CN206235218U - Outer ripple heat exchange of heat pipe and sea water desalinating unit - Google Patents
Outer ripple heat exchange of heat pipe and sea water desalinating unit Download PDFInfo
- Publication number
- CN206235218U CN206235218U CN201621235236.4U CN201621235236U CN206235218U CN 206235218 U CN206235218 U CN 206235218U CN 201621235236 U CN201621235236 U CN 201621235236U CN 206235218 U CN206235218 U CN 206235218U
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- Prior art keywords
- heat pipe
- pipe
- outer ripple
- ripple heat
- heat
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- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A20/00—Water conservation; Efficient water supply; Efficient water use
- Y02A20/124—Water desalination
Abstract
The utility model provides a kind of outer ripple heat exchange of heat pipe and sea water desalinating unit, the technical field for being related to heat exchange to evaporate, including outer ripple heat pipe, sleeve pipe, housing and dividing plate；The housing is separated into vaporization chamber and condensation chamber by dividing plate；Outer ripple heat pipe two ends closure, outer ripple heat pipe is placed on enclosure interior, and outer ripple heat pipe is passed through dividing plate, is supported by the external ripple heat pipe of dividing plate, outer ripple heat pipe is divided into evaporation tube and condenser pipe by dividing plate, and evaporation tube and condenser pipe are separately positioned in vaporization chamber and condensation chamber；On outer ripple heat pipe, sleeve pipe passes through dividing plate to casing pipe sleeve, and sleeve pipe does not contact setting with outer ripple heat pipe, and the gap between sleeve pipe and outer ripple heat pipe forms heat exchanging chamber；Outer ripple heat pipe is provided with ripple outside pipe, and ripple includes two kinds of forms：Lateral-cut and longitudinal corrugation；The technical problem of desalting process fouling of evaporator, outer ripple heat pipe are solved because its outer ripple struction, the heat transfer efficiency of evaporator is improved, it is less scaling in evaporation process.
Description
Technical field
The utility model is related to technical field of heat exchangers, more particularly, to a kind of outer ripple heat exchange of heat pipe and desalinization
Device.
Background technology
Hot pipe technique is the phase-change heat transfer technology in a kind of closed chamber, using quite extensive.In field of seawater desalination, although
Heat pipe sea water desalination device is used for the research of the marine sea water desalination device, but still the outer fouling of pipe of evaporation section cannot have been avoided
Phenomenon occurs.
Bellows heat-exchange element is a kind of high efficient heat exchanging element that last century the mid-1970s occur.It is straight for identical nominal
The bellows and light pipe in footpath, in same traffic, the flow resistance coefficient and pressure drop ratio light pipe of bellows are big, but bellows has
The advantage that scale velocity is slow, induction period is long, dirtiness resistance asymptotic value is small, and bellows has good reinforcing before and after fouling
Heat transfer property.Bellows processing is simple, cheap for manufacturing cost, can significantly strengthen in the case of pump power consumption is not increased
The heat-transfer effect of fluid.
Heat exchanger, is the equipment that the partial heat of hot fluid is passed to cold fluid, also known as heat exchanger.
It is poor that tube-sheet heat exchanger of the prior art, wherein shortcoming are followed successively by sealing property, is not suitable for volatile, easy
Combustion, explosive and poisonous medium, structure are more complicated, and the sealing situation of floating head checks that cleaning is because of pipe into U in difficult, pipe during operation
Shape and it is more difficult, the replacing that heat exchanger tube is enclosed in tube bank is more difficult, and the intrinsic frequency of tube bank is relatively low easy to be evoked vibration, shell side and cannot enter
Row mechanical cleaning, shell side checks difficult, can produce larger thermal (temperature difference) stress when between housing and pipe without temperature difference compensation element, i.e.,
The temperature difference need to use the compensating element,s such as expansion joint or bellows to reduce thermal (temperature difference) stress when larger.
So, how to solve fouling and heat conduction efficiency is those skilled in the art's problem demanding prompt solution at this stage.
Utility model content
The purpose of this utility model is to provide a kind of outer ripple heat exchange of heat pipe and sea water desalinating unit, to alleviate Jie
The technical problem of the fouling that matter occurs in evaporation and heat-exchange process.
