CN108444330A - A kind of compound intensified heat-transfer pipe - Google Patents

A kind of compound intensified heat-transfer pipe Download PDF

Info

Publication number
CN108444330A
CN108444330A CN201810145072.3A CN201810145072A CN108444330A CN 108444330 A CN108444330 A CN 108444330A CN 201810145072 A CN201810145072 A CN 201810145072A CN 108444330 A CN108444330 A CN 108444330A
Authority
CN
China
Prior art keywords
twisted strip
twisted
strip
pipe
tubular body
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.)
Withdrawn
Application number
CN201810145072.3A
Other languages
Chinese (zh)
Inventor
洪宇翔
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Lishui University
Original Assignee
Lishui University
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Lishui University filed Critical Lishui University
Priority to CN201810145072.3A priority Critical patent/CN108444330A/en
Publication of CN108444330A publication Critical patent/CN108444330A/en
Withdrawn legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/10Process efficiency

Landscapes

  • Rigid Pipes And Flexible Pipes (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)

Abstract

The present invention relates to Summarization on heat transfer enhancement in heat exchangers field more particularly to a kind of augmentation of heat transfer pipes.A kind of compound intensified heat-transfer pipe, including tube body, and the twisted strip in tubular body is set;The twisted strip is that one end of metal strip is fixed, and another free end rotates a certain angle around its center line with length;The twisted strip of tubular body is axially laid out with 180 ° or 360 ° for swing circle along tube body, and a twisted strip unit is formed in each period, is 30 ° ~ 90 ° with the intersecting angle between two neighboring twisted strip unit on root twisted strip.A kind of tubular body twisted strip of the compound intensified heat-transfer pipe of twisted tape inserts forms big longitudinal Vortex in tube hub region and wall section, longitudinal Vortex has the characteristics that high-efficiency low-resistance, so as to implement to manage the high intensity fluid substitution of interior span, to reach flow field homogenizing, temperature gradient at nearly wall is improved, the effect of tube wall rate of heat transfer is increased.

