CN101893404A - Arch static turbulent element in heat exchange pipe - Google Patents
Arch static turbulent element in heat exchange pipe Download PDFInfo
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- CN101893404A CN101893404A CN 201010246347 CN201010246347A CN101893404A CN 101893404 A CN101893404 A CN 101893404A CN 201010246347 CN201010246347 CN 201010246347 CN 201010246347 A CN201010246347 A CN 201010246347A CN 101893404 A CN101893404 A CN 101893404A
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- disk
- heat exchange
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- exchange pipe
- hollow shaft
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Abstract
The invention provides an arch static turbulent element in a heat exchange pipe, which comprises a hollow shaft and a disk, wherein the disk is an arch protruding rib on the hollow shaft; the outer diameter of the disk is larger than that of the hollow shaft; a heat exchange device applied by the turbulent element comprises a heat exchange pipe, turbulent elements, hanging elements and a support shaft; a plurality of turbulent elements penetrate through the support shaft; and the support shaft is fixed by hanging elements at both ends of the heat exchange pipe. In the technical scheme, when fluid in the heat exchange pipe passes through the turbulent elements, the outer diameter of the hollow shaft at the front end is smaller; when the fluid flows through the arch surface of the disk, the sectional area through which the fluid can flow is reduced; the fluid flows out of a clearance between the outer edge of the disk and the inner surface of the heat exchange pipe; the higher the speed of the fluid is, the larger the mixing degree of the fluid is, and the larger the scouring force on the inner wall of the heat exchange pipe is, thereby being beneficial to preventing and removing scales; and the speed fluctuation of the fluid is larger, and turbulivity is improved, therefore, the reinforced heat transfer effect of the fluid is improved.
Description
Technical field
What the present invention relates to is a kind of interior inserted component that is applied to augmentation of heat transfer and antiscaling, descaling in the heat exchanger tube in the equipment such as shell-and-tube heat exchanger, heat exchange reactor.
Background technology
Current social energy-saving and emission-reduction are the key technologies that the whole world is all paid much attention to, especially all to be applied to many heat exchangers in various fields such as oil, chemical industry, thermoelectricity, nuclear power, metallurgy, light industry, aviation device and boats and ships vehicles, what wherein be most widely used is shell-and-tube heat exchanger, but inwall ubiquity lamination dirt in these heat exchanger tubes, cause fluid transporting resistance in pipeline to increase, meeting blocking pipe when serious, heat transfer property greatly descends simultaneously; Dirt can seriously reduce heat transfer efficiency and cause great energy waste in the heat exchanger tube, meanwhile dirt generally has corrosivity, tube wall is corrosion therefore, leak fluid causes major safety risks, therefore be forced to exactly take stop production and professional cleaning personnel clean in treating method traditionally, so not only stopped over the manufacturing schedule of factory, also needed to pay expensive cleaning charge simultaneously and use; In order to address this problem better, people study the on-line automatic augmentation of heat transfer that employing do not stop production and the various ways and the device of descaling and antiscaling always, but because technology is not mature enough, also do not have widespread adoption to arrive in the middle of the industry.The device of the turbulent element of online rotation, element rotates certain kinetic energy that will consume fluid, and the frictional force during rotation between element and the back shaft is bigger, has shortened the life-span of turbulent element device.
Summary of the invention
The objective of the invention is in heat exchanger tube, to be provided with static turbulent element, promptly can improve heat exchange efficiency, do not consume the kinetic energy of fluid again by the convection cell flow-disturbing.