To achieve the above object, the utility model provides following technical scheme：
In a first aspect, the utility model provides a kind of outer ripple heat exchange of heat pipe, including：Outer ripple heat pipe, sleeve pipe, housing
And dividing plate；
The housing is separated into vaporization chamber and condensation chamber by the dividing plate；
The outer ripple heat pipe two ends closure, the outer ripple heat pipe is placed on the enclosure interior, the outer ripple heat
Through the dividing plate, the outer ripple heat pipe is divided into evaporation tube and condenser pipe to pipe by the dividing plate, the evaporation tube and described cold
Solidifying pipe is separately positioned in the vaporization chamber and the condensation chamber；
Described sleeve pipe is sleeved on the outer ripple heat pipe, described sleeve pipe pass through the dividing plate, and described sleeve pipe with it is described
Outer ripple heat pipe does not contact setting, and the gap between described sleeve pipe and the outer ripple heat pipe forms heat exchanging chamber.
Further, the outer ripple heat pipe is supported by the dividing plate.
Further, the outer ripple heat pipe is provided with two kinds of ripples outside pipe：Lateral-cut and longitudinal corrugation.
Further, the lateral-cut includes several equidistant ripple bars, and adjacent corrugations bar be arranged in parallel, and with outer ripple
Heat pipe axial direction is parallel；
The longitudinal corrugation includes several equidistant ripple bars, and adjacent corrugations bar be arranged in parallel, and with outer ripple heat pipe axial direction
Direction is vertical.
Further, it is provided with heat transfer medium in the outer ripple heat pipe.
Further, described sleeve pipe and the outer ripple heat pipe are in triangular distribution on the dividing plate.
Further, described sleeve pipe and the outer ripple heat pipe are set in parallel in the housing.
Further, described sleeve pipe is provided with leakage fluid dram, and described sleeve pipe is provided with ripple.
Further, charging aperture and discharging opening are provided with outside the vaporization chamber；Feed liquor is provided with outside the condensation chamber
Mouth and liquid outlet.
Second aspect, the utility model is provided in also providing a kind of sea water desalinating unit, including distributor and first aspect
Any one outer ripple heat exchange of heat pipe.
The outer ripple heat exchange of heat pipe and sea water desalinating unit that the utility model is provided have the advantages that：
A kind of outer ripple heat exchange of heat pipe provided using the utility model, by being provided with dividing plate on housing, shell
Body is divided into two parts, respectively vaporization chamber and condensation chamber, and is exchanged heat by the outer ripple heat pipe set in heat exchanger,
Outer ripple heat pipe is because the outer ripple struction of its outer surface, can greatly improve the heat transfer efficiency of evaporator, in evaporation process not
Easy fouling；The quantity of outer ripple heat pipe and the number of heat exchanger can be arranged as required to, it is possible to increase the evaporation capacity of liquid, improve and steam
Hair efficiency；Not only there is separation in heat exchanger by setting this simple structure that dividing plate is separated, dividing plate in heat exchanger
Effect, while serving the effect of the support of external ripple heat pipe.The outer ripple heat pipe of the antiscale is used for desalinization, not only can be big
Amplitude reduces the construction investment of taking and discharging and pretreatment, reduces operating cost, and for after desalination concentrated seawater application provide height
The raw material of concentration, it is to avoid the influence that the direct discharge into sea of concentrated seawater is likely to result in marine ecology, will produce comprehensive benefit, drop
The integrated cost of low desalinization.
The sea water desalinating unit provided using the utility model, distributor is provided with by face on heat exchangers, so that
Into the seawater in vaporization chamber be uniformly distributed being evaporated, the steam of generation be condensed into needed for product-fresh water,
And concentrated seawater out, can need to enter in next effect heat exchanger according to production, it is evaporated.
Brief description of the drawings
In order to illustrate more clearly of the utility model specific embodiment or technical scheme of the prior art, below will be right
The accompanying drawing to be used needed for specific embodiment or description of the prior art is briefly described, it should be apparent that, describe below
In accompanying drawing be some implementation methods of the present utility model, for those of ordinary skill in the art, do not paying creativeness
On the premise of work, other accompanying drawings can also be obtained according to these accompanying drawings.
The outer ripple heat exchange of heat pipe structural representation that Fig. 1 is provided for the utility model embodiment；
The longitudinal corrugation main view of the outer ripple heat pipe of the outer ripple heat exchange of heat pipe that Fig. 2 is provided for the utility model embodiment
Figure；
The longitudinal corrugation side-looking of the outer ripple heat pipe of the outer ripple heat exchange of heat pipe that Fig. 3 is provided for the utility model embodiment
Figure；
The lateral-cut main view of the outer ripple heat pipe of the outer ripple heat exchange of heat pipe that Fig. 4 is provided for the utility model embodiment
Figure；
The lateral-cut side-looking of the outer ripple heat pipe of the outer ripple heat exchange of heat pipe that Fig. 5 is provided for the utility model embodiment
Figure.