Description

A kind of compound intensified heat-transfer pipe
One divisional application of present patent application, the applying date of former invention patent application case is 2015-10-13, application Number it is for " 2015106576902 " and invention and created name《A kind of compound intensified heat-transfer pipe of twisted tape inserts》.
Technical field
The present invention relates to Summarization on heat transfer enhancement in heat exchangers field more particularly to a kind of compound intensified heat-transfers of twisted tape inserts Pipe.
Background technology
Since the 1970s oil crisis, heat conduction reinforced technology is widely used in all trades and professions and subtracts for energy saving Row, such as the new and high technologies industry neck such as power, metallurgy, oil, chemical industry convention body industrial circle and aviation, electronics, nuclear energy Domain.Due to the needs of industrial production and scientific technological advance, heat conduction reinforced technology is widely paid attention to and is grown in recent decades The development of foot.Whether heat conduction reinforced technology needs external work by it, is divided into actively reinforcing and passive facilitation two types, wherein passively For reinforcement technique due to not needing external work, mode of operation is simple, highly reliable and more extensive use, in numerous passive facilitation technologies In, it is a kind of heat transfer enhancement technology of practicality to manage the interior twisted strip that is inserted into, since simple in structure, performance is stable, is easy to assembly and disassembly and repair The advantages that, the technological transformation and waste heat recovery that can be used for existing heat exchanger are strengthened, and solar water heater, reaction are can be used for The various fields such as device, nuclear cooling device, new energy, have wide practical use.But existing smooth tube is interior to be inserted into twisted strip mostly all It is to use single long twisted strip, the structure of twisted strip is single, is extremely effective for laminar flow operating mode, but for turbulent flow operating mode(Re> 10000), under unit flow resistance power consumption, rate of heat transfer promotes limited extent, and heat transfer comprehensive performance is often less than 1, especially big thunder Under promise number, heat transfer comprehensive performance is lower.
With the development of heat transfer enhancement technology, in recent years, the famous scholar Arthur E. of external augmentation of heat transfer Bergles proposes forth generation heat transfer enhancement technology, i.e., compound, the i.e. complex intensifying of two kinds and two or more heat transfer enhancement technologies Heat transfer technology.Relative to single heat transfer enhancement technology, such as rough rib face enhanced tube(Including band pipe, shaped telescopic tube, helicla flute Pipe, bellows etc.)Or single twisted strip, Combination Intensified Heat Transfer Technology can play the advantage of two kinds of technologies, be superimposed rate of heat transfer, lead to Rational design is crossed, heat transfer comprehensive performance more better than single reinforced element can be obtained within the scope of reasonable pressure drop.
Invention content
To solve the above-mentioned problems, the purpose of the present invention is to provide a kind of compound intensified heat-transfer pipes of twisted tape inserts, should A kind of tubular body twisted strip of the compound intensified heat-transfer pipe of twisted tape inserts forms big longitudinal direction in tube hub region and wall section Whirlpool, longitudinal Vortex have the characteristics that high-efficiency low-resistance, equal to reach flow field so as to implement to manage the high intensity fluid substitution of interior span Change, improve temperature gradient at nearly wall, increases the effect of tube wall rate of heat transfer.
In order to achieve the above purpose, present invention employs technical solutions below:
A kind of compound intensified heat-transfer pipe of twisted tape inserts, including tube body, and the twisted strip in tubular body is set;The twisted strip is One end of metal strip is fixed, and another free end rotates a certain angle around its center line with length;The twisted strip of tubular body is along pipe Body is axial to be laid out with 180 ° or 360 ° for swing circle, a twisted strip unit is formed in each period, on root twisted strip adjacent two Intersecting angle between a twisted strip unit is 30 ° ~ 90 °.
Preferably, the torsion rate of twisted stripy=1.5 ~ 1.0, torsion rateyDefinition be that twisted strip rotates 180 ° of half pitch P and twisted strip WidthWRatio.
Preferably, being provided with trepanning or flow-disturbing object on the twisted strip;The flow-disturbing object can be fin, sawtooth, cylinder Shape flow-disturbing object, spherical shape flow-disturbing object or spike flow-disturbing object.
Preferably, the outer diameter of the tube body, in 20mm or less, tubular body is equipped with single twisted strip.
Preferably, when the outer diameter of the tube body is between 20 ~ 50mm, tubular body is equipped with dual twisted strip;Dual twisted strip Reversed mutually to revolve, i.e., the direction of rotation of one twisted strip is to rotate clockwise, and the direction of rotation of another twisted strip is rotation counterclockwise.
Preferably, when the outer diameter of the tube body is between 20 ~ 50mm, tubular body is equipped with triple twisted strips;Triple twisted strips In at least two twisted strips reversely mutually revolve, i.e., the direction of rotation of one twisted strip is to rotate clockwise, and the direction of rotation of a twisted strip is Rotation counterclockwise.
Preferably, the outer diameter of the tube body, in 50mm or more, tubular body is equipped with quadruple twisted strip;Quadruple twisted strip is in square Battle array shape arrangement, adjacent two twisted strips reversely mutually revolve.
