CN205860827U - Spiral elliptical tube double pipe heat exchanger - Google Patents

Spiral elliptical tube double pipe heat exchanger Download PDF

Info

Publication number
CN205860827U
CN205860827U CN201620860678.1U CN201620860678U CN205860827U CN 205860827 U CN205860827 U CN 205860827U CN 201620860678 U CN201620860678 U CN 201620860678U CN 205860827 U CN205860827 U CN 205860827U
Authority
CN
China
Prior art keywords
tube
side fluid
spiral
heat exchanger
inner tube
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.)
Expired - Fee Related
Application number
CN201620860678.1U
Other languages
Chinese (zh)
Inventor
黄德斌
严晓晴
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.)
Foshan University
Original Assignee
Foshan 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 Foshan University filed Critical Foshan University
Priority to CN201620860678.1U priority Critical patent/CN205860827U/en
Application granted granted Critical
Publication of CN205860827U publication Critical patent/CN205860827U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

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

Abstract

The utility model discloses a kind of Spiral Elliptical Tube double pipe heat exchanger, including outer tube, it is placed in the interior inner tube with described outer coaxial tube of outer tube, and it is connected to drive end bearing bracket and the rear end cap at outer tube two ends, inner tube is respectively arranged at two ends with tube side fluid inlet and tube side fluid outlet and extends through drive end bearing bracket and rear end cap, outer tube be respectively arranged at two ends with tube side fluid flow to contrary shell side fluid inlet and shell side fluid outlet, said inner tube shape helically ellipticity, forms circular spiral cavity between inner tube and outer tube.In heat exchanger of the present utility model, the runner in ring-type spiraled cavity is in the shape of a spiral, by the effect of centrifugal force and periodic variation speed and direction when shell-side fluid is moved wherein, thus strengthen shell-side fluid radially mixing, enhance the turbulivity of shell-side fluid self, improve convection transfer rate, meanwhile, the screw of tube side fluid improves its turbulent extent, increasing the convection transfer rate in pipe, simple in construction is prone to unpick and wash and keep in repair.