Icon：The outer ripple heat pipes of 1-；11- evaporation tubes；12- condenser pipes；13- lateral-cuts；14- longitudinal corrugations；2- sleeve pipes；21-
Heat exchanging chamber；22- leakage fluid drams；3- housings；31- vaporization chambers；311- charging apertures；312- discharging openings；32- condensation chambers；321- inlets；
322- liquid outlets；4- dividing plates.
Specific embodiment
The technical solution of the utility model is clearly and completely described below in conjunction with accompanying drawing, it is clear that described
Embodiment is a part of embodiment of the utility model, rather than whole embodiments.Based on the embodiment in the utility model, this
The every other embodiment that field those of ordinary skill is obtained under the premise of creative work is not made, belongs to this practicality
Novel protected scope.
It is term " " center ", " on ", D score, "left", "right", " perpendicular, it is necessary to explanation in description of the present utility model
Directly ", the orientation or position relationship of the instruction such as " level ", " interior ", " outward " are, based on orientation shown in the drawings or position relationship, to be only
Described with simplified for the ease of description the utility model, must had rather than the device or element for indicating or implying meaning specific
Orientation, with specific azimuth configuration and operation, therefore it is not intended that to limitation of the present utility model.Additionally, term " the
One ", " second ", " the 3rd " are only used for describing purpose, and it is not intended that indicating or implying relative importance.
, it is necessary to explanation, unless otherwise clearly defined and limited, term " is pacified in description of the present utility model
Dress ", " connected ", " connection " should be interpreted broadly, for example, it may be fixedly connected, or be detachably connected, or integratedly
Connection；Can mechanically connect, or electrically connect；Can be joined directly together, it is also possible to be indirectly connected to by intermediary,
Can be two connections of element internal.For the ordinary skill in the art, above-mentioned art can be understood with concrete condition
Concrete meaning of the language in the utility model.
Specific embodiment of the present utility model is described in detail below in conjunction with accompanying drawing.It should be appreciated that herein
Described specific embodiment is merely to illustrate and explains the utility model, is not limited to the utility model.
The outer ripple heat exchange of heat pipe structural representation that Fig. 1 is provided for the utility model embodiment；
The longitudinal corrugation main view of the outer ripple heat pipe of the outer ripple heat exchange of heat pipe that Fig. 2 is provided for the utility model embodiment
Figure；
The longitudinal corrugation side-looking of the outer ripple heat pipe of the outer ripple heat exchange of heat pipe that Fig. 3 is provided for the utility model embodiment
Figure；
The lateral-cut main view of the outer ripple heat pipe of the outer ripple heat exchange of heat pipe that Fig. 4 is provided for the utility model embodiment
Figure；
The lateral-cut side-looking of the outer ripple heat pipe of the outer ripple heat exchange of heat pipe that Fig. 5 is provided for the utility model embodiment
Figure.
Fig. 1, Fig. 2, Fig. 3, Fig. 4 and Fig. 5 are refer to, below in conjunction with the external wave that accompanying drawing is provided the utility model embodiment
Line heat exchange of heat pipe elaborates.
The embodiment of the utility model first aspect provides a kind of outer ripple heat exchange of heat pipe, including：
Outer ripple heat pipe 1, sleeve pipe 2, housing 3 and dividing plate 4；
Housing 3 is separated into vaporization chamber 31 and condensation chamber 32 by dividing plate 4；
The outer two ends of ripple heat pipe 1 closure, outer ripple heat pipe 1 is placed on inside housing 3, and outer ripple heat pipe 1 passes through dividing plate 4,
It is supported by the external ripple heat pipe 1 of dividing plate 4,1 point by outer ripple heat pipe of dividing plate 4 is evaporation tube 11 and condenser pipe 12, evaporation
Pipe 11 and condenser pipe 12 are separately positioned in vaporization chamber 31 and condensation chamber 32；
Sleeve pipe 2 is sleeved on outer ripple heat pipe 1, and sleeve pipe 2 passes through dividing plate 4, and sleeve pipe 2 not to be contacted with outer ripple heat pipe 1 and set
Put, the gap between sleeve pipe 2 and outer ripple heat pipe 1 forms heat exchanging chamber 21；
Outer ripple heat pipe 1 is provided with ripple outside pipe, and ripple includes two kinds of forms：Lateral-cut 13 and longitudinal corrugation 14.