Technical scheme of the present invention is, arch static turbulent element in heat exchange pipe, comprise hollow shaft and disk, described disk is arranged on the fin on the hollow shaft, the center of disk and hollow shaft centres, described hollow shaft is connected with disk, the external diameter of described disk is greater than the external diameter of hollow shaft, and the external diameter of disk is convenient to fluid flowing in heat exchanger tube less than the internal diameter of heat exchanger tube, and the external diameter of hollow shaft external diameter and disk passes through arc transition, the hollow shaft internal diameter is greater than the diameter of back shaft, fluid flows through the cambered surface that the hollow shaft outer surface flows to disk again, and the cross-sectional area that fluid is flowed through diminishes, and it is big that the axial velocity of the fluid between disk periphery and heat exchanger tube inner surface becomes, the turbulivity of fluid increases, the good mixing effect of fluid, the boundary layer of destruction fluid, the heat exchange efficiency of raising heat exchanger tube; The speed of fluid can produce radial velocity when the cambered surface along disk flows through simultaneously, the fluid heat exchange efficiency that has radial velocity according to the collaborative theory in field increases, the scouring force of heat exchanging inside pipe wall is also bigger, helps removing the dirt on the tube wall, keeps the cleaning of heat exchange tube wall.
Can offer hollow structure on the disk of arch static turbulent element in heat exchange pipe of the present invention, help reducing the flow resistance of convection cell, strengthen the turbulent extent of center fluid simultaneously, can also save the material cost of element.
The disk of arch static turbulent element in heat exchange pipe of the present invention can be made streamlined on its upstream face, is beneficial to fluid and flows through, and reduces the resistance of convection cell.
The disk outer rim of arch static turbulent element in heat exchange pipe of the present invention can offer breach, when fluid flows through breach, turbulivity further strengthens, on breach, can be provided with the inclined-plane, the convection cell pilot flow direction, fluid deflects, and produces certain peripheral speed, improves the heat exchange efficiency of heat exchanger tube.
The disk of arch static turbulent element in heat exchange pipe of the present invention and hollow shaft be by macromolecular material, polymer-based composite, metal or ceramic material, and parameters such as the external diameter of the length of hollow shaft, internal diameter size, external diameter, disk, arc are that working conditions such as the media type, temperature according to the fluid in heat exchanger tube internal diameter, heat exchanger tube length and the heat exchanger tube are determined.
Arch static turbulent element in heat exchange pipe of the present invention, its beneficial effect is: when 1, fluid is flowed through space between heat exchanger tube inwall and the disk, it is big that the axial velocity of fluid becomes, the turbulivity of fluid increases, the good mixing effect of fluid, destroy the boundary layer of fluid, improve the heat exchange efficiency of heat exchanger tube; 2, the speed of fluid can produce radial velocity when the cambered surface along disk flows through, and the scouring force of heat exchanging inside pipe wall is also bigger, helps removing the dirt on the tube wall, keeps the cleaning of heat exchange tube wall; 3, can offer hollow structure on the disk, help reducing the flow resistance of convection cell, can also save material cost simultaneously; 4, disk is made streamlinedly on upstream face, is beneficial to fluid and flows through, and reduces the resistance of convection cell; 5, the disk outer rim can offer breach, and turbulivity further strengthens, and can be provided with the inclined-plane on the breach, and drain fluids further strengthens the turbulivity of fluid, improves the heat exchange efficiency of heat exchanger tube.
Description of drawings
Fig. 1 is the front view of arch static turbulent element in heat exchange pipe of the present invention.
Fig. 2 is the left view of Fig. 1.
Fig. 3 is the three-dimensional structure schematic diagram of Fig. 1.
Fig. 4 is the three-dimensional structure schematic diagram of arch static turbulent element in heat exchange pipe of the present invention, offers hollow structure on disk.
Fig. 5 is the three-dimensional structure schematic diagram of arch static turbulent element in heat exchange pipe of the present invention, offers the profile of tooth breach on disk.
Fig. 6 is the mounting structure schematic diagram that arch static turbulent element in heat exchange pipe of the present invention is used.
Among the figure, 1-hollow shaft, 2-disk, the saturating sky of 3-, 4-breach, 5-water conservancy diversion inclined-plane, 6-heat exchanger tube, 7-back shaft, 8-locating part, 9-suspension member.
