CN205825508U - Diverter and dry evaporator - Google Patents
Diverter and dry evaporator Download PDFInfo
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- CN205825508U CN205825508U CN201620745253.6U CN201620745253U CN205825508U CN 205825508 U CN205825508 U CN 205825508U CN 201620745253 U CN201620745253 U CN 201620745253U CN 205825508 U CN205825508 U CN 205825508U
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Abstract
This utility model provides a kind of diverter and dry evaporator, and wherein, this diverter includes: flow distribution plate and the multiple isocons arranged on this flow distribution plate, wherein, the plurality of isocon includes the isocon of at least two length.By the isocon of diverter being set to the isocon with different length, the cold medium flux being assigned in each heat exchanger tube of dry evaporator by isocon is made to keep uniformly, the heat exchange area of each heat exchanger tube can be made full use of, thus be effectively improved the heat exchange efficiency of dry evaporator.
Description
Technical field
This utility model relates to refrigeration technology field, particularly relates to a kind of diverter and dry evaporator.
Background technology
Along with the commonly used of Refrigeration Technique and the worsening shortages of the energy, for refrigeration and the joint of Refrigeration Technique
The requirement of energy is more and more higher.Heat transmission equipment is the vitals in refrigeration system, nowadays, the refrigeration master of the refrigeration systems such as air-conditioning
The commonly used dry evaporator of machine is as main heat transmission equipment.The refrigeration system of employing dry evaporator, its coolant filling weight,
Reliability and stability and the equipment investment cost of oil return have the biggest advantage, and tool relative to full liquid vaporizer and falling film evaporator
Compact in standby structure, the features such as system controls simple, follow-up maintenance low cost, therefore, dry evaporator obtains extensively should
With.
The raising required energy-conserving and environment-protective along with society, the requirement for refrigeration host computer efficiency improves the most therewith.Dry type is steamed
Send out device, as main heat transmission equipment, the height of its heat exchange efficiency, the efficiency of refrigeration host computer is had important impact.Existing
Diverter in dry evaporator is for being assigned to coolant in each heat exchanger tube, and this diverter generally comprises has multiple running through
The flow distribution plate in hole and multiple carbon steel isocon with equal length and internal diameter, one end of each isocon is by electric welding respectively
Be welded at each through hole of flow distribution plate, thus corresponding with this through hole, the other end of each isocon respectively with dry type
Each heat exchanger tube of vaporizer connects.The coolant of input dry evaporator flows into each isocon by the through hole of flow distribution plate
In, import in each heat exchanger tube through each isocon.
It should be noted that introduction to technical background above is intended merely to convenient carry out the technical solution of the utility model clearly
Chu, complete explanation, and facilitate the understanding of those skilled in the art to illustrate.Can not be merely because these schemes be in this practicality
Novel background section is set forth and thinks that technique scheme is known to those skilled in the art.
Utility model content
Inventor of the present utility model finds, in above-mentioned existing dry evaporator, due to the effect of gravity, input is dry
The liquid refrigerants bulk deposition of formula vaporizer is in the bottom of dry evaporator, and uneven the causing of coolant distribution distributes to dry type steaming
Send out the refrigerant flow rate more than distribution to dry evaporator top of the refrigerant flow rate in the heat exchanger tube bottom device, in the heat exchanger tube of bottom
Coolant cannot evaporate completely, and cold medium shortage in heat exchange of top part pipe and refrigerant vapor in causing this heat exchanger tube is overheated, thus
Waste the area of heat exchanger tube so that the heat exchange efficiency of dry evaporator reduces.
This utility model embodiment provides a kind of diverter and dry evaporator, it is possible to will enter the coolant of dry evaporator
Distribute to each heat exchanger tube uniformly, it is possible to make full use of the heat exchange area of each heat exchanger tube, thus be effectively improved dry type evaporation
The heat exchange efficiency of device.
First aspect according to this utility model embodiment, it is provided that a kind of diverter, described diverter includes: flow distribution plate and
The multiple isocons arranged on described flow distribution plate, wherein, the plurality of isocon includes the isocon of at least two length.
According to the second aspect of this utility model embodiment, wherein, the plurality of isocon includes the first length isocon
With the second length isocon, the length of described second length isocon is more than the length of described first length isocon.
According to the third aspect of this utility model embodiment, wherein, the length of described second length isocon is described
1.5～3 times of the length of one length isocon.
According to the fourth aspect of this utility model embodiment, wherein, described first length isocon a length of 10mm～
80mm, a length of 20mm～120mm of described second length isocon.
The 5th aspect according to this utility model embodiment, wherein, the length of the plurality of isocon along with described point
The direction that the surface of stream plate is parallel is gradually increased.
The 6th aspect according to this utility model embodiment, wherein, the length of the plurality of isocon along with described point
The direction that the surface of stream plate is parallel is gradually increased in the range of 10mm～120mm.
The 7th aspect according to this utility model embodiment, wherein, the plurality of isocon includes at least two internal diameter chi
Very little isocon.
According to the eighth aspect of this utility model embodiment, wherein, the plurality of isocon includes the first internal diameter isocon
With the second internal diameter isocon, the internal diameter of described first internal diameter isocon is more than the internal diameter of described second internal diameter isocon.