It should be noted that liquid enter heat exchanger when, fluid liquid film along it is continuous alternately wavy surface by upper
And during lower flowing, fluid thinning of liquid film, speed reduction at crest, thickness increase, the speed of fluid liquid film at trough
Increase, this can be mixed liquid film internal liquid and be produced additional disturbance so as to wash away the boundary layer of fluid, both be increased
The turbulence of fluid is thinned boundary layer again, so as to enhance heat transfer.
Corresponding corrugated surface not only increases heat transfer area outside the pipe of outer ripple heat pipe 1 simultaneously, also increases disturbance, promotees
Condensate film is flowed down rapidly, reduce liquid-film resistance, significantly improve heat-transfer effect.
Because outer ripple heat pipe 1 is full arc structure, and tube wall is thin, outer ripple heat pipe 1 is turned into full length of tube model
There is axial stretching ability and full elasticity in enclosing.It can the antiscale in terms of two：
One, there is no local-laminar, i.e. liquid under very low flow velocity in turbulence state in wholecircle arc elasticity system, have to tube wall
There is comprehensive flushing action, dielectric deposition chance seldom, fully extends the induction period of fouling；
Two, in thermal shock, elastic deformation can all occur in whole arc surfaces of bellows, and each locally has curvature to become
Change, even if the dirty layer of bellows has been formed, the flexible of it can also force dirty slabbing exoneration to fall, and realize the effect of automatic desludging.
It should be noted that when steam or hot material is entered from the charging aperture 311 of heat exchanger vaporization chamber 31, while heat transfer
To outward corrugated tube, the heat transfer medium in outer ripple heat pipe 1 is changed into gas by heat exchange from liquid, due to gas mobility more
By force, so being filled with gaseous heat transfer medium inside whole outer ripple heat pipe 1；The steam entered from vaporization chamber 31 cools down and becomes
From the discharging opening 312 of vaporization chamber 31 out, above-mentioned series reaction is in heat exchanger vaporization chamber 31 for condensed water or indirect steam
Inside carry out.
Needs are evaporated or the cold medium that exchange heat is by the entrance condensation chamber 32 of inlet 321, by with condensation chamber 32
The interior outer ripple heat pipe 1 of a part is that condenser pipe 12 is contacted, so as to the process for being evaporated or exchanging heat.
Specifically, the outer ripple struction of outer its uniqueness of ripple heat pipe 1 has 14 two kinds of lateral-cut 13 and longitudinal corrugation, lateral-cut 13
Including several equidistant ripple bars, adjacent corrugations bar be arranged in parallel, and parallel with the outer axial direction of ripple heat pipe 1；Longitudinal corrugation 14
Including several equidistant ripple bars, adjacent corrugations bar be arranged in parallel, and vertical with the outer axial direction of ripple heat pipe 1.Ripple bar is high
It is 1mm-3mm to spend, specially：1mm、2mm、3mm.
In view of in desalinization, the corrosivity of concentrated seawater, the outer material of ripple heat pipe 1 selects to be titanium.Titanium is most useful
Two characteristics are, highest strength-to-weight ratio in corrosion resistance, and metal.Titanium in the state of non-alloyed, the intensity of titanium
It is identical with some steel, but weight is also lighter by 45% than steel.
Because the heat transfer area of outer ripple heat pipe 1 is smaller, so that heat exchange efficiency is relatively low, so in order to increase heat transfer area,
Sleeve pipe 2 is cased with outside outer ripple heat pipe 1, gap forms heat exchanging chamber 21 between sleeve pipe 2 and outer ripple heat pipe 1, in order to more favourable
In the heat exchange and circulation of the fluid in heat exchanging chamber 21, the bottom of sleeve pipe 2 is provided with leakage fluid dram 22, so as to increase the flowing of fluid.
The size of heat exchanging chamber 21 is configured also according to the viscosity and temperature of fluid.
In view of fouling, sleeve pipe 2 is provided with ripple, above-mentioned bellows-shaped can be transverse wave and longitudinal ripple, or
The ripple that person is at an angle of with the axial direction of sleeve pipe 2, angle can be 30 °, 45 °, 60 °.
Additionally, sleeve pipe 2 and outer ripple heat pipe 1 are in triangular distribution on dividing plate 4.Can be arranged for equilateral triangle, also may be used
Think corner triangular pitch.
