CN107588579A - Evaporator and air-conditioning system - Google Patents
Evaporator and air-conditioning system Download PDFInfo
- Publication number
- CN107588579A CN107588579A CN201710841124.6A CN201710841124A CN107588579A CN 107588579 A CN107588579 A CN 107588579A CN 201710841124 A CN201710841124 A CN 201710841124A CN 107588579 A CN107588579 A CN 107588579A
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- Prior art keywords
- liquid separation
- bobbin carriage
- refrigerant
- hole
- mouth
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Links
- 238000004378 air conditioning Methods 0.000 title claims abstract description 10
- 239000007788 liquid Substances 0.000 claims abstract description 178
- 239000003507 refrigerant Substances 0.000 claims abstract description 87
- 238000000926 separation method Methods 0.000 claims description 133
- 239000011148 porous material Substances 0.000 claims description 16
- 238000000889 atomisation Methods 0.000 claims description 7
- 230000002093 peripheral effect Effects 0.000 claims description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 6
- 230000000694 effects Effects 0.000 description 5
- 238000001704 evaporation Methods 0.000 description 3
- 230000008020 evaporation Effects 0.000 description 3
- 239000003595 mist Substances 0.000 description 3
- 239000007921 spray Substances 0.000 description 2
- 238000010586 diagram Methods 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000002360 explosive Substances 0.000 description 1
- 230000004907 flux Effects 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 230000037431 insertion Effects 0.000 description 1
- 238000003780 insertion Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000005057 refrigeration Methods 0.000 description 1
- 230000000452 restraining effect Effects 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
Landscapes
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
The invention discloses a kind of evaporator and air-conditioning system, the evaporator includes tube sheet, heat exchanger tube, bobbin carriage and liquid distributing device, the bobbin carriage is connected with the tube sheet formed with the bobbin carriage chamber for connecting feed pipe, the heat exchanger tube connects with the bobbin carriage chamber, the liquid distributing device is provided with the bobbin carriage chamber, the liquid distributing device is used to the refrigerant for entering the bobbin carriage chamber being atomized and is dispersed in the bobbin carriage intracavitary.The present invention sets liquid distributing device using in bobbin carriage intracavitary, the refrigerant for entering bobbin carriage chamber is atomized by liquid distributing device, refrigerant is set to be atomized to form tiny drop completely, and it is evenly distributed on bobbin carriage intracavitary, so that refrigerant can be distributed uniformly to the mouth of pipe of each heat exchanger tube, and then improve the heat exchange efficiency of evaporator.
Description
Technical field
The present invention relates to air-conditioning technical field, and in particular to a kind of evaporator and air-conditioning system.
Background technology
Shell and tube evaporator is the important component in refrigerated air-conditioning system, and its performance drops to the energy-conservation of whole refrigeration air-conditioner
Consumption plays the central role of key.In big-and-middle-sized handpiece Water Chilling Units, shell-and-tube evaporator mainly has two kinds of dry type and full-liquid type.
Wherein, shell and tube evaporator shell-side walks chilled water, and refrigerant is walked in heat exchanger tube, by the evaporation of refrigerant in horizontal tube, by outside pipe
Water cools to produce water at low temperature.Its application is relatively ripe, is designed without single heat exchanger oil return, but shell and tube evaporator
Have one disadvantage in that, more due to restraining, refrigerant is difficult to evenly distribute in each heat exchanger tube, and some heat exchanger tube refrigerants are more, have
Refrigerant is few, due to refrigerant distribution it is uneven, a big chunk heat exchange area does not make full use of, have impact on it heat exchange effect
Rate.
Although prior art also has carries out gas-liquid separation using by the refrigerant gas-liquid mixture for entering bobbin carriage, changed so as to improve
The thermal efficiency, still, the liquid refrigerants part after gas-liquid separation still have the problem of evenly distributed, therefore, liquid refrigerants part
Heat exchange efficiency is still very low, that is to say, that the refrigerant for entering bobbin carriage can not be atomized by prior art completely completely, and heat exchange effect is still
It is very low.
