CN106482547A - Inside and outside Double helix is wandered about as a refugee heart separate type heat exchanger - Google Patents

Inside and outside Double helix is wandered about as a refugee heart separate type heat exchanger Download PDF

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Publication number
CN106482547A
CN106482547A CN201611079835.6A CN201611079835A CN106482547A CN 106482547 A CN106482547 A CN 106482547A CN 201611079835 A CN201611079835 A CN 201611079835A CN 106482547 A CN106482547 A CN 106482547A
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CN
China
Prior art keywords
inner tube
straight length
tube
double helix
inlet
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Withdrawn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
CN201611079835.6A
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Chinese (zh)
Inventor
王尊策
李森
闫月娟
徐艳
张井龙
孙丽丽
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Northeast Petroleum University
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Northeast Petroleum University
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Publication date
Application filed by Northeast Petroleum University filed Critical Northeast Petroleum University
Priority to CN201611079835.6A priority Critical patent/CN106482547A/en
Publication of CN106482547A publication Critical patent/CN106482547A/en
Withdrawn legal-status Critical Current

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Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D7/00Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D7/10Heat-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 one within the other, e.g. concentrically
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F1/00Tubular elements; Assemblies of tubular elements
    • F28F1/10Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses
    • F28F1/12Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element
    • F28F1/34Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element and extending obliquely
    • F28F1/36Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element and extending obliquely the means being helically wound fins or wire spirals

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  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Geometry (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)

Abstract

A kind of inside and outside Double helix is wandered about as a refugee heart separate type heat exchanger.Main purpose is to solve the problems, such as that cold and hot media for heat exchange efficiency is low, is particularly well-suited to the heat exchange of vehicle repair major medium.It is characterized in that:This device has inside and outside helical flow path double-layer structure, the inner tube of described straight length(4)In have an interior arm(2), it is fixed with one group of inner screwy fin around described interior arm(3), the inner tube of the outer rim of described inner screwy fin and described straight length(4)Inwall touch;Inner tube around described straight length(4)Outer wall be fixed with one group of external spiral piece(5), the outer rim of described external spiral piece and the outer tube of described straight length(6)Inwall touch.This kind of heat-exchanger rig can be realized Double helix stream inside and outside cold and hot medium and continuously flow after using cooperatively with medium accelerator, increase heat transfer temperature difference and heat exchange area, reduce vibration, effectively improve the heat transfer effect between medium.