The 9th aspect according to this utility model embodiment, wherein, the internal diameter of described first internal diameter isocon is described
1.5～3 times of the internal diameter of two internal diameter isocons.
The tenth aspect according to this utility model embodiment, wherein, the internal diameter of described first internal diameter isocon be 1.0mm～
3.0mm, the internal diameter of described second internal diameter isocon is 0.8mm～2.0mm.
The 11st aspect according to this utility model embodiment, wherein, the internal diameter of the plurality of isocon is along with described
The direction that the surface of flow distribution plate is parallel is gradually reduced.
The 12nd aspect according to this utility model embodiment, wherein, the internal diameter of the plurality of isocon is along with described
The direction that the surface of flow distribution plate is parallel is gradually reduced in the range of 0.8mm～3.0mm.
The 13rd aspect according to this utility model embodiment, wherein, the excursion of the length of the plurality of isocon
For 10mm～120mm, and/or, the excursion of the internal diameter of the plurality of isocon is 0.8mm～3.0mm.
According to the fourteenth aspect of this utility model embodiment, wherein, described flow distribution plate has multiple through hole, described
Multiple isocons are correspondingly arranged with the plurality of through hole respectively, the isocon of the corresponding setting of size of described through hole
Internal diameter size is consistent.
The 15th aspect according to this utility model embodiment, wherein, described flow distribution plate is rustless steel flow distribution plate, described point
Flow tube is rustless steel isocon.
The 16th aspect according to this utility model embodiment, wherein, described flow distribution plate and described isocon pass through laser
Weld and connect.
The 17th aspect according to this utility model embodiment, it is provided that a kind of dry evaporator, it is characterised in that described dry
Formula vaporizer includes that first aspect according to this utility model embodiment is to the diverter described in any one in the 16th aspect
And multiple heat exchanger tube, wherein, multiple isocons of described diverter are connected with the plurality of heat exchanger tube respectively.
The 18th aspect according to this utility model embodiment, wherein, being arranged in the plurality of isocon is described dry
The length of the isocon of formula base of evaporator is more than the length of the isocon being arranged on described dry evaporator top.
The 19th aspect according to this utility model embodiment, wherein, being arranged in the plurality of isocon is described dry
The internal diameter of the isocon of formula base of evaporator is less than the internal diameter of the isocon being arranged on described dry evaporator top.
The beneficial effects of the utility model are: by the isocon of diverter is set to the shunting with different length
Pipe so that the cold medium flux being assigned in each heat exchanger tube of dry evaporator by isocon keeps uniformly, it is possible to fully profit
With the heat exchange area of each heat exchanger tube, thus it is effectively improved the heat exchange efficiency of dry evaporator.
With reference to explanation hereinafter and accompanying drawing, disclose in detail particular implementation of the present utility model, specify this practicality
Novel principle can be in adopted mode.It should be understood that embodiment of the present utility model in scope not thus be subject to
Limit.In the range of the spirit and terms of claims, embodiment of the present utility model includes many changes, amendment
And equivalent.
The feature described for a kind of embodiment and/or illustrate can be in same or similar mode one or more
Other embodiment individual uses, combined with the feature in other embodiment, or substitute the feature in other embodiment.
It should be emphasized that term " includes/comprises " existence referring to feature, one integral piece, step or assembly herein when using, but also
It is not excluded for the existence of one or more further feature, one integral piece, step or assembly or additional.
Accompanying drawing explanation
Included accompanying drawing is used for providing being further understood from this utility model embodiment, which constitutes description
A part, is used for illustrating embodiment of the present utility model, and comes together to explain principle of the present utility model with word description.Aobvious
And easy insight, the accompanying drawing in describing below is only embodiments more of the present utility model, for those of ordinary skill in the art
From the point of view of, on the premise of not paying creative work, it is also possible to obtain other accompanying drawing according to these accompanying drawings.In the accompanying drawings:
Fig. 1 is a side view of the diverter of this utility model embodiment 1；
Fig. 2 is a front view of the diverter of this utility model embodiment 1；
Fig. 3 is another side view of the diverter of this utility model embodiment 1；
Fig. 4 is another front view of the diverter of this utility model embodiment 1；
Fig. 5 is a side view of the diverter of this utility model embodiment 2；
Fig. 6 is a front view of the diverter of this utility model embodiment 2；
Fig. 7 is the structure chart of the dry evaporator of this utility model embodiment 3.
Detailed description of the invention
Referring to the drawings, by description below, of the present utility model aforementioned and further feature will be apparent from.Saying
In bright book and accompanying drawing, specifically disclose particular implementation of the present utility model, which show and this practicality wherein can be used new
The some embodiments of the principle of type, it will thus be appreciated that this utility model is not limited to described embodiment, on the contrary, this reality
With novel whole amendments, modification and the equivalent including and falling within the scope of the appended claims.
Embodiment 1
Fig. 1 is a side view of the diverter of this utility model embodiment 1, and Fig. 2 is dividing of this utility model embodiment 1
One front view of stream device.As depicted in figs. 1 and 2, diverter 100 includes: flow distribution plate 101 and setting on flow distribution plate 101
Multiple isocons 102, wherein, the plurality of isocon 102 includes the isocon of at least two length.