Preferably, the outer diameter of the tube body, in 50mm or more, tubular body is equipped with five heavy twisted strips;The five heavy twisted strip Including center twisted strip, and centered on the twisted strip of center arranged in matrix periphery twisted strip;The center twisted strip is to rotate clockwise, Two adjacent periphery twisted strips reversely mutually revolve.
The present invention uses above-mentioned technical proposal, which is in Period is laid out, and the intersecting angle between two twisted strip units is 30 ° ~ 90 °, and twisted strip is formed greatly in tube hub region and wall section Longitudinal Vortex, twisted strip streamwise can induce generation longitudinal Vortex;Under the structure, longitudinal whorl strengthened heat transfer has been given full play to Advantage, relative to the lateral whirlpool that traditional rough pipe induces, longitudinal Vortex has the characteristics that high-efficiency low-resistance, so as to implement in pipe across Away from high intensity fluid substitution improve temperature gradient at nearly wall to reach flow field homogenizing, increase the effect of tube wall rate of heat transfer Fruit.
Description of the drawings
Fig. 1 is the single twisted strip side view in the present invention.
Fig. 2 is the structural parameters schematic diagram of twisted strip of the present invention.
Fig. 3 is the side view of compound intensified heat-transfer pipe in the present invention.
Fig. 4 is the stereogram of compound intensified heat-transfer pipe in the present invention.
Fig. 5 is that the solid of the embodiment of the present invention 1 is attached to partial sectional view.
Fig. 6 is the side view of the embodiment of the present invention 1.
Fig. 7 is the axonometric drawing of the embodiment of the present invention 1.
Fig. 8 is the side view of the single twisted strip of the embodiment of the present invention 1.
Fig. 9 is that the solid of the embodiment of the present invention 2 is attached to partial sectional view.
Figure 10 is the side view of the embodiment of the present invention 2
Figure 11 is the axonometric drawing of the embodiment of the present invention 2.
Figure 12 is the side view of double twisted strips in the embodiment of the present invention 2.
Figure 13 is that the solid of the embodiment of the present invention 3 is attached to partial sectional view.
Figure 14 is the side view of the embodiment of the present invention 3.
Figure 15 is the axonometric drawing of the embodiment of the present invention 3.
Figure 16 is the side view of double twisted strips in the embodiment of the present invention 3.
Figure 17 is the side view for intersecting double twisted strips in the embodiment of the present invention 4.
Figure 18 is the axonometric drawing for intersecting double twisted strip a cycles in the embodiment of the present invention 4.
Figure 19 is the axonometric drawing that the embodiment of the present invention 5 intersects double twisted strip a cycles.
Figure 20 is the axonometric drawing that the embodiment of the present invention 6 intersects double twisted strip a cycles.
Figure 21 is the axonometric drawing that the embodiment of the present invention 7 intersects double twisted strip a cycles.
Figure 22 is the axonometric drawing that the embodiment of the present invention 8 intersects double twisted strip a cycles.
Figure 23 is that the solid of the embodiment of the present invention 9 is attached to partial sectional view.
Figure 24 is the side view of the embodiment of the present invention 9.
Figure 25 is the axonometric drawing of the embodiment of the present invention 9.
Figure 26 is the side view one of three twisted strips in embodiment 9.
Figure 27 is the side view two of three twisted strips in embodiment 9.
Figure 28 is that the solid of the embodiment of the present invention 10 is attached to partial sectional view.
Figure 29 is the side view of the embodiment of the present invention 10.
Figure 30 is the axonometric drawing of the embodiment of the present invention 10.
Figure 31 is the side view one of 10 4 twisted strip of the embodiment of the present invention.
Figure 32 is the side view two of 10 4 twisted strip of the embodiment of the present invention.
Figure 33 is that the solid of the embodiment of the present invention 11 is attached to partial sectional view.
Figure 34 is the axonometric drawing of the embodiment of the present invention 11.
Figure 35 is the side view one of 11 5 twisted strip of the embodiment of the present invention.
Figure 36 is the side view two of 11 5 twisted strip of the embodiment of the present invention.
Specific implementation mode
Below in conjunction with the accompanying drawings, the preferred embodiments of the invention are described in further detail.
A kind of compound intensified heat-transfer pipe of twisted tape inserts as shown in Fig. 1 ~ 4, including tube body, and be arranged in tubular body Twisted strip;The twisted strip is that one end of metal strip is fixed, and another free end rotates a certain angle around its center line with length;Tube body Internal twisted strip is axially laid out with 180 ° or 360 ° for swing circle along tube body, a twisted strip unit is formed in each period, together Intersecting angle on root twisted strip between two neighboring twisted strip unit is 30 ° ~ 90 °.The torsion rate of the twisted stripy=1.5 ~ 1.0, torsion ratey Definition be that twisted strip rotates 180 ° of half pitchPWith twisted strip widthWRatio.Trepanning or flow-disturbing object are provided on twisted strip;Flow-disturbing Object can be fin, sawtooth, cylindric flow-disturbing object, spherical shape flow-disturbing object or spike flow-disturbing object.The tubular body is generally arranged There is 1 ~ 5 twisted strip, specifically related to the size of outer tube diameter, such as when the outer diameter of tube body is in 20mm or