Description

Inside and outside Double helix is wandered about as a refugee heart separate type heat exchanger
Technical field
The present invention relates to a kind of heat exchanger of the cold and hot media for heat exchange being applied to petroleum chemical industry, it is particularly well-suited to vapour-liquid Two-phase medium heat exchange.
Background technology
Heat exchanger as a kind of general thermal process equipment oil refining, chemical industry, environmental protection, generating, refrigeration, food processing, It is used widely in many industrial departments such as utilization of new energy resources.In view of heat exchanger important function in the industrial production, improve Its performance becomes the important channel of energy-saving and emission-reduction with improving its efficiency, will produce significantly Social and economic benef@.But, many Heat exchanger remains and does not enable abundant heat exchange between medium, heat exchange area is not high, between cold and hot medium heat transfer temperature difference less, The problem of heat exchange efficiency difference.
Content of the invention
In order to solve the technical problem being previously mentioned in background technology, the present invention provides a kind of inside and outside Double helix stream centrifugation Formula heat exchanger, this kind of heat exchanger can realize Double helix stream continuous stream inside and outside cold and hot medium after using cooperatively with medium accelerator Dynamic, increase heat transfer temperature difference and heat exchange area, reduce vibration, effectively improve the heat transfer effect between medium.
The technical scheme is that:Inside and outside this kind, Double helix is wandered about as a refugee heart separate type heat exchanger, connects including a pair of import and export Head and be sequentially connected with some straight lengths between the pair of inlet-outlet connector and some bend loss, described import and export connect Head, some straight lengths and some bend loss by outer tube nested with inner tube after composition, it is unique in that:Described straight length Have an interior arm in inner tube, be fixed with one group of inner screwy fin around described interior arm, the outer rim of described inner screwy fin with described The inwall of the inner tube of straight length touches;Outer wall around the inner tube of described straight length is fixed with one group of external spiral piece, described outer spiral shell The outer rim of blade is touched with the inwall of the outer tube of described straight length.
Further, it is designed with shoulder, right in the inner tube of inlet-outlet connector and in the annular space of inner tube and outer tube formation Answer tube chamber shunting cylinder and outer lumen shunting torus, said inner tube chamber shunting cylinder and outer tube in fixing respectively at shoulder Uniformly have, on chamber shunting torus, the hole passing through for medium.
Additionally, the inwall of the inner tube of described straight length has the thread groove screwing in for inner screwy fin, the spiral of inner screwy fin Angle and pitch are consistent with the helical angle of corresponding thread groove and pitch, with realize the screw-in of described inner screwy fin, fixation with close Envelope;The inwall of the outer tube of described straight length also opens thread groove, the helical angle of described external spiral piece and the spiral shell screwing in for external spiral piece Away from consistent with the helical angle and pitch of corresponding thread groove, to realize described external spiral piece screw-in, fixation and sealing;Described interior, Difference range between 20 °~40 °, between the width of corresponding thread groove and the thickness of flight for the liter angle range of external spiral piece Between 5 millimeters~15 millimeters.
In addition, the outer outer tube layer in described inlet-outlet connector, some straight lengths and some bend loss all has a heat-insulation layer.
Further, using between the inwall of outer tube and the outer wall of inner tube as heating medium flowing external spiral runner, The inner chamber of inner tube is the internal coiling runner of cooling media flow, the inlet-outlet connector conduct of one of the pair of inlet-outlet connector Hot import and cold outlet, another inlet-outlet connector then as heat outlet and cold import so that cold and hot two media realize inverse Stream flowing
The present invention has the advantages that:The present invention is adopted as internal coiling runner, external spiral runner double-layer structure, and thermal medium exists In external spiral runner, flowing, cold medium flow in internal coiling runner, and each self-forming spiral flow, due to cold and hot fluid medium So that the respective fluid media (medium) in internal and external screw runner produces temperature difference after heat exchange, and then lead to the difference of density, this difference Can increase further in the case of two-phase medium heat exchange.This allows for moving under produced centrifugal action in spiral flow, outward The part that in thermal medium in helical flow path, temperature is high, density is little, enthalpy is high to central motion, that is, is drawn close in outer wall of inner tube, interior spiral shell The part that in cold medium in rotation, temperature is low, density is big, enthalpy is low is moved to side wall, that is, draw close in inner tube wall, and then permissible Increase inner tube inside and outside wall heat transfer temperature difference, improve heat exchange efficiency.This kind of heat-exchanger rig can be realized inside and outside Double helix stream and continuously flow, Increase heat transfer temperature difference and heat exchange area, reduce vibration, effectively improve the heat transfer effect between medium.Additionally, dividing on connector unit Stream device, can simultaneously work as shunting vibration damping and centralizing function, and the heat-insulation layer coating on outer outer tube layer, minimizing can be played Thermal loss and safe effect.