Description

Spiral Elliptical Tube double pipe heat exchanger
Technical field
This utility model relates to heat-transfer equipment field, particularly to a kind of Spiral Elliptical Tube double pipe heat exchanger.
Background technology
Heat exchanger is to realize energy-conservation the setting of heat transmission between material between two or more fluid of different temperatures Standby, it is to make heat be passed to, by the fluid that temperature is higher, the fluid that temperature is relatively low, makes fluid temperature (F.T.) reach the index of flow specification, To meet the needs of process conditions, energy utilization rate can also be improved simultaneously, thus be widely used in HVAC, pressure vessel, in Water treatment facilities, the field such as chemical industry and oil, in current double pipe heat exchanger annular space liquid turbulence degree not thus convection current The coefficient of heat transfer is low, and the heat transfer coefficient causing double-tube heat exchanger total is low.
Utility model content
Task of the present utility model is to provide in a kind of inner tube helically ellipticity can make working fluid inner tube when moving and is subject to Centrifugal action and periodic variation speed and direction and improve convection transfer rate to solve the deficiencies in the prior art.
This utility model is achieved through the following technical solutions utility model purpose:
A kind of Spiral Elliptical Tube double pipe heat exchanger, including outer tube, is placed in the interior inner tube with described outer coaxial tube of outer tube, with And be connected to drive end bearing bracket and the rear end cap at outer tube two ends, inner tube be respectively arranged at two ends with tube side fluid inlet and tube side fluid outlet and Extend through drive end bearing bracket and rear end cap, outer tube be respectively arranged at two ends with tube side fluid flow to contrary shell side fluid inlet and shell Journey fluid issuing, said inner tube shape helically ellipticity, form circular spiral cavity between inner tube and outer tube.
Further, said inner tube is to utilize elliptical tube stamping die that pipe is struck out elliptical tube again elliptical tube to be twisted into spiral shell Rotation and helically ellipticity.
Further, said inner tube spiral torsional is 6 ~ 12:1 away from the ratio with base tube external diameter, and transverse with the ratio of short axle is 1.5 ~ 2.0:1.
Further, said inner tube and outer tube use any one or two kinds of materials in steel, copper, titanium.These materials all have There is preferable corrosion resistance can extend the service life of heat exchanger.
The Spiral Elliptical Tube double pipe heat exchanger that this utility model provides has the advantage that inner tube uses spiral oval Pipe, Spiral Elliptical Tube is first to be pressed into ellipse by pipe, then elliptical tube distortion is formed, forms helical flow path, and outer tube in pipe Between inner surface, inner tube outer surface and two end cap formed circular spiral cavity, the runner in circular spiral cavity in the shape of a spiral, shell By the effect of centrifugal force and periodic variation speed and direction when Cheng Liuti moves in circular spiral cavity, thus strengthen Shell-side fluid radially mixing, enhances the turbulivity of shell-side fluid self, improves convection transfer rate;Meanwhile, tube side fluid Screw improve its turbulent extent, increase the convection transfer rate in pipe, simple in construction is prone to unpick and wash and keep in repair.
Accompanying drawing explanation
Fig. 1 is the cross-sectional view of a kind of embodiment of this utility model;
Fig. 2 is the profile in Fig. 1 at A-A;
Wherein: 1 outer tube, 2 inner tubes, 3 drive end bearing bracket 4 rear end caps, 5 tube side fluid inlet, 6 tube side fluid Outlet, 7 shell side fluid inlet, 8 shell side fluid outlet, 9 circular spiral cavitys.
Detailed description of the invention
Below in conjunction with the accompanying drawings embodiment of the present utility model is described in further detail.
As shown in Figure 1 to Figure 2, a kind of Spiral Elliptical Tube double pipe heat exchanger, including outer tube 1, in being placed in outer tube 1 and outer tube 1 coaxial inner tube 2, and it is connected to drive end bearing bracket 3 and the rear end cap 4 at outer tube 1 two ends, inner tube 2 is respectively arranged at two ends with tube side fluid Entrance 5 and tube side fluid export 6 and extend through drive end bearing bracket 3 and rear end cap 4, and outer tube 1 is respectively arranged at two ends with and tube side fluid Flowing to contrary shell side fluid inlet 7 and shell side fluid outlet 8, inner tube 2 shape helically ellipticity, between inner tube 2 and outer tube 1 Form circular spiral cavity 9.Inner tube 2 is to utilize elliptical tube stamping die that pipe is struck out elliptical tube again elliptical tube to be twisted into spiral And helically ellipticity, in order to obtain preferable combination property (heat transfer and resistance), inner tube spiral torsional is away from the ratio with base tube external diameter Being 6 ~ 12:1, transverse is 1.5 ~ 2.0:1 with the ratio of short axle, and inner and outer tubes use stainless steel material, it is also possible to select casting Any one or two kinds of materials in ferrum, copper, titanium, pottery or glass.
Above-described is only embodiments more of the present utility model.For the person of ordinary skill of the art, On the premise of creating design without departing from this utility model, it is also possible to making some deformation and improvement, these broadly fall into this practicality Novel protection domain.

Claims (4)

1. a Spiral Elliptical Tube double pipe heat exchanger, including outer tube, is placed in the interior inner tube with described outer concentric tube of outer tube, and Being connected to drive end bearing bracket and the rear end cap at outer tube two ends, inner tube is respectively arranged at two ends with tube side fluid inlet and tube side fluid outlet and divides Do not run through drive end bearing bracket and rear end cap, outer tube be respectively arranged at two ends with tube side fluid flow to contrary shell side fluid inlet and shell side Fluid issuing, it is characterised in that: said inner tube shape helically ellipticity, form circular spiral cavity between inner tube and outer tube.
Spiral Elliptical Tube double pipe heat exchanger the most according to claim 1, it is characterised in that said inner tube is to utilize ellipse Pipe is struck out elliptical tube and elliptical tube is twisted into spiral again and helically ellipticity by pipe stamping die.
Spiral Elliptical Tube double pipe heat exchanger the most according to claim 1, it is characterised in that: said inner tube spiral torsional away from The ratio of base tube external diameter is 6 ~ 12:1, and transverse is 1.5 ~ 2.0:1 with the ratio of short axle.
Spiral Elliptical Tube double pipe heat exchanger the most according to claim 1, it is characterised in that: said inner tube and outer tube use Steel, cast iron, copper, any one or two kinds of materials of titanium.
CN201620860678.1U 2016-08-10 2016-08-10 Spiral elliptical tube double pipe heat exchanger Expired - Fee Related CN205860827U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201620860678.1U CN205860827U (en) 2016-08-10 2016-08-10 Spiral elliptical tube double pipe heat exchanger