The content of the invention
The invention discloses a kind of evaporator and air-conditioning system, and the cold of bobbin carriage can not will be entered completely by solving prior art
Matchmaker is atomized completely, the problem of causing heat exchange efficiency low.
According to an aspect of the present invention, a kind of evaporator, including tube sheet, heat exchanger tube, bobbin carriage and liquid distributing device are disclosed,
The bobbin carriage is connected with the tube sheet to be connected formed with the bobbin carriage chamber for connecting feed pipe, the heat exchanger tube with the bobbin carriage chamber
It is logical, the liquid distributing device is provided with the bobbin carriage chamber, the liquid distributing device is used to that the refrigerant mist of the bobbin carriage chamber will to be entered
Change and be dispersed in the bobbin carriage intracavitary.
Further, the liquid distributing device includes being used for the liquid separation mouth for being atomized the refrigerant, is provided with the bobbin carriage
The refrigerant inlet connected with the feed pipe, the inlet of the liquid separation mouth connect with the refrigerant inlet.
Further, the liquid distributing device includes：First liquid separation mouth and the second liquid separation mouth, the first liquid separation mouth set institute
The inside of the second liquid separation mouth is stated, liquid separation chamber is formed between the first liquid separation mouth and the second liquid separation mouth.
Further, multiple first through hole are arranged at intervals with the middle part of the first liquid separation mouth, the refrigerant is from the liquid separation
The first through hole is flowed through in mouth inlet and enters the liquid separation intracavitary.
Further, the first liquid separation mouth peripheral side is formed with liquid separation passage.
Further, the first through hole and the liquid separation passage are arranged to make unit of the refrigerant by the first through hole
Flow is less than the specific discharge by the liquid separation passage.
Further, the second liquid separation mouth is arranged at intervals with multiple second through holes, the liquid separation chamber and the bobbin carriage chamber
Connected by second through hole, the refrigerant flows through second through hole from the liquid separation intracavitary and enters the bobbin carriage chamber
It is interior.
Further, second through-hole aperture is less than the aperture of the first through hole.
Further, second through hole include multiple clear openings parallel with the second liquid separation mouth axis direction and
There are multiple inclined holes of angle with the second liquid separation mouth axis direction, the inclined hole is disposed on the clear opening.
Further, the aperture of the clear opening is less than the aperture of the inclined hole.
Further, week of the one end of inlet of the liquid separation passage from the liquid distributing device to the second liquid separation mouth
It is extended to the other end in direction.
Further, second through hole is set towards the tube sheet.
Further, the tube sheet has pore, and the pore first end connects with the heat exchanger tube；The evaporator is also
Including homogenizing plate, the homogenizing plate is arranged on the second side of the tube sheet, and equal discharge orifice is provided with the homogenizing plate, described equal
Discharge orifice is correspondingly arranged with the pore.
Further, drainage tube is additionally provided with the homogenizing plate, one end of the drainage tube is arranged on the equal discharge orifice
The interior, other end is inserted in the pore.
According to another aspect of the present invention, a kind of air-conditioning system, including above-mentioned evaporator are disclosed.
The present invention sets liquid distributing device using in bobbin carriage intracavitary, and the refrigerant for entering bobbin carriage chamber is carried out into mist by liquid distributing device
Change, make refrigerant be atomized to form tiny drop completely, and be evenly distributed on bobbin carriage intracavitary, so that refrigerant can be distributed uniformly
To the mouth of pipe of each heat exchanger tube, and then improve the heat exchange efficiency of evaporator.
Brief description of the drawings
Fig. 1 is the structural representation of evaporator of the embodiment of the present invention；
Fig. 2 is the partial enlarged drawing of A in Fig. 1；
Fig. 3 is the explosive view of bobbin carriage of the embodiment of the present invention；
Fig. 4 is liquid distributing device B-B direction sectional view of the embodiment of the present invention；
Fig. 5 is liquid distributing device of embodiment of the present invention A-A to sectional view；
Fig. 6 is the second liquid separation mouth structure schematic diagram of the embodiment of the present invention.