The specific embodiment
Figure 6 shows that a kind of examples of implementation of arch static turbulent element in heat exchange pipe of the present invention, arch static turbulent element in heat exchange pipe of the present invention is installed in the heat exchanger tube 6, locating part 8, back shaft 7 and suspension member 9, several arch static turbulent element in heat exchange pipe of the present invention are installed on the back shaft 7 of 9 of two suspension members, suspension member 9 is fixed on heat exchanger tube 6 two ends, the two ends of back shaft 7 are separately fixed on the suspension member 9, arch static turbulent element in heat exchange pipe of the present invention is made up of hollow shaft 1 and disk 2, hollow shaft 1 matches with back shaft 7, the head of the hollow shaft 1 of one of them and the afterbody of another hollow shaft 1 link to each other in per two turbulent elements, the left side is a fluid inlet shown in the figure, and fluid flows to the outer rim of disk 2 from the outer surface of the hollow shaft 1 of each turbulent element.
In Fig. 1 to Fig. 5, Fig. 1 is the front view of arch static turbulent element in heat exchange pipe of the present invention, described turbulent element comprises hollow shaft 1 and disk 2, disk 2 is the fins on hollow shaft 1, its center and hollow shaft 1 centres, hollow shaft 1 is connected with disk 2, the diameter that the diameter of disk 2 is compared hollow shaft 1 is bigger, and less than the internal diameter of heat exchanger tube 6, fluid flows through the cambered surface that hollow shaft 1 flows to disk 2 again, the cross-sectional area that fluid is flowed through diminishes, it is big that the axial velocity of the fluid between disk 2 peripheries and heat exchanger tube 6 inner surfaces becomes, and the turbulivity of fluid increases, the good mixing effect of fluid, destroy the boundary layer of fluid, improve the heat exchange efficiency of heat exchanger tube 6; The speed of fluid can produce radial velocity when the cambered surface along disk 2 flows through simultaneously, the heat exchange efficiency of working in coordination with the fluid of theoretical radial speed according to the field increases, the scouring force of exchange heat pipe 6 inwalls is also bigger, helps removing the dirt on the tube wall, keeps the cleaning and the heat exchange efficiency of heat exchanger tube 6.Fig. 2 is the left view of Fig. 1, Fig. 3 is the three-dimensional structure schematic diagram of Fig. 1, Fig. 4 is the three-dimensional structure schematic diagram of arch static turbulent element in heat exchange pipe of the present invention, disk 2 is provided with empty 3 structures among the figure, saturating empty 3 seamed edges are provided with water conservancy diversion inclined-plane 5, Fig. 5 is the three-dimensional structure schematic diagram of arch static turbulent element in heat exchange pipe of the present invention, and the edge of disk 2 is provided with profile of tooth breach 4 among the figure, is provided with water conservancy diversion inclined-plane 5 at the seamed edge of breach 4.
Among Fig. 4, offer empty 3 structures on the described disk 2, help reducing the flow resistance of convection cell, the heat exchange influential effect of the turbulent flow exchange heat pipe 6 of core flow is not as big from the near fluid turbulent degree of tube wall, the material cost that can also save simultaneously is provided with water conservancy diversion inclined-plane 5 on saturating empty 3 edge.
In Fig. 1 to Fig. 6, described disk 2 is made streamlined on upstream face, and fluid flows in the space between disk 2 outer rims and heat exchanger tube 6 inwalls along the streamlined cambered surface of the outside of disk 2 again, helps fluid and flows through, and reduces the resistance of convection cell.
Among Fig. 5, described disk 2 outer rims can offer breach 4, and when fluid flow through breach 4, turbulivity further strengthened, and described breach 4 is provided with water conservancy diversion inclined-plane 5, drain fluids, and fluid deflects, and produces certain peripheral speed, improves the heat exchange efficiency of heat exchanger tube 6.
The disk 2 of arch static turbulent element in heat exchange pipe of the present invention and hollow shaft 1 are by macromolecular material, polymer-based composite, metal or ceramic material, and parameters such as the external diameter of the length of hollow shaft 1, internal diameter size, external diameter, disk 2, arc are to determine according to working conditions such as the media type of the fluid in heat exchanger tube 6 internal diameters, heat exchanger tube 6 length and the heat exchanger tube 6, temperature.
