medium passes through spiral plate by the distribution of branch chapelet, and heat transfer effect is more preferable, and it is convenient for dismounting and washing, be not susceptible to block.
Description
Technical field
It the utility model is related to technical field of heat exchangers, more particularly to a kind of strake heat exchanger.
Background technology
Spiral-plate heat exchanger, it is that two spirality channels are made by two parallel metal plate coils, leads between cold fluid and hot fluid
Cross the heat exchanger that spiral wooden partition is exchanged heat.Spiral-plate heat exchanger is widely used, many application field heat exchanger spirals
Sheet heat exchanger substitutes tubular heat exchanger.Spiral-plate heat exchanger heat conductive efficiency is good, has a self-cleaning effect, non-disconnectable formula structure it is close
Sealing property is good, suitable for hypertoxic, inflammable, explosive or precious fluids heat exchange.But although it has self-cleaning effect, due to
Design or misoperation can also block, and at this moment also be difficult to mechanically clean using dismountable structure, because internal
Do not allow after the chaotic dismounting of structure easy to clean.The shortcomings that spiral-plate heat exchanger maximum is that maintenance is difficult, and inner ring spiral plate such as occurs
Rupture, will make whole equipment scrapping, when pipeline of the medium by heat exchanger, it is undesirable to be usually present heat transfer effect.
Utility model content
The purpose of this utility model is overcome the deficiencies in the prior art, avoid heat exchanger occur when in use block, no
Easily cleaning or maintenance, and provide a kind of strake heat exchanger, the utility model by the way that spiral-plate heat exchanger is improved, when
Medium can be with turbulization when passing through spiral plate, and heat transfer effect is more preferable, and it is convenient for dismounting and washing, be not susceptible to block.
The purpose of this utility model is achieved by the following measures：A kind of strake heat exchanger, including tubular shell, institute
It is provided with the spiral plate for rolling into cylinder in the housing stated, described spiral plate forms helical duct, on described spiral plate
Even to be welded with branch chapelet, described spiral plate is internally formed cavity, is provided with cavity dimidiation in described cavity
Septum cordis plate, is welded with support ring on described central partition plate, and the half cavity upper and lower ends that are separated by central partition plate are equal
Semicircle shrouding is provided with, the inlet duct and outlet conduit for being passed through helical duct, described entrance are provided with described housing
Pipeline is connected with spiral plate, and described outlet conduit connects with the semicircle shrouding of cavity bottom, and described housing upper end is provided with
Upper cover, housing lower end are provided with low head, and described upper cover and low head are ellipticity, described upper cover and lower envelope
The pipeline connected with cavity is provided with head.
Preferably, the crisscross distribution of branch chapelet on the described each helical layer plate for rolling into tubular, the branch of same file
Chapelet and adjacent columns branch chapelet not in the same horizontal line, and on adjacent layer spiral plate between branch chapelet not in same level
On line.
Preferably, described upper cover, low head are by flange and housing seal, and flange intermediate cryptographic packing is close
Envelope.
Preferably, described upper cover both sides are provided with hoisting ring.
Preferably, described low head bottom is provided with supporting leg.
Preferably, described inlet duct, outlet conduit, the pipeline opening of upper low head pipeline are welded with flange.
The beneficial effects of the utility model are：The utility model is by will install elliptoid upper cover additional with on heat exchanger
End socket, can dismantle heat exchanger and inner passage also disassembling cleaning, internal structure clearly arrange it is regular, it is easy to maintenance, clearly
Wash fast, exchanged especially suitable for toughness, the liquid for having precipitating liquid with liquid, and gas-liquid, steam condensation, spiral board channel
The branch chapelet of interior setting is regular, and flowing forms turbulent flow up and down in passage where heated medium, less scaling, and this spiral
Structure can largely reduce the resistance of fluid, improve heat transfer efficiency.
Brief description of the drawings
Fig. 1 is the structural representation of strake heat exchanger.
Fig. 2 is the distribution schematic diagram of branch chapelet.
Fig. 3 is the top view of riser heat exchanger.
In figure：1- housings, 2- spiral plates, 3- branch chapelets, 4- central partition plates, 5- support rings, 6- semicircle shroudings, 7- inlet tubes
Road, 8- outlet conduits, 9- upper covers, 10- low heads, 11- flanges, 12- hoisting rings, 13- supporting legs.
Embodiment
In order to deepen to understanding of the present utility model, the utility model is made below in conjunction with embodiment and accompanying drawing further
It is described in detail.