Legend：1st, tube sheet；11st, pore；2nd, heat exchanger tube；3rd, bobbin carriage；31st, bobbin carriage chamber；32nd, the second end；321st, refrigerant enters
Mouthful；33rd, dividing plate；4th, liquid distributing device；41st, liquid separation mouth；411st, the first liquid separation mouth；4111st, first through hole；4112nd, liquid separation passage；
412nd, the second liquid separation mouth；4121st, clear opening；4122nd, inclined hole；413rd, liquid separation chamber；42nd, liquid separation mouth joint；5th, homogenizing plate；51st,
Discharge orifice；52nd, drainage tube；6th, feed pipe.
Embodiment
With reference to embodiment, the present invention will be further described, but is not limited to the content on specification.
The invention discloses a kind of evaporator, including tube sheet 1, heat exchanger tube 2, bobbin carriage 3 and liquid distributing device 4, heat exchanger tube 2 to be set
In the first side of tube sheet 1, bobbin carriage 3 is arranged on the second side of tube sheet 1, and the first side of tube sheet 1 is with the second side of tube sheet 1 on the contrary, pipe
Case 3 is connected with tube sheet 1 to be connected formed with the bobbin carriage chamber 31 for connecting feed pipe 6, the heat exchanger tube 2 with the bobbin carriage chamber 31,
Liquid distributing device 4 is provided with the inwall of bobbin carriage chamber 31, liquid distributing device 4 is used to the refrigerant for entering bobbin carriage chamber 31 being atomized and uniformly divided
It is dispersed in bobbin carriage chamber 31.After refrigerant, which enters liquid distributing device, to be atomized, exchanged heat into heat exchanger tube 2.The present invention is using in bobbin carriage chamber 31
Interior setting liquid distributing device 4, the refrigerant for entering bobbin carriage chamber 31 is atomized by liquid distributing device 4, makes refrigerant be atomized to be formed completely
Tiny drop, and be evenly distributed in bobbin carriage chamber 31, so that refrigerant can be distributed uniformly to the pipe of each heat exchanger tube 2
Mouthful, and then improve the heat exchange efficiency of evaporator.
In the above-described embodiments, liquid distributing device 4 includes being used for the liquid separation mouth 41 for being atomized refrigerant, be provided with bobbin carriage 3 with
The refrigerant inlet 321 that feed pipe 6 connects, refrigerant inlet 321 are connected with refrigerant pipe, the inlet and refrigerant inlet of liquid separation mouth 41
321 connections.Refrigerant in feed pipe 6 is entered in liquid separation mouth 41 by refrigerant inlet 321, then is formed carefully by the atomization of liquid separation mouth 41
Small drop, and be evenly distributed in bobbin carriage chamber 31, it is then dispensed in each heat exchanger tube 2 and is exchanged heat.Due to using liquid separation
Refrigerant is atomized by mouth 41, makes to be evenly distributed with the refrigerant drop after atomization in bobbin carriage chamber 31, therefore, the mouth of pipe of heat exchanger tube 2 is also uniform
Refrigerant drop is distributed with, so as to accomplish can to evenly distribute refrigerant into each heat exchanger tube 2, improves the heat exchange effect of evaporator
Rate.