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201620860678.1U CN205860827U (en) 2016-08-10 2016-08-10 Spiral elliptical tube double pipe heat exchanger

Publications (1)

Publication Number Publication Date
CN205860827U true CN205860827U (en) 2017-01-04

Family

ID=57657545

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201620860678.1U Expired - Fee Related CN205860827U (en) 2016-08-10 2016-08-10 Spiral elliptical tube double pipe heat exchanger

Country Status (1)

Country Link
CN (1) CN205860827U (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108225057A (en) * 2018-02-11 2018-06-29 佛山科学技术学院 A kind of concave surface heat exchanger tube double pipe heat exchanger
CN108332583A (en) * 2018-02-11 2018-07-27 佛山科学技术学院 A kind of axial notch heat exchanger tube double pipe heat exchanger
WO2018223296A1 (en) * 2017-06-07 2018-12-13 南京工业大学 Pipe-type mixer
CN109443051A (en) * 2018-11-20 2019-03-08 佛山科学技术学院 A kind of double pipe heat exchanger

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2018223296A1 (en) * 2017-06-07 2018-12-13 南京工业大学 Pipe-type mixer
CN108225057A (en) * 2018-02-11 2018-06-29 佛山科学技术学院 A kind of concave surface heat exchanger tube double pipe heat exchanger
CN108332583A (en) * 2018-02-11 2018-07-27 佛山科学技术学院 A kind of axial notch heat exchanger tube double pipe heat exchanger
CN109443051A (en) * 2018-11-20 2019-03-08 佛山科学技术学院 A kind of double pipe heat exchanger

Similar Documents

Publication Publication Date Title
CN205860827U (en) Spiral elliptical tube double pipe heat exchanger
CN206056350U (en) The double pipe heat exchanger of built-in helical ribbon
CN201306953Y (en) Heat exchanger
CN206073761U (en) Groove heat exchange tube
CN102564189A (en) Heat transfer pipe
CN203837550U (en) Discontinuous and bi-directional warping type heat exchange tube
CN103697740A (en) Inner petal-shaped irregular-shaped heat exchange tube
CN101349521A (en) Variable-pitch screw thread metal pipe
CN103424012A (en) Immersion type ring tube heat exchanger
CN203454864U (en) Jacketed pipe heat exchanger
CN207991332U (en) A kind of concave surface heat exchanger tube double pipe heat exchanger that interlocks
CN208059638U (en) A kind of axial notch heat exchanger tube double pipe heat exchanger
CN202692733U (en) Fin condensing pipe provided with liquid absorption core body
CN105571353A (en) Pin-fin spiral heat exchanger
CN202915742U (en) Tangential continuous spiral diversion winding pipe condenser
CN108332583A (en) A kind of axial notch heat exchanger tube double pipe heat exchanger
CN204574847U (en) A kind of Novel condenser
CN204329683U (en) A kind of pipe heat exchanger
CN208998599U (en) A kind of baffle formula coil heat exchanger
CN207907740U (en) A kind of concave surface heat exchanger tube double pipe heat exchanger
CN205300369U (en) Can conduct heat many planes spinning disk intensive to double -pipe heat exchanger
CN201407929Y (en) Large pore plate convergent-divergent tube efficient heat exchanger
CN203240927U (en) Conical heat exchanger
CN202442614U (en) Bushing type heat exchanger
CN207214863U (en) Bushing type micro-channel heat exchanger

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20170104

Termination date: 20170810