Embodiment 1：As shown in Figure 1, Figure 2, Figure 3 shows, a kind of strake heat exchanger, including tubular shell 1, set in described housing
The spiral plate 2 for rolling into cylinder is equipped with, described spiral plate forms the exchange that helical duct is used for carrying out medium, described spiral
Branch chapelet 3 is welded with plate, the crisscross distribution of branch chapelet rolled on each helical layer plate of tubular, the arrangement of branch chapelet is plum
Flower-shaped distribution, the branch chapelet of same file and adjacent columns branch chapelet not in the same horizontal line, and on adjacent layer spiral plate it
Between branch chapelet not in the same horizontal line, turbulent flow can be now formed on certain angle when medium passes through pipeline, due to angle
The influence of degree causes the heat transfer effect of turbulent flow more preferable, and branch chapelet is evenly distributed rationally, be easy to the dismounting in later stage with it is clear
Wash, will not cause to perplex during cleaning.Described spiral plate is internally formed cavity, is provided with sky in described cavity
The central partition plate 4 of chamber dimidiation, central partition plate can separate two kinds of materials, and support is welded with described central partition plate
Ring 5, support ring play a part of support, and the half cavity upper and lower ends separated by central partition plate are provided with semicircle envelope
Plate 6, the inlet duct 7 and outlet conduit 8 for being passed through helical duct, described inlet duct and spiral are provided with described housing
Plate connects, and described outlet conduit connects with the semicircle shrouding of cavity bottom, and described housing upper end is provided with upper cover 9, shell
Body lower end is provided with low head 10, and upper low head is ellipticity, and ellipticity can play a part of aggregation and collect, and play
The effect of decompression, it is the junction of into or out material, ensure that the flow of material；Upper cover, low head pass through flange 11
With housing seal, and flange intermediate cryptographic packing seals, and the sealing of such a device is tight, is not easy to reveal when work
Situation, upper cover both sides are provided with the hoisting ring 12 being easily installed, and low head bottom is provided with supporting leg 13.Upper cover and lower envelope
The pipeline connected with cavity is provided with head, pipeline of this connection is to be used to pass in and out medium, inlet duct, outlet conduit, on
The pipeline opening of low head pipeline is welded with flange, and medium can enter what is separated by central partition plate from upper cover when work
Then half of cavity goes out from low head, can also enter from inlet duct, be said from outlet, this outlet conduit is in semicircle shrouding
At the helical duct of connectivity part.
Claims (6)
- A kind of 1. strake heat exchanger, it is characterised in that：Including tubular shell, the spiral shell for rolling into cylinder is provided with described housing Rotating plate, described spiral plate form helical duct, and uniform welding has a branch chapelet on described spiral plate, inside described spiral plate Cavity is formed, is provided with the central partition plate of cavity dimidiation in described cavity, branch is welded with described central partition plate Pushing out ring, the half cavity upper and lower ends separated by central partition plate are provided with semicircle shrouding, are provided with and are passed through on described housing The inlet duct and outlet conduit of helical duct, described inlet duct connect with spiral plate, described outlet conduit and cavity The semicircle shrouding connection of bottom, described housing upper end are provided with upper cover, and housing lower end is provided with low head, described upper envelope Head and low head are ellipticity, and described upper cover is with being provided with the pipeline connected with cavity on low head.
- 2. strake heat exchanger according to claim 1, it is characterised in that：The described each helical layer plate for rolling into tubular On the crisscross distribution of branch chapelet, the branch chapelet of same file with adjacent columns branch chapelet not in the same horizontal line, and adjacent layer Branch chapelet between on spiral plate is not in the same horizontal line.
- 3. strake heat exchanger according to claim 1, it is characterised in that：Described upper cover, low head pass through flange With housing seal, and flange intermediate cryptographic packing seal.
- 4. strake heat exchanger according to claim 3, it is characterised in that：Described upper cover both sides are provided with hoisting ring.
- 5. strake heat exchanger according to claim 3, it is characterised in that：Described low head bottom is provided with supporting leg.
- 6. strake heat exchanger according to claim 1, it is characterised in that：Described inlet duct, up and down outlet conduit, envelope The pipeline opening in head tube road is welded with flange.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720348915.0U CN206739957U (en) | 2017-04-05 | 2017-04-05 | Strake heat exchanger |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720348915.0U CN206739957U (en) | 2017-04-05 | 2017-04-05 | Strake heat exchanger |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206739957U true CN206739957U (en) | 2017-12-12 |
Family
ID=60558534
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720348915.0U Active CN206739957U (en) | 2017-04-05 | 2017-04-05 | Strake heat exchanger |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206739957U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112044363A (en) * | 2020-08-31 | 2020-12-08 | 江苏永大化工机械有限公司 | Coupling reactor for producing ethylene glycol from coal |
-
2017
- 2017-04-05 CN CN201720348915.0U patent/CN206739957U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112044363A (en) * | 2020-08-31 | 2020-12-08 | 江苏永大化工机械有限公司 | Coupling reactor for producing ethylene glycol from coal |
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