Brief description:
Fig. 1 is the flow direction schematic diagram of cold and hot two media during present invention application.
Fig. 2 is the configuration schematic diagram of the present invention.
Fig. 3 is inner screwy fin structural representation of the present invention.
Fig. 4 is external spiral chip architecture schematic diagram of the present invention.
Fig. 5 is inner and outer pipe structural representation of the present invention.
Fig. 6 is the structural representation of flight of the present invention and heat exchanger tube assembling.
Fig. 7 is the assembling structure schematic diagram of Fig. 3, Fig. 4, Fig. 5, Fig. 9.
Fig. 8 is that heat exchange unit of the present invention is connected generalized section with interior coupling.
Fig. 9 is into and out a mouthful joint design sectional view.
In figure 1- inlet-outlet connector, arm in 2-, 3- inner screwy fin, 4- inner tube, 5- external spiral piece, 6- outer tube, 7- inner tube Joint, 8- outer tube joint, 9- shunting body, 10- heat-insulation layer.
Specific embodiment:
The invention will be further described below in conjunction with the accompanying drawings:
By shown in Fig. 1 to Fig. 9, inside and outside this kind, Double helix is wandered about as a refugee heart separate type heat exchanger, including a pair of inlet-outlet connector 1 and suitable The secondary some straight lengths being connected between the pair of inlet-outlet connector and some bend loss, described inlet-outlet connector, Ruo Ganzhi Pipeline section and some bend loss by outer tube 6 nested with inner tube 4 after constitute, it is unique in that:In the inner tube 4 of described straight length There is an interior arm 2, be fixed with one group of inner screwy fin 3, the outer rim of described inner screwy fin and described straight tube around described interior arm The inwall of the inner tube 4 of section touches;Outer wall around the inner tube 4 of described straight length is fixed with one group of external spiral piece 5, described external spiral The outer rim of piece is touched with the inwall of the outer tube 6 of described straight length.
Further, it is designed with shoulder, right in the inner tube of inlet-outlet connector 1 and in the annular space of inner tube and outer tube formation Answer tube chamber shunting cylinder and outer lumen shunting torus, said inner tube chamber shunting cylinder and outer tube in fixing respectively at shoulder Uniformly have, on chamber shunting torus, the hole passing through for medium.Described shunting body as shown in Figure 2 and Figure 9, plays shunting vibration damping With centralizing function, require the area of passage of part flow arrangement to be greater than the area of passage between flight simultaneously, medium so can be made to exist In flight, abundant eddy flow, does not interspace, and strengthens heat transfer.
In addition, the inwall of the inner tube 4 of described straight length has the thread groove screwing in for inner screwy fin 3, the spiral shell of inner screwy fin 3 Swing angle and pitch are consistent with the helical angle of corresponding thread groove and pitch, with realize the screw-in of described inner screwy fin, fixation with Sealing;The inwall of the outer tube 6 of described straight length also opens the thread groove screwing in for external spiral piece 5, the helical angle of described external spiral piece Consistent with the helical angle of corresponding thread groove and pitch with pitch, to realize described external spiral piece screw-in, fixation and sealing;Described Difference between 20 °~40 °, between the width of corresponding thread groove and the thickness of flight for the liter angle range of inside and outside flight Scope is between 5 millimeters~15 millimeters.
Additionally, the outer outer tube layer of described inlet-outlet connector, some straight lengths and some bend loss all has a heat-insulation layer 10.
It is the external spiral runner in flowing for the heating medium between the outer wall of the inwall of outer tube 6 and inner tube 4, the inner chamber of inner tube 4 For the internal coiling runner of cooling media flow, one of the pair of inlet-outlet connector 1 inlet-outlet connector as hot import and Cold outlet, another inlet-outlet connector then exports and cold import as heat, so that cold and hot two media realizes counter-current flow.
During use, the specific work process of this device is as follows:
After using cooperatively with medium accelerator, cold and hot medium enters heat exchanger from inlet-outlet connector, and all has certain initial velocity Degree.Thermal medium enters external spiral runner, flowing of spinning in outer flight by part flow arrangement, and cold medium passes through part flow arrangement Enter internal coiling runner, flowing of spinning in inner screwy fin, two media realizes counter-current flow.So, by helical flow Centrifugal action, the part that in thermal medium in external spiral piece, temperature is high, density is little, enthalpy is high is drawn close to center, that is, draw close in inner tube Outer wall, the part that in the cold medium in internal coiling, temperature is low, density is big, enthalpy is low is drawn close to side wall, that is, draw close in inner tube wall, Inner tube inside and outside wall heat transfer temperature difference so can be increased, be conducive to cold and hot medium fully to carry out heat exchange, effectively improve heat exchange effect Rate.After the completion of heat exchange, cold and hot medium flows out from outlet connection.