Claims (6)
1. arch static turbulent element in heat exchange pipe, it is characterized in that: comprise hollow shaft and disk, disk is arranged on the fin on the hollow shaft, the center of disk and hollow shaft centres, hollow shaft is connected with disk, and the external diameter of disk is greater than the external diameter of hollow shaft, and the external diameter of disk is less than the internal diameter of heat exchanger tube, the external diameter of hollow shaft external diameter and disk is by arc transition, and the hollow shaft internal diameter is greater than the diameter of back shaft.
2. arch static turbulent element in heat exchange pipe according to claim 1 is characterized in that: offer hollow structure on the disk.
3. arch static turbulent element in heat exchange pipe according to claim 1 is characterized in that: disk is made streamlined on its upstream face.
4. arch static turbulent element in heat exchange pipe according to claim 1 is characterized in that: the disk outer rim offers breach.
5. arch static turbulent element in heat exchange pipe according to claim 4 is characterized in that: the breach of disk is provided with the inclined-plane.
6. arch static turbulent element in heat exchange pipe according to claim 1 is characterized in that: disk and hollow shaft are by macromolecular material, polymer-based composite, metal or ceramic material.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201010246347 CN101893404A (en) | 2010-08-06 | 2010-08-06 | Arch static turbulent element in heat exchange pipe |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201010246347 CN101893404A (en) | 2010-08-06 | 2010-08-06 | Arch static turbulent element in heat exchange pipe |
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| CN101893404A true CN101893404A (en) | 2010-11-24 |
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| CN 201010246347 Pending CN101893404A (en) | 2010-08-06 | 2010-08-06 | Arch static turbulent element in heat exchange pipe |
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Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102161045A (en) * | 2011-01-13 | 2011-08-24 | 清华大学 | Self-supporting and self-rotating cleaning and scale-removing element in pipe |
| CN102419132A (en) * | 2011-11-11 | 2012-04-18 | 北京化工大学 | Heat exchange tube goes out water end pendant |
| CN102589345A (en) * | 2012-03-14 | 2012-07-18 | 北京化工大学 | Low-flow-resistance quick-mounting hanger |
| CN102878856A (en) * | 2012-10-25 | 2013-01-16 | 北京化工大学 | Baffling and turbulence combined type enhanced heat transfer inner inserting element |
| CN105115347A (en) * | 2015-07-27 | 2015-12-02 | 华中科技大学 | Flow-guiding plug-in device in heat exchange tube |
| CN108993187A (en) * | 2018-09-20 | 2018-12-14 | 龚育才 | Pipeline static hybrid element and pipeline static mixer containing the hybrid element |
| CN112986056A (en) * | 2021-02-09 | 2021-06-18 | 太原理工大学 | Resistance reduction experimental device for reducing circular tube development turbulence section and using method thereof |
| CN114777534A (en) * | 2022-03-30 | 2022-07-22 | 三江乐天化工有限公司 | Cooling device for lean absorption liquid in ethylene oxide production system |
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| GB899785A (en) * | 1960-10-28 | 1962-06-27 | Andre Vandevelde | Turbulence generating element for heat exchangers |
| US4784218A (en) * | 1982-11-01 | 1988-11-15 | Holl Richard A | Fluid handling apparatus |
| US4794980A (en) * | 1987-11-16 | 1989-01-03 | Raydot Incorporated | Air to air heat exchanger |
| RU2027137C1 (en) * | 1991-12-25 | 1995-01-20 | Ерченко Герман Николаевич | Heat exchanger |