less, tubular body is equipped with Single twisted strip;When the outer diameter of the tube body is between 20 ~ 50mm, tubular body is equipped with dual twisted strip;The dual reversed phase of twisted strip Rotation, i.e., the direction of rotation of one twisted strip are to rotate clockwise, and the direction of rotation of another twisted strip is rotation counterclockwise.When the pipe When the outer diameter of body is between 20 ~ 50mm, tubular body is equipped with triple twisted strips;At least two twisted strips reversely mutually revolve in triple twisted strips, The direction of rotation of i.e. one twisted strip is to rotate clockwise, and the direction of rotation of a twisted strip is rotation counterclockwise.When the tube body For outer diameter in 50mm or more, tubular body is equipped with quadruple twisted strip;Quadruple twisted strip is in rectangular arrangement, the reversed phase of adjacent two twisted strips Rotation.When the outer diameter of the tube body is in 50mm or more, tubular body is equipped with five heavy twisted strips;The five weights twisted strip includes that center is turned round Band, and centered on the twisted strip of center arranged in matrix periphery twisted strip;The center twisted strip is to rotate clockwise, adjacent two Periphery twisted strip reversely mutually revolves.The tube body is just(It is remaining)Raised line design pipe, just(It is remaining)Raised line design rib height is preferably 0.5 ~ 2mm, and rib line shakes Width is preferably 8 ~ 20 mm, and the number of cycles on circumferencial direction is preferably 2 ~ 8, and the pitch in flow direction is preferably 10 ~ 50mm.
Above-mentioned technical proposal takes full advantage of the high-efficiency low-resistance characteristic of longitudinal Vortex, and the present invention designs mostly longitudinal in a kind of pipe The Combination Intensified Heat Transfer Technology of whirlpool superposition, is combining tube body just(It is remaining)Both the special construction of string rib line and twisted strip can lure Artificial delivery life is along the longitudinal Vortex flowed to, just(It is remaining)String rib line can induce multiple relatively small one in the region close to tube wall by rib line The longitudinal Vortex of point, each period on circumferencial direction is just(It is remaining)String rib line can induce generation longitudinal Vortex;Twisted strip is in pipe Heart district domain forms big longitudinal Vortex with wall section;By the collaboration relay of size longitudinal Vortex, not only for compared with pipe with small pipe diameter, for Compared with Large Diameter Pipeline, the high intensity fluid substitution for managing interior span can also be implemented, to reach flow field homogenizing, improve temperature ladder at nearly wall Degree, to make the rate of heat transfer under unit work consumptiom be improved, that is, comprehensive performance of conducting heat is improved.In addition, the biography of the present invention Hot comprehensive performance is controllable, and structural parameters can be adjusted flexibly according to concrete operations operating mode and flow media.In conjunction with aftermentioned The structural parameters of attached drawing, the used tube body of the present invention and twisted strip include, as shown in Fig. 2,PRepresent half-section when twisted strip rotates 180 ° Away from length,WRepresent the width of twisted strip;As shown in Fig. 6,LIt represents just(It is remaining)The rib line pitch of raised line design pipe,AIt represents just(It is remaining) The rib line amplitude of raised line design pipe;As shown in Fig. 7,dIt represents just(It is remaining)The outer diameter of raised line design pipe,eIt represents just(It is remaining)The rib of raised line design pipe is high,tIt represents just(It is remaining)The wall thickness of raised line design pipe,BRepresent the thickness of twisted strip;In additionnIt represents just(It is remaining)The circumferential number of string pattern pipe;Also Have as shown in Fig. 8,CRepresent the length of pitch when twisted strip is rotated by 360 °;As shown in attached drawing 17 ~ 18,ɑRepresent two neighboring pitch The angle intersected between twisted strip, the meaning that the structural parameters variable of other figures represents are as described above.
By combining and screening in practice, best structural parameters assembled scheme can be derived that.With reference to above-mentioned implementation The structure of scheme enumerates the structural parameters assembled scheme of multigroup compound intensified heat-transfer pipe, for further being retouched to the present invention It states, wherein each embodiment is both needed to combine above structure, and the implementation of the present invention is not limited to this, every to the present invention Essence is made simple modification or is changed, and the range of technical solution of the present invention is belonged to.In addition, in order to evaluate the property of each embodiment Can, definition heat transfer comprehensive performance is:, whereinPECRepresent heat transfer comprehensive performance, that is, property It can evaluation criterion(Performance evaluation criterion,PEC),Nu 0NuRespectively represent light pipe and enhanced tube Dimensionless rate of heat transfer, that is, nusselt number,f 0fRespectively represent the dimensionless pressure drop i.e. friction factor of light pipe and enhanced tube, same to work( Under consumption, ifPECMore than 1, then the comprehensive performance that illustrates to conduct heat is improved with respect to light pipe, on the contrary then do not improve.
Embodiment 1:
As shown in attached drawing 5 ~ 8, a kind of outer tube diameter of the compound intensified heat-transfer pipe of twisted tape inserts is in 20mm hereinafter, tube body is Just(It is remaining)Raised line design pipe, just(It is remaining)The rib line pitch of raised line design pipeL=20mm, rib line amplitudeA=12mm, circumferential rib line numbern=4, outer diameterd=19mm, wall thicknesst=2mm, rib are highe=1.1mm is internally provided with single twisted strip, twisted strip torsion rate y=2.67, half pitchP=32mm, section Away fromC=64mm, twisted strip thicknessB=1mm, twisted strip widthW=12mm。