Claims (5)

1. a kind of inside and outside Double helix is wandered about as a refugee heart separate type heat exchanger, including a pair of inlet-outlet connector(1)And be sequentially connected with institute State some straight lengths between a pair of inlet-outlet connector and some bend loss, described inlet-outlet connector, some straight lengths and some Bend loss is by outer tube(6)And inner tube(4)Nesting after constitute it is characterised in that:The inner tube of described straight length(4)In have in one Arm(2), it is fixed with one group of inner screwy fin around described interior arm(3), the outer rim of described inner screwy fin and described straight length Inner tube(4)Inwall touch;Inner tube around described straight length(4)Outer wall be fixed with one group of external spiral piece(5), described outer spiral shell The outer rim of blade and the outer tube of described straight length(6)Inwall touch.
2. inside and outside Double helix according to claim 1 wander about as a refugee heart separate type heat exchanger it is characterised in that:In inlet-outlet connector (1)Inner tube in and the annular space that formed of inner tube and outer tube in be designed with shoulder, fix respectively at corresponding shoulder in tube chamber shunting Uniformly have for being situated between on cylinder and outer lumen shunting torus, said inner tube chamber shunting cylinder and outer lumen shunting torus The hole that matter is passed through.
3. inside and outside Double helix according to claim 2 wander about as a refugee heart separate type heat exchanger it is characterised in that:Described straight length Inner tube(4)Inwall have and supply inner screwy fin(3)The thread groove screwing in, inner screwy fin(3)Helical angle and pitch and corresponding spiral shell The helical angle of groove and pitch are consistent, to realize screw-in, fixation and the sealing of described inner screwy fin;Outside described straight length Pipe(6)Inwall also open for external spiral piece(5)Thread groove, the helical angle of described external spiral piece and pitch and the corresponding screw thread screwing in The helical angle of groove is consistent with pitch, to realize screw-in, fixation and the sealing of described external spiral piece;The liter of described inside and outside flight , between 20 °~40 °, difference range between the width of corresponding thread groove and the thickness of flight is 5 millimeters~15 for angle range Between millimeter.
4. inside and outside Double helix according to claim 3 wander about as a refugee heart separate type heat exchanger it is characterised in that:Described import and export connect The outer outer tube layer of head, some straight lengths and some bend loss all has a heat-insulation layer (10).
5. inside and outside Double helix according to claim 4 wander about as a refugee heart separate type heat exchanger it is characterised in that:Outer tube(6)Interior Wall and inner tube(4)Outer wall between for heating medium flowing external spiral runner, inner tube(4)Inner chamber be cooling media flow Internal coiling runner, the pair of inlet-outlet connector(1)One of inlet-outlet connector as hot import and cold outlet, another Inlet-outlet connector then exports and cold import as heat, so that cold and hot two media realizes counter-current flow.
CN201611079835.6A 2016-11-30 2016-11-30 Inside and outside Double helix is wandered about as a refugee heart separate type heat exchanger Withdrawn CN106482547A (en)

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CN201611079835.6A CN106482547A (en) 2016-11-30 2016-11-30 Inside and outside Double helix is wandered about as a refugee heart separate type heat exchanger

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Application Number Priority Date Filing Date Title
CN201611079835.6A CN106482547A (en) 2016-11-30 2016-11-30 Inside and outside Double helix is wandered about as a refugee heart separate type heat exchanger

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Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107764099A (en) * 2017-10-30 2018-03-06 清华大学 Sleeve pipe enhanced heat exchange unit block and penetrate mixing rotational-flow high-efficient double pipe heat exchanger
KR101924975B1 (en) 2017-06-26 2018-12-04 (주)코스 Double tube for generatibg cyclone
JP2020012619A (en) * 2018-07-20 2020-01-23 株式会社ヴァレオジャパン Double-pipe heat exchanger
CN110849179A (en) * 2019-10-12 2020-02-28 西安交通大学 High-temperature high-pressure heat exchanger with temperature compensation and machining method thereof
CN112944959A (en) * 2021-03-09 2021-06-11 格力电器(武汉)有限公司 Rotational flow disturbance device and heat exchange tube structure