In the above-described embodiments, liquid distributing device 4 includes：First liquid separation mouth 411 and the second liquid separation mouth 412, the first liquid separation mouth
411 are arranged on inside the second liquid separation mouth 412, and liquid separation chamber 413 is formed between the first liquid separation mouth 411 and the second liquid separation mouth 412, and
The axis direction of liquid separation chamber 413 is parallel to side with the axis of the inlet of liquid separation mouth 41, and the axis direction and tube sheet of liquid separation chamber 413
Plane where 1 is vertical.Refrigerant enters the first liquid separation mouth 411 by the inlet of liquid separation mouth 41, is made by the first liquid separation mouth 411 cold
Matchmaker's liquid forms less refrigerant drop, and enters in liquid separation chamber 413, so as to complete first time liquid separation, due to refrigerant constantly
Enter from the inlet of liquid separation mouth 41, therefore, the refrigerant after the first liquid separation mouth 411 completes first time liquid separation can be continuously
Into liquid separation chamber 413, so that producing high pressure in liquid separation chamber 413, make the refrigerant drop after first time liquid separation, pass through second
Liquid separation mouth 412 forms more tiny drop and entered in bobbin carriage chamber 31, second of liquid separation is completed, so as to reach the complete mist of refrigerant
The effect of change, the high pressure of liquid separation chamber 413 is additionally, since, makes the refrigerant after second of liquid separation that there is higher spouting velocity, so as to
The refrigerant fine drop after atomization is set to be evenly distributed on tube sheet 1.Because liquid separation mouth 41 uses two nozzles, and two
Liquid separation chamber 413 is provided between individual nozzle, so as to uniformly divide refrigerant on tube sheet 1 in vaporific by liquid separation twice, makes heat exchanger tube 2
The mouth of pipe is also evenly distributed with refrigerant drop, so as to accomplish can to evenly distribute refrigerant into each heat exchanger tube 2, improves evaporator
Heat exchange efficiency.
In order that refrigerant drop can be distributed more uniformly in each heat exchanger tube, and in the above-described embodiments, first point
The middle part annular space of liquid mouth 411 is provided with multiple first through hole 4111, and refrigerant flows through first through hole out of liquid separation mouth 41 inlet
4111 are entered in the liquid separation chamber 413, and the inlet of liquid separation mouth 41 is connected with liquid separation chamber 413 by first through hole 4111, and often
The axis direction of one first through hole 4111 is parallel with the axis direction of liquid separation chamber 413；The peripheral side of first liquid separation mouth 411 is formed
There is liquid separation passage 4112, first through hole 4111 and liquid separation passage 4112 are arranged to make unit stream of the refrigerant by first through hole 4111
Amount is less than by the specific discharge of liquid separation passage 4112, liquid separation passage 4112 from the liquid distributing device 4 inlet one end to
The other end of the circumferential direction of the second liquid separation mouth 412 is extended, and the inlet of liquid separation mouth 41 passes through liquid separation with liquid separation chamber 413
Passage 4112 connects, and the liquid feeding end of each liquid separation passage 4112 is close to the liquid feeding end of first through hole 4111, liquid separation passage 4112
Outlet end deviate from first through hole 4111 outlet end；The cross section of liquid separation passage 4112 is sector, and from liquid separation passage 4112
Water inlet end is gradually big to its water side, fan shaped cross section area.
Second liquid separation mouth 412 is arranged at intervals with multiple second through holes, and liquid separation chamber 413 passes through the second through hole with bobbin carriage chamber 31
4121 connections, refrigerant flow through the second through hole out of liquid separation chamber 413 and entered in bobbin carriage chamber 31, and the second through hole includes and the second liquid separation
The parallel multiple clear openings 4121 of the axis direction of mouth 412 and with the axis direction of the second liquid separation mouth 412 have angle it is multiple tiltedly
Hole 4122, inclined hole 4122 are disposed on clear opening 4121；The aperture of clear opening 4121 is less than the aperture of inclined hole 4122.
Refrigerant is led to from the inlet of liquid separation mouth 41 by the liquid separation of first through hole 4111 and surrounding among the first liquid separation mouth 411
Road 4112 enters in liquid separation chamber 413, then sprayed by the clear opening 4121 and inclined hole 4122 of annular array on the second liquid separation mouth 412
Onto tube sheet 1, vaporific refrigerant drop sprays to distance of the distance of tube sheet 1 than spraying to tube sheet 1 from inclined hole 4122 from clear opening 4121
It is short, therefore, in order to ensure that refrigerant drop can be distributed more uniformly to tube sheet 1, it will be set in the surrounding of the first liquid separation mouth 411
Liquid separation passage 4112 is put, the flow of the body surrounding of bobbin carriage chamber 31 is greater than intermediate position flow.