Embodiment 2:
As shown in attached drawing 9 ~ 12, a kind of outer tube diameter of the compound intensified heat-transfer pipe of twisted tape inserts is between 20 ~ 50mm, pipe Body is just(It is remaining)Raised line design pipe, just(It is remaining)The rib line pitch of raised line design pipeL=30mm, rib line amplitudeA=16mm, circumferential rib line numbern=8, Outer diameterd=32mm, wall thicknesst=3mm, rib are highe=0.8mm;Tubular body is provided with dual twisted strip, dual twisted strip it is oppositely oriented, i.e., A piece twisted strip is rotated clockwise around central shaft, and in addition a twisted strip rotates counterclockwise around central shaft, is conducive to improve vortex intensity. The twisted strip torsion ratey=2.87, half pitchP=33mm, pitchC=66mm, twisted strip thicknessB=1mm, twisted strip widthW=11.5mm。
Embodiment 3:
As shown in attached drawing 13 ~ 16, a kind of outer tube diameter of the compound intensified heat-transfer pipe of twisted tape inserts between 20 ~ 50mm, Tube body is just(It is remaining)Raised line design pipe, just(It is remaining)The rib line pitch of raised line design pipeL=20mm, rib line amplitudeA=12mm, circumferential rib line numbern= 6, outer diameterd=32mm, wall thicknesst=3mm, rib are highe=1.1mm;Tubular body is provided with dual twisted strip, dual twisted strip it is oppositely oriented, Be conducive to improve vortex intensity;Twisted strip torsion ratey=2.09, half pitchP=24mm, pitchC=48mm, twisted strip thicknessB=1mm, twisted strip WidthW=11.5mm.When turbulent flow, opposite light pipe rate of heat transfer maximum can improve 2 times or more, with comprehensive performance of under power consumption, conducting heat Reach 1.1 or more.
Embodiment 4:
As shown in attached drawing 17 ~ 18, the present embodiment difference from Example 3 is between the twisted strip unit on same root twisted strip Layout is to intersect, cross angleɑIt it is 90 °, other structures size is the same as embodiment 3;The opposite heat transfer of embodiment 3 comprehensive performance is maximum It can be improved 8% or more.
Embodiment 5:
As shown in Fig. 19, the present embodiment difference from Example 4 is the friendship between the twisted strip unit on same root twisted strip It is different to pitch angle, cross angleɑIt it is 75 °, other structures size is the same as embodiment 4.
Embodiment 6:
As shown in Fig. 20, the present embodiment difference from Example 4 is the friendship between the twisted strip unit on same root twisted strip It is different to pitch angle, cross angleɑIt it is 60 °, other structures size is the same as embodiment 4.
Embodiment 7:
As shown in Fig. 21, the present embodiment difference from Example 4 is the friendship between the twisted strip unit on same root twisted strip It is different to pitch angle, cross angleɑIt it is 45 °, other structures size is the same as embodiment 4.
Embodiment 8:
As shown in Fig. 22, the present embodiment difference from Example 4 is the friendship between the twisted strip unit on same root twisted strip It is different to pitch angle, cross angleɑIt it is 30 °, other structures size is the same as embodiment 4.
Embodiment 9:
As shown in attached drawing 23 ~ 27, a kind of outer tube diameter of the compound intensified heat-transfer pipe of twisted tape inserts between 20 ~ 50mm, Tube body is just(It is remaining)Raised line design pipe, just(It is remaining)The rib line pitch of raised line design pipeL=30mm, rib line amplitudeA=20mm, circumferential rib line numbern= 6, outer diameterd=45mm, wall thicknesst=2.5mm, rib are highe=0.8mm;Tubular body is provided with triple twisted strips, wherein two in triple twisted strips Root twisted strip it is oppositely oriented, two twisted strips are rotated clockwise around central shaft, and in addition a twisted strip rotates counterclockwise around central shaft;It turns round Band torsion ratey=2.06, half pitchP=36mm, pitchC=72mm, twisted strip thicknessB=1mm, twisted strip widthW=17.5mm。
Embodiment 10:
As shown in attached drawing 28 ~ 32, a kind of outer tube diameter of the compound intensified heat-transfer pipe of twisted tape inserts is in 50mm or more, tube body For just(It is remaining)Raised line design pipe, just(It is remaining)The rib line pitch of raised line design pipeL=25mm, rib line amplitudeA=12mm, circumferential rib line numbern=6, outside Diameterd=57mm, wall thicknesst=3.5mm, rib are highe=1.5mm;Tubular body is provided with quadruple twisted strip, and quadruple twisted strip is in rectangular arrangement, It is wherein oppositely oriented per adjacent two twisted strips in quadruple twisted strip;Twisted strip torsion ratey=2.5, half pitchP=47.5mm, pitchC= 95mm, twisted strip thicknessB=1mm, twisted strip widthW=19mm.When turbulent flow, intraductal heat transfer rate is with respect to light pipe increase rate up to 2.5 Times, heat transfer comprehensive performance can reach 1.2 or more.
Embodiment 11:
As shown in attached drawing 33 ~ 36, a kind of outer tube diameter of the compound intensified heat-transfer pipe of twisted tape inserts is in 50mm or more, tube body For just(It is remaining)Raised line design pipe, just(It is remaining)For the structural parameters of raised line design pipe with embodiment 10, tubular body is provided with five heavy twisted strips;Described five Weight twisted strip include center twisted strip, and centered on the twisted strip of center arranged in matrix periphery twisted strip;Center twisted strip is rotation clockwise Turn, periphery twisted strip each adjacent two in addition to the twisted strip of center is oppositely oriented;Half pitch of twisted strip, pitch and the same embodiment of thickness 10, twisted strip widthW=15.5mm。