Citations (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02265564A (en) * 1989-04-07 1990-10-30 Ube Ind Ltd Blood heat exchanger
CN2510814Y (en) * 2001-12-26 2002-09-11 台湾雷德斯减废科技有限公司 Heat exchanger
CN2795782Y (en) * 2005-03-31 2006-07-12 广州百晟空调配件有限公司 High efficiency sleeve type heat exchanger
CN2828706Y (en) * 2005-09-15 2006-10-18 葛建民 Vortex double-pipe heat exchanger
CN101210783A (en) * 2006-12-28 2008-07-02 株式会社科倍可菱材料 Heat exchanger
CN201476660U (en) * 2009-08-14 2010-05-19 陈禺伶 Internal and external spiral fin heat transfer tube
CN101738109A (en) * 2009-11-30 2010-06-16 江秋良 Spiral-tube heat exchanger
CN201697505U (en) * 2010-05-05 2011-01-05 赵常铭 Bushing type spiral heat exchanger
CN103115516A (en) * 2011-11-16 2013-05-22 江苏大自然电器标牌厂 Integral spiral finned tube
CN104501628A (en) * 2014-12-24 2015-04-08 高台县聚合热力有限责任公司 Double-spiral flat type heat exchange unit and double-spiral flat type heat exchanger
CN206208071U (en) * 2016-11-30 2017-05-31 东北石油大学 Inside and outside double helix is wandered about as a refugee heart separate type heat exchanger

Patent Citations (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02265564A (en) * 1989-04-07 1990-10-30 Ube Ind Ltd Blood heat exchanger
CN2510814Y (en) * 2001-12-26 2002-09-11 台湾雷德斯减废科技有限公司 Heat exchanger
CN2795782Y (en) * 2005-03-31 2006-07-12 广州百晟空调配件有限公司 High efficiency sleeve type heat exchanger
CN2828706Y (en) * 2005-09-15 2006-10-18 葛建民 Vortex double-pipe heat exchanger
CN101210783A (en) * 2006-12-28 2008-07-02 株式会社科倍可菱材料 Heat exchanger
CN201476660U (en) * 2009-08-14 2010-05-19 陈禺伶 Internal and external spiral fin heat transfer tube
CN101738109A (en) * 2009-11-30 2010-06-16 江秋良 Spiral-tube heat exchanger
CN201697505U (en) * 2010-05-05 2011-01-05 赵常铭 Bushing type spiral heat exchanger
CN103115516A (en) * 2011-11-16 2013-05-22 江苏大自然电器标牌厂 Integral spiral finned tube
CN104501628A (en) * 2014-12-24 2015-04-08 高台县聚合热力有限责任公司 Double-spiral flat type heat exchange unit and double-spiral flat type heat exchanger
CN206208071U (en) * 2016-11-30 2017-05-31 东北石油大学 Inside and outside double helix is wandered about as a refugee heart separate type heat exchanger

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101924975B1 (en) 2017-06-26 2018-12-04 (주)코스 Double tube for generatibg cyclone
CN107764099A (en) * 2017-10-30 2018-03-06 清华大学 Sleeve pipe enhanced heat exchange unit block and penetrate mixing rotational-flow high-efficient double pipe heat exchanger
CN107764099B (en) * 2017-10-30 2019-09-17 清华大学 Casing enhanced heat exchange unit block and penetrate mixing rotational-flow high-efficient double pipe heat exchanger
JP2020012619A (en) * 2018-07-20 2020-01-23 株式会社ヴァレオジャパン Double-pipe heat exchanger
CN110849179A (en) * 2019-10-12 2020-02-28 西安交通大学 High-temperature high-pressure heat exchanger with temperature compensation and machining method thereof
CN112944959A (en) * 2021-03-09 2021-06-11 格力电器(武汉)有限公司 Rotational flow disturbance device and heat exchange tube structure
CN112944959B (en) * 2021-03-09 2022-05-24 格力电器(武汉)有限公司 Rotational flow disturbance device and heat exchange tube structure

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Application publication date: 20170308

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