Specifically, the present invention is by the smaller first through hole 4111 of the middle part setting area of the first liquid separation mouth 411, and the
The larger liquid separation passage 4112 of the outside setting area of one through hole 4111, ensure that the cold medium flux for entering the surrounding of liquid separation chamber 413 is big
In the flow for entering the middle part of liquid separation chamber 413.And refrigerant passes through more small straight passage hole above the second liquid separation mouth 412 from liquid separation chamber 413
4121 and inclined hole 4122 equably to shunting everywhere, and because clear opening 4121 and inclined hole 4122 have smaller, refrigerant can be made
Vaporific injection, be advantageous to uniform liquid separation, and because the flow of the surrounding of shunting time-division first time sap cavity 413 is more than middle stream
Amount, and the diameter of inclined hole 4122 on the second liquid separation mouth 412 is more than the diameter of middle clear opening 4121, at this moment can cause to spray to
Inclined hole 4122 flow of the surrounding apart from new tube sheet 1 remotely is more than the flow of middle, so that into bobbin carriage chamber 31 everywhere
Local flow it is impartial.
In the above-described embodiments, liquid distributing device 4 also includes liquid separation mouth joint 42, and inlet and the liquid separation mouth of liquid separation mouth 41 connect
First 42 connection, and be connected by liquid separation mouth joint 42 with refrigerant inlet 321, liquid separation mouth 41 is installed and safeguard more and facilitate.
In the above-described embodiments, liquid separation mouth 41 exports is set towards tube sheet 1, and the refrigerant drop after atomization can be made directly equal
On even distribution to tube sheet 1, due to being connected with heat exchanger tube 2 on tube sheet 1, therefore, vaporific refrigerant can be directly entered heat exchanger tube 2,
Refrigerant is evenly distributed into each heat exchanger tube 2 so as to realize, improves the heat exchange efficiency of evaporator.
On the basis of above-described embodiment, tube sheet 1 has pore 11, and the first end of pore 11 connects with heat exchanger tube 2；Evaporator
Also include homogenizing plate 5, homogenizing plate 5 is arranged on the second side of tube sheet 1, and equal discharge orifice 51 is provided with homogenizing plate 5, and equal discharge orifice 51 exists
Projection on tube sheet 1 overlaps with pore 11 or in the range of pore 11.Above-mentioned equal discharge orifice 51 corresponds with pore 11,
And tube sheet 1 will not stop equal discharge orifice 51, refrigerant drop is flowed by homogenizing plate 5, and refrigerant drop is by homogenizing plate 5
Pore 11 is directly entered after equal discharge orifice 51, the problem of circulation is obstructed after refrigerant flows is avoided, is flowed so as to improve homogenizing plate
Efficiency, improve refrigerant distribution effect.
In the above-described embodiments, drainage tube 52 is additionally provided with homogenizing plate 5, one end of drainage tube 52 is arranged on equal discharge orifice 51
In interior, other end insertion pore 11.The present invention is being flowed by setting homogenizing plate 5 between liquid distributing device 4 and heat exchanger tube 2
Many discharge orifices 51 have been opened on plate 5, and each discharge orifice 51 has welded one section tiny of the access heat exchanger tube 2 of drainage tube 52,
When refrigerant is by liquid distributing device 4, due to the presence of liquid separation mouth 41 so that liquid refrigerants forms the droplet of atomization, whole pipe
All it is vaporific refrigerant in case chamber 31, because elongated drainage tube 52 plays throttling action, pressure is formed between bobbin carriage chamber 31 and heat exchanger tube 2
Difference, vaporific refrigerant is evenly distributed in the drainage tube 52 on homogenizing plate 5 by pressure, entered directly into heat exchanger tube 2；When cold
When matchmaker enters drainage tube 52, because the aperture of drainage tube 52 is more tiny so that refrigerant forms atomization again in heat exchanger tube 2,
Refrigerant expansion evaporation, increases the heat exchange area of refrigerant, heat exchange is more abundant, and heat exchange efficiency is higher, that is to say, that refrigerant is by dividing
Liquid mouth 41 carries out liquid separation twice, forms vaporific fine drop and enters in bobbin carriage chamber 31, and enters drainage tube by pressure difference
In 52, third time liquid separation is carried out by drainage tube 52, is atomized into more tiny drop, so as to refrigerant expansion evaporation, increase refrigerant
Heat exchange area, heat exchange it is more abundant, heat exchange efficiency is higher.