Claims (1)

1. a kind of compound intensified heat-transfer pipe, including tube body, and the twisted strip in tubular body is set;It is characterized in that:The pipe Body is positive raised line design pipe or cosine line pipe, and positive raised line design or a height of 0.5 ~ 2mm of cosine line rib, rib line amplitude are 8 ~ 20 mm, circumference side Upward number of cycles is 2 ~ 8, and the pitch in flow direction is 10 ~ 50mm;The twisted strip is that one end of metal strip is fixed, it is another from It is rotated a certain angle with length around its center line by holding;The twisted strip of tubular body is axially rotation with 180 ° or 360 ° along tube body Period is laid out, and a twisted strip unit is formed in each period, with the intersecting angle between two neighboring twisted strip unit on root twisted strip It is 30 ° ~ 90 °;The torsion rate of twisted stripy=1.5 ~ 1.0, torsion rateyDefinition be that twisted strip rotates 180 ° of half pitchPWith twisted strip widthWIt Ratio;Trepanning or flow-disturbing object are provided on the twisted strip;The flow-disturbing object is fin, sawtooth, cylindric flow-disturbing object, spherical shape are disturbed Flow object or spike flow-disturbing object;For the outer diameter of the tube body between 20 ~ 50mm, tubular body is equipped with dual twisted strip;Dual twisted strip is anti- Xiang Xiangxuan, i.e., the direction of rotation of one twisted strip are to rotate clockwise, and the direction of rotation of another twisted strip is rotation counterclockwise.
CN201810145072.3A 2015-10-13 2015-10-13 A kind of compound intensified heat-transfer pipe Withdrawn CN108444330A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201810145072.3A CN108444330A (en) 2015-10-13 2015-10-13 A kind of compound intensified heat-transfer pipe