The distribution of sleeve pipe 2 and outer ripple heat pipe 1 on dividing plate 4, is done a downward by the difference of the property according to treatment fluid
Whole, equilateral triangle arrangement has following characteristics：It is most universal, stringing is more, sound and vibration is small, extratubal fluid disturbance is big, conduct heat, but be difficult clearly
Wash；Corner triangle has following characteristics:Easy cleaning, but heat-transfer effect is not so good as equilateral triangle.
, to be detachably connected, such connected mode makes for above-mentioned outer ripple heat pipe 1 and the connection between sleeve pipe 2 and dividing plate 4
Obtain whole equipment in use, any part goes wrong can be individually replaced part of damage, so as to save
Cost.
Dividing plate 4 not only serves and heat exchanger is separated into vaporization chamber 31 and the two spaces of condensation chamber 32 here, while right
Outer ripple heat pipe 1 and sleeve pipe 2 serve the effect of support, in order to ensure the absolute cut-off of vaporization chamber 31 and condensation chamber 32, every
Sealant is provided with around plate 4, makes vaporization chamber 31 and the two spaces of condensation chamber 32 completely isolated, so as to ensure that the effect of heat exchange
The degree of purity of rate and heat transferring medium.
Specifically, sleeve pipe 2 and outer ripple heat pipe 1 are set in parallel in the housing 3.
Heat exchange efficiency heat exchanging device in heat exchanger it is critical that, in order to increase heat exchange efficiency, changed in outer ripple heat pipe 1
Agitating device is provided with hot device.
Above-mentioned agitating device can have multiple choices mode, such as：
Mode one, above-mentioned agitating device can include：Stirring rod, stirring rod bottom is provided with impeller blade, impeller blade number
Amount at least two, stirring rod upper end is connected with motor, and agitating device is separately positioned on the He of vaporization chamber 31 of outer ripple heat pipe 1
In condensation chamber 32.
Mode two, above-mentioned agitating device can include：Stirring rod, stirring rod bottom is provided with square department, in stirring rod
End is connected with motor, and agitating device is separately positioned in the vaporization chamber 31 and condensation chamber 32 of outer ripple heat pipe 1.
Charging aperture 311 and discharging opening 312 are provided with outside vaporization chamber 31；The He of inlet 321 is provided with outside condensation chamber 32
Liquid outlet 322.
The embodiment of the utility model second aspect provides a kind of sea water desalinating unit (not shown), including above-mentioned
Outer ripple heat exchange of heat pipe in any one embodiment.
By taking desalinization as an example：Seawater enters from the condensation chamber of outer ripple heat exchange of heat pipe, by distributor by seawater
Sprayed, steam enters from the charging aperture of outer ripple heat exchange of heat pipe, and the evaporation tube with outer ripple heat pipe is exchanged heat, heat
The condenser pipe of outer ripple heat pipe is delivered to, condenser pipe is evaporated to seawater, concentrated seawater flows out from liquid outlet, fixed gas is from condensation
The fixed gas on device top mouthful out, as required fresh water.
A kind of outer ripple heat exchange of heat pipe provided using the utility model, by being provided with dividing plate on housing, shell
Body is divided into two parts, respectively vaporization chamber and condensation chamber, and is exchanged heat by the outer ripple heat pipe set in heat exchanger,
Outer ripple heat pipe is because the outer ripple struction of its outer surface, can greatly improve the heat transfer efficiency of evaporator, in evaporation process not
Easy fouling；The quantity of outer ripple heat pipe and the number of heat exchanger can be arranged as required to, it is possible to increase the evaporation capacity of liquid, improve and steam
Hair efficiency；Not only there is separation in heat exchanger by setting this simple structure that dividing plate is separated, dividing plate in heat exchanger
Effect, while serving the effect of the support of external ripple heat pipe.The outer ripple heat pipe of the antiscale is used for desalinization, not only can be big
Amplitude reduces the construction investment of taking and discharging and pretreatment, reduces operating cost, and for after desalination concentrated seawater application provide height
The raw material of concentration, it is to avoid the influence that the direct discharge into sea of concentrated seawater is likely to result in marine ecology, will produce comprehensive benefit, drop
The integrated cost of low desalinization.
The sea water desalinating unit provided using the utility model, distributor is provided with by face on heat exchangers, so that
Into the seawater in vaporization chamber be uniformly distributed being evaporated, the steam of generation be condensed into needed for product-fresh water,
And concentrated seawater out, can need to enter in next effect heat exchanger according to production, it is evaporated.