In another embodiment, dividing plate 33, inwall, part tube sheet 1 and the dividing plate of part bobbin carriage 3 are provided with bobbin carriage 3
33 surround bobbin carriage chamber 31, by setting dividing plate 33, make the space in bobbin carriage chamber 31 smaller, save space, and it is possible to will heat exchange
The muffler of pipe 2 is arranged in the cavity of the opposite side of dividing plate 33, makes heat exchanger tube 2 length of the heat exchanger tube 2 in the housing of evaporator
It is longer, make refrigerant stroke longer, fully heat exchange, improve heat exchange efficiency.
According to the another aspect of the application, a kind of air-conditioning system, including above-mentioned evaporator are also disclosed.
Obviously, above-mentioned embodiment of the invention is only intended to clearly illustrate example of the present invention, and is not
Restriction to embodiments of the present invention.For those of ordinary skill in the field, on the basis of the above description also
It can make other changes in different forms.Here all embodiments can not be exhaustive.It is every to belong to this
Row of the obvious changes or variations that the technical scheme of invention is extended out still in protection scope of the present invention.
Claims (15)
1. a kind of evaporator, it is characterised in that including tube sheet (1), heat exchanger tube (2), bobbin carriage (3) and liquid distributing device (4), the pipe
Case (3) is connected with the tube sheet (1) formed with the bobbin carriage chamber (31) for connecting feed pipe (6), the heat exchanger tube (2) with it is described
Bobbin carriage chamber (31) connects, and the liquid distributing device (4) is provided with the bobbin carriage chamber (31), the liquid distributing device (4) is used for will
Refrigerant into the bobbin carriage chamber (31) is atomized and is dispersed in the bobbin carriage chamber (31).
2. evaporator according to claim 1, it is characterised in that the liquid distributing device (4) includes being used for the refrigerant
The liquid separation mouth (41) of atomization, is provided with the refrigerant inlet (321) connected with the feed pipe (6) on the bobbin carriage (3), described point
The inlet of liquid mouth (41) connects with the refrigerant inlet (321).
3. evaporator according to claim 1 or 2, it is characterised in that the liquid distributing device (4) includes：First liquid separation mouth
(411) and the second liquid separation mouth (412), the inside of the first liquid separation mouth (411) setting the second liquid separation mouth (412) are described
Liquid separation chamber (413) is formed between first liquid separation mouth (411) and the second liquid separation mouth (412).
4. evaporator according to claim 3, it is characterised in that be arranged at intervals with the middle part of the first liquid separation mouth (411)
Multiple first through hole (4111), the refrigerant flow through the first through hole (4111) entrance out of described liquid separation mouth (41) inlet
In to the liquid separation chamber (413).
5. evaporator according to claim 4, it is characterised in that the first liquid separation mouth (411) peripheral side formed with
Liquid separation passage (4112).
6. evaporator according to claim 5, it is characterised in that the first through hole (4111) and the liquid separation passage
(4112) it is arranged to refrigerant by the specific discharge of the first through hole (4111) is less than by the liquid separation passage (4112)
Specific discharge.
7. evaporator according to claim 4, it is characterised in that the second liquid separation mouth (412) is arranged at intervals with multiple
Second through hole, the liquid separation chamber (413) are connected with the bobbin carriage chamber (31) by second through hole, and the refrigerant is from described point
Second through hole is flowed through in sap cavity (413) to enter in the bobbin carriage chamber (31).
8. evaporator according to claim 7, it is characterised in that second through-hole aperture is less than the first through hole
(4111) aperture.