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
CN201510657690.2A CN105300156B (en) 2015-10-13 2015-10-13 A kind of compound intensified heat-transfer pipe of twisted tape inserts
CN201810145072.3A CN108444330A (en) 2015-10-13 2015-10-13 A kind of compound intensified heat-transfer pipe

Related Parent Applications (1)

Application Number Title Priority Date Filing Date
CN201510657690.2A Division CN105300156B (en) 2015-10-13 2015-10-13 A kind of compound intensified heat-transfer pipe of twisted tape inserts

Publications (1)

Publication Number Publication Date
CN108444330A true CN108444330A (en) 2018-08-24

Family

ID=55197704

Family Applications (6)

Application Number Title Priority Date Filing Date
CN201810144949.7A Withdrawn CN108507398A (en) 2015-10-13 2015-10-13 Compound intensified heat-transfer pipe
CN201810144916.2A Withdrawn CN108469199A (en) 2015-10-13 2015-10-13 Augmentation of heat transfer pipe
CN201810145072.3A Withdrawn CN108444330A (en) 2015-10-13 2015-10-13 A kind of compound intensified heat-transfer pipe
CN201510657690.2A Expired - Fee Related CN105300156B (en) 2015-10-13 2015-10-13 A kind of compound intensified heat-transfer pipe of twisted tape inserts
CN201810144920.9A Withdrawn CN108489316A (en) 2015-10-13 2015-10-13 The compound intensified heat-transfer pipe of twisted tape inserts
CN201810145073.8A Withdrawn CN108489317A (en) 2015-10-13 2015-10-13 A kind of augmentation of heat transfer pipe

Family Applications Before (2)

Application Number Title Priority Date Filing Date
CN201810144949.7A Withdrawn CN108507398A (en) 2015-10-13 2015-10-13 Compound intensified heat-transfer pipe
CN201810144916.2A Withdrawn CN108469199A (en) 2015-10-13 2015-10-13 Augmentation of heat transfer pipe

Family Applications After (3)

Application Number Title Priority Date Filing Date
CN201510657690.2A Expired - Fee Related CN105300156B (en) 2015-10-13 2015-10-13 A kind of compound intensified heat-transfer pipe of twisted tape inserts
CN201810144920.9A Withdrawn CN108489316A (en) 2015-10-13 2015-10-13 The compound intensified heat-transfer pipe of twisted tape inserts
CN201810145073.8A Withdrawn CN108489317A (en) 2015-10-13 2015-10-13 A kind of augmentation of heat transfer pipe

Country Status (1)

Country Link
CN (6) CN108507398A (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106895733B (en) * 2017-02-08 2019-08-06 哈尔滨工程大学 A kind of novel coaxial intersects the thermoexcell of tie and the application tie
RU2725307C1 (en) * 2019-10-11 2020-06-30 федеральное государственное бюджетное образовательное учреждение высшего образования "Донской государственный технический университет", (ДГТУ) Multi-form composite bimetallic pipeline
CN112728990A (en) * 2020-12-30 2021-04-30 佛山科学技术学院 Heat exchange tube with ball inserted inside