| CN2349530Y (en) * | 1998-12-22 | 1999-11-17 | 蔡国庆 | Round type scale-removing cleaner used in pipe |
| WO2001012960A1 (en) * | 1999-08-17 | 2001-02-22 | Emitec Gesellschaft Für Emissionstechnologie Mbh | Mixer element for a fluid that is guided in a pipe |
| CN101551214A (en) * | 2008-04-03 | 2009-10-07 | 北京化工大学 | Rotating piece type automatic-cleaning and heat-transfer enhancing device |
| US20090296411A1 (en) * | 2008-05-28 | 2009-12-03 | Delta Electronics Inc. | Illuminating device and heat-dissipating structure thereof |
-
2010
- 2010-08-06 CN CN 201010246347 patent/CN101893404A/en active Pending
Patent Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB189702650A (en) * | 1897-02-01 | 1898-03-01 | Samuel Chatwood | Improvements in Apparatus for Superheating Steam. |
| GB899785A (en) * | 1960-10-28 | 1962-06-27 | Andre Vandevelde | Turbulence generating element for heat exchangers |
| US4784218A (en) * | 1982-11-01 | 1988-11-15 | Holl Richard A | Fluid handling apparatus |
| US4794980A (en) * | 1987-11-16 | 1989-01-03 | Raydot Incorporated | Air to air heat exchanger |
| RU2027137C1 (en) * | 1991-12-25 | 1995-01-20 | Ерченко Герман Николаевич | Heat exchanger |
| CN2349530Y (en) * | 1998-12-22 | 1999-11-17 | 蔡国庆 | Round type scale-removing cleaner used in pipe |
| WO2001012960A1 (en) * | 1999-08-17 | 2001-02-22 | Emitec Gesellschaft Für Emissionstechnologie Mbh | Mixer element for a fluid that is guided in a pipe |
| CN101551214A (en) * | 2008-04-03 | 2009-10-07 | 北京化工大学 | Rotating piece type automatic-cleaning and heat-transfer enhancing device |
| US20090296411A1 (en) * | 2008-05-28 | 2009-12-03 | Delta Electronics Inc. | Illuminating device and heat-dissipating structure thereof |
Cited By (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102161045A (en) * | 2011-01-13 | 2011-08-24 | 清华大学 | Self-supporting and self-rotating cleaning and scale-removing element in pipe |
| CN102161045B (en) * | 2011-01-13 | 2012-11-14 | 清华大学 | Self-supporting and self-rotating cleaning and scale-removing element in pipe |
| CN102419132A (en) * | 2011-11-11 | 2012-04-18 | 北京化工大学 | Heat exchange tube goes out water end pendant |
| CN102589345A (en) * | 2012-03-14 | 2012-07-18 | 北京化工大学 | Low-flow-resistance quick-mounting hanger |
| CN102589345B (en) * | 2012-03-14 | 2013-05-29 | 北京化工大学 | Low-flow-resistance quick-mounting hanger |
| CN102878856A (en) * | 2012-10-25 | 2013-01-16 | 北京化工大学 | Baffling and turbulence combined type enhanced heat transfer inner inserting element |
| CN105115347A (en) * | 2015-07-27 | 2015-12-02 | 华中科技大学 | Flow-guiding plug-in device in heat exchange tube |
| CN105115347B (en) * | 2015-07-27 | 2017-04-12 | 华中科技大学 | Flow-guiding plug-in device in heat exchange tube |
| CN108993187A (en) * | 2018-09-20 | 2018-12-14 | 龚育才 | Pipeline static hybrid element and pipeline static mixer containing the hybrid element |
| CN108993187B (en) * | 2018-09-20 | 2023-10-27 | 龚育才 | Pipeline static mixing element and pipeline static mixer comprising same |
| CN112986056A (en) * | 2021-02-09 | 2021-06-18 | 太原理工大学 | Resistance reduction experimental device for reducing circular tube development turbulence section and using method thereof |
| CN114777534A (en) * | 2022-03-30 | 2022-07-22 | 三江乐天化工有限公司 | Cooling device for lean absorption liquid in ethylene oxide production system |
| CN114777534B (en) * | 2022-03-30 | 2023-10-27 | 浙江浩浩化工有限公司 | Cooling device for lean absorption liquid in ethylene oxide production system |
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Open date: 20101124 |