9. evaporator according to claim 7, it is characterised in that second through hole includes and the second liquid separation mouth
(412) the parallel multiple clear openings (4121) of axis direction and there is angle with the second liquid separation mouth (412) axis direction
Multiple inclined holes (4122), the inclined hole (4122) is disposed on the clear opening (4121).
10. evaporator according to claim 9, it is characterised in that the aperture of the clear opening (4121) is less than described oblique
The aperture in hole (4122).
11. evaporator according to claim 9, it is characterised in that the liquid separation passage (4112) is by the liquid distributing device
(4) one end of inlet is extended to the other end of the circumferential direction of the second liquid separation mouth (412).
12. evaporator according to claim 2, it is characterised in that second through hole is set towards the tube sheet (1).
13. evaporator according to claim 12, it is characterised in that the tube sheet (1) has pore (11), the pore
(11) first end connects with the heat exchanger tube (2)；
The evaporator also includes homogenizing plate (5), and the homogenizing plate (5) is arranged on the second side of the tube sheet (1), described equal
Equal discharge orifice (51) is provided with flowing plate (5), the discharge orifice (51) is correspondingly arranged with the pore (11).
14. evaporator according to claim 13, it is characterised in that be additionally provided with drainage tube on the homogenizing plate (5)
(52), one end of the drainage tube (52) is arranged in the equal discharge orifice (51), the other end is inserted in the pore (11).
15. a kind of air-conditioning system, it is characterised in that including the evaporator described in claim any one of 1-14.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710841124.6A CN107588579A (en) | 2017-09-18 | 2017-09-18 | Evaporator and air-conditioning system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710841124.6A CN107588579A (en) | 2017-09-18 | 2017-09-18 | Evaporator and air-conditioning system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN107588579A true CN107588579A (en) | 2018-01-16 |
Family
ID=61048206
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710841124.6A Pending CN107588579A (en) | 2017-09-18 | 2017-09-18 | Evaporator and air-conditioning system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN107588579A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110068182A (en) * | 2019-05-29 | 2019-07-30 | 天津商业大学 | Atomizer formula current divider and refrigeration system |
| CN111023630A (en) * | 2019-12-18 | 2020-04-17 | 东南大学 | Shell-and-tube evaporator with liquid separating device |
| CN117387254A (en) * | 2023-12-11 | 2024-01-12 | 江苏世林博尔制冷设备有限公司 | Evaporator with multistage heat exchange |
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| US20130112381A1 (en) * | 2010-07-16 | 2013-05-09 | Alfa Laval Corporate Ab | Heat exchange device with improved system for distributing coolant fluid |
| JP2013108673A (en) * | 2011-11-21 | 2013-06-06 | Ihi Corp | Heat pump |
| CN106482550A (en) * | 2016-10-21 | 2017-03-08 | 珠海格力电器股份有限公司 | Channel structure, shell and tube exchanger and air-conditioner |
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2017
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| US20130112381A1 (en) * | 2010-07-16 | 2013-05-09 | Alfa Laval Corporate Ab | Heat exchange device with improved system for distributing coolant fluid |
| JP2013108673A (en) * | 2011-11-21 | 2013-06-06 | Ihi Corp | Heat pump |
| CN106482550A (en) * | 2016-10-21 | 2017-03-08 | 珠海格力电器股份有限公司 | Channel structure, shell and tube exchanger and air-conditioner |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110068182A (en) * | 2019-05-29 | 2019-07-30 | 天津商业大学 | Atomizer formula current divider and refrigeration system |
| CN111023630A (en) * | 2019-12-18 | 2020-04-17 | 东南大学 | Shell-and-tube evaporator with liquid separating device |
| CN117387254A (en) * | 2023-12-11 | 2024-01-12 | 江苏世林博尔制冷设备有限公司 | Evaporator with multistage heat exchange |
| CN117387254B (en) * | 2023-12-11 | 2024-04-26 | 江苏世林博尔制冷设备有限公司 | Evaporator |
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Application publication date: 20180116 |