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1727833A (en) * 2004-07-30 2006-02-01 株洲工学院 Bringing along automatic cleanout inside pipe by teeth at rotational flow mouth, and technique for strengthening heat transfer
CN201246993Y (en) * 2008-06-30 2009-05-27 刘卫东 Internal tooth type hot extrusion aluminum pipe
CN203443449U (en) * 2013-08-29 2014-02-19 山东科技大学 Combined bond insert
CN104180689A (en) * 2014-08-25 2014-12-03 哈尔滨工程大学 Built-in full-length twisted ball projecting tube type heat exchanger

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN2089155U (en) * 1990-08-02 1991-11-20 上海市红光锅炉厂 Inserting twist-belt type turbolator for forced heat transfer in pipe
CN201069336Y (en) * 2007-03-28 2008-06-04 陈舒萍 An intensified heat exchange device for heat conduction pipe
CN102997740A (en) * 2011-09-09 2013-03-27 杨伟光 Novel reinforced tube for boiling and heat exchange in tube
CN203824400U (en) * 2014-05-16 2014-09-10 北京京诚凤凰工业炉工程技术有限公司 Heat exchange tube and insert

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1727833A (en) * 2004-07-30 2006-02-01 株洲工学院 Bringing along automatic cleanout inside pipe by teeth at rotational flow mouth, and technique for strengthening heat transfer
CN201246993Y (en) * 2008-06-30 2009-05-27 刘卫东 Internal tooth type hot extrusion aluminum pipe
CN203443449U (en) * 2013-08-29 2014-02-19 山东科技大学 Combined bond insert
CN104180689A (en) * 2014-08-25 2014-12-03 哈尔滨工程大学 Built-in full-length twisted ball projecting tube type heat exchanger

Also Published As

Publication number Publication date
CN108489316A (en) 2018-09-04
CN108507398A (en) 2018-09-07
CN108469199A (en) 2018-08-31
CN108489317A (en) 2018-09-04
CN105300156A (en) 2016-02-03
CN105300156B (en) 2018-05-15

Similar Documents

Publication Publication Date Title
CN105300156B (en) A kind of compound intensified heat-transfer pipe of twisted tape inserts
CN206683439U (en) A kind of fin heat exchanger
CN202442625U (en) Energy-saving self-cleaning pipe
CN202281538U (en) Heat exchange tube internally provided with spiral spoilers
CN106979714A (en) A kind of lozenge fin tube beam
CN103697740A (en) Inner petal-shaped irregular-shaped heat exchange tube
CN101839670A (en) Inner diversion type self-tightening hanging part of heat exchange tube
CN205505825U (en) Heat exchange tube of air ability water heater
CN101532797A (en) Enhanced heat transfer unit of self-drive periodically brushing boundary layer fracture in heat exchange tube
CN203163576U (en) Variable-diameter wave node heat exchange pipe
CN203259054U (en) Tube fin heat exchanger
CN201611236U (en) Double spiral vortex tube
CN204787980U (en) Heat exchange tube of interpolation interval hurricane band
CN203037125U (en) Double-sided reinforced heat exchange tube
CN203908385U (en) Novel grating spiral link
CN205940267U (en) Turbulent flow heat exchange tube and heat exchanger
CN102735089A (en) Heat transfer pipe, and heat and mass transfer equipment having heat transfer pipe
CN203629403U (en) Inner petal special-shaped heat exchange tube
CN205002648U (en) Variable cross section heat exchange tube and shell and tube type heat exchanger
CN204514129U (en) Double-tube heat exchanger
CN204142047U (en) Tubular type gas-liquid heat-exchange
CN103940283B (en) A kind of longitudinal turbulence works in coordination with generating polynomial heat transfer element
CN204787979U (en) Revolve to hurricane band in turn and be equipped with its heat exchange tube
CN206787361U (en) A kind of lozenge fin tube binding structure
CN203464832U (en) Turbulent flow element of convection heat transfer in strengthening pipes

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
WW01 Invention patent application withdrawn after publication

Application publication date: 20180824

WW01 Invention patent application withdrawn after publication