Finally it should be noted that：Various embodiments above is only used to illustrate the technical solution of the utility model, rather than it is limited
System；Although being described in detail to the utility model with reference to foregoing embodiments, one of ordinary skill in the art should
Understand：It can still modify to the technical scheme described in foregoing embodiments, or to which part or whole
Technical characteristic carries out equivalent；And these modifications or replacement, the essence of appropriate technical solution is departed from this practicality newly
The scope of each embodiment technical scheme of type.
Claims (10)
1. a kind of outer ripple heat exchange of heat pipe, it is characterised in that including：Outer ripple heat pipe (1), sleeve pipe (2), housing (3) and every
Plate (4)；
The housing (3) is separated into vaporization chamber (31) and condensation chamber (32) by the dividing plate (4)；
Outer ripple heat pipe (1) the two ends closure, the outer ripple heat pipe (1) is placed on the housing (3) inside, the external wave
The outer ripple heat pipe (1) is divided into evaporation tube (11) and condenser pipe by line heat pipe (1) through the dividing plate (4), the dividing plate (4)
(12), the evaporation tube (11) and the condenser pipe (12) are separately positioned on the vaporization chamber (31) and the condensation chamber (32)
In；
Described sleeve pipe (2) is sleeved on the outer ripple heat pipe (1), and described sleeve pipe (2) is through the dividing plate (4), and the set
Pipe (2) does not contact setting, the gap shape between described sleeve pipe (2) and the outer ripple heat pipe (1) with the outer ripple heat pipe (1)
Into heat exchanging chamber (21).
2. outer ripple heat exchange of heat pipe according to claim 1, it is characterised in that by the dividing plate (4) to described outer
Ripple heat pipe (1) is supported.
3. outer ripple heat exchange of heat pipe according to claim 1, it is characterised in that the outer ripple heat pipe (1) is outer in pipe
It is provided with two kinds of ripples：Lateral-cut (13) and longitudinal corrugation (14).
4. outer ripple heat exchange of heat pipe according to claim 3, it is characterised in that the lateral-cut (13) is including several
Equidistant ripple bar, adjacent corrugations bar be arranged in parallel, and parallel with outer ripple heat pipe axial direction；
The longitudinal corrugation (14) includes several equidistant ripple bars, and adjacent corrugations bar be arranged in parallel, and with outer ripple heat pipe axial direction
Direction is vertical.
5. outer ripple heat exchange of heat pipe according to claim 1, it is characterised in that set in the outer ripple heat pipe (1)
There is heat transfer medium.
6. outer ripple heat exchange of heat pipe according to claim 1, it is characterised in that described sleeve pipe (2) and the outer ripple
Heat pipe (1) is in triangular distribution on the dividing plate (4).
7. outer ripple heat exchange of heat pipe according to claim 5, it is characterised in that described sleeve pipe and the outer ripple heat pipe
It is set in parallel in the housing.
8. outer ripple heat exchange of heat pipe according to claim 1, it is characterised in that described sleeve pipe (2) is provided with leakage fluid dram
(22), described sleeve pipe (2) is provided with ripple.
9. outer ripple heat exchange of heat pipe according to claim 1, it is characterised in that charging is provided with outside the vaporization chamber
Mouth (311) and discharging opening (312)；Inlet (321) and liquid outlet (322) are provided with outside the condensation chamber.
10. a kind of sea water desalinating unit, it is characterised in that including the external wave any one of distributor and claim 1 to 9
Line heat exchange of heat pipe.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621235236.4U CN206235218U (en) | 2016-11-17 | 2016-11-17 | Outer ripple heat exchange of heat pipe and sea water desalinating unit |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621235236.4U CN206235218U (en) | 2016-11-17 | 2016-11-17 | Outer ripple heat exchange of heat pipe and sea water desalinating unit |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206235218U true CN206235218U (en) | 2017-06-09 |
Family
ID=58991433
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621235236.4U Withdrawn - After Issue CN206235218U (en) | 2016-11-17 | 2016-11-17 | Outer ripple heat exchange of heat pipe and sea water desalinating unit |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206235218U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106288896A (en) * | 2016-11-17 | 2017-01-04 | 河北工业大学 | Outer ripple heat exchange of heat pipe and sea water desalinating unit |
-
2016
- 2016-11-17 CN CN201621235236.4U patent/CN206235218U/en not_active Withdrawn - After Issue
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106288896A (en) * | 2016-11-17 | 2017-01-04 | 河北工业大学 | Outer ripple heat exchange of heat pipe and sea water desalinating unit |
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| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20170609 Effective date of abandoning: 20190305 |
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| AV01 | Patent right actively abandoned |