So, the coolant of input dry evaporator imports in multiple heat exchanger tubes through multiple isocons of diverter, passes through
The isocon of diverter is set to the isocon with different length so that be assigned to each of dry evaporator by isocon
Cold medium flux in individual heat exchanger tube keeps uniformly, it is possible to makes full use of the heat exchange area of each heat exchanger tube, thus is effectively improved dry
The heat exchange efficiency of formula vaporizer.
In the present embodiment, the shape of flow distribution plate 101 can be arranged according to actual needs, such as, with dry evaporator
The shape of the tube sheet of middle installation diverter adapts.Such as, the surface of flow distribution plate 101 is rectangle substantially, or circle etc..
In the present embodiment, the quantity of multiple isocons 102 can be carried out according to the heat exchanger tube quantity in dry evaporator
Corresponding setting.
In the present embodiment, the proportionate relationship between the isocon quantity of different length can be arranged according to actual needs,
Such as, in the case of multiple isocons 102 include the isocon of two kinds of length, the quantity of the isocon of both length is set
It is set to equal.
In the present embodiment, multiple isocons 102 can include the isocon of at least two length, wherein, isocon
The kind quantity of length can be arranged according to actual needs, and such as, multiple isocons 102 can include the shunting of two kinds of length
Pipe, or the isocon of three kinds of length, or the isocon that length is gradually increased.
In the present embodiment, in multiple isocons 102, the distribution mode of the isocon of different length can be according to actual needs
And arrange, such as, the shorter isocon of length 102 is set on the top of flow distribution plate 101, length is set in the bottom of flow distribution plate 101
Spend longer isocon 102；Or, the length of isocon 102 is along the direction (flow distribution plate parallel with the surface of flow distribution plate 101
The length direction of 101) it is gradually increased.
In the present embodiment, in multiple isocons 102, the length of the isocon of different length can set according to actual needs
Putting, such as, the excursion of the length of multiple isocons 102 is 10mm～120mm.
In the present embodiment, the multiple isocons 102 being arranged on flow distribution plate 101 can be vertical with the surface of flow distribution plate 101
Connect.
In the present embodiment, flow distribution plate 101 is provided with multiple through hole 103, multiple isocons 102 and multiple through holes
103 are correspondingly arranged, and the internal diameter size of the isocon 102 of the corresponding setting of size of multiple through holes 103 is consistent.
In the present embodiment, the internal diameter of multiple isocons 102 may be configured as equal, for example, it is possible to by multiple isocons 102
Certain numerical value of being disposed as in 1.0mm～3.0mm of internal diameter.
In the present embodiment, flow distribution plate 101 and isocon 102 can use rustless steel to make, so, and diverter weather-proof
Property preferable, not with the moisture in air and oxygen generation chemical reaction and produce oxidative phenomena such that it is able to the most permanent
Holding any surface finish, it is easy to preserve.
In the present embodiment, flow distribution plate 101 can be connected by laser welding with isocon 102, so, due to Laser Welding
The welding temperature connect is relatively low, and diverter is not likely to produce deformation after carrying out assembly welding.
In the diverter shown in Fig. 1 and Fig. 2, include carrying out as a example by the isocon of two kinds of length by multiple isocons 102
Explanation, as depicted in figs. 1 and 2, multiple isocons 102 include the first length isocon 102-1 and the second length isocon
102-2, is positioned at the length of the second length isocon 102-2 of bottom more than superposed first length isocon 102-1's
Length, wherein, after this diverter is installed to dry evaporator, the second length isocon 102-2 being positioned at bottom is positioned at
The bottom of dry evaporator.
In the present embodiment, between length and the length of the first length isocon 102-1 of the second length isocon 102-2
Proportionate relationship can arrange according to actual needs, such as, the length of the second length isocon 102-2 is the first length isocon
1.5～3 times of the length of 102-1.
In the present embodiment, the concrete numerical value of the length of the first length isocon 102-1 and the second length isocon 102-2
Can arrange according to actual needs, such as, a length of 10mm～80mm of the first length isocon 102-1, the second length shunting
A length of 20mm～120mm of pipe 102-2.
Fig. 3 is another side view of the diverter of this utility model embodiment 1, and Fig. 4 is this utility model embodiment 1
Another front view of diverter.As shown in Figure 3 and Figure 4, diverter 200 includes: flow distribution plate 201 and setting on flow distribution plate 201
The multiple isocons 202 put, multiple isocons 202 include the isocon of at least two length, wherein, multiple isocons 202
Length along the direction (above-below direction in the length direction of flow distribution plate 201, i.e. Fig. 3) parallel with the surface of flow distribution plate 201 by
Cumulative greatly.
In the present embodiment, the length of multiple isocons 202 can be along the direction parallel with the surface of flow distribution plate 201
(above-below direction in the length direction of flow distribution plate 201, i.e. Fig. 3) is gradually increased in the range of 10mm～120mm.Such as,
The a length of 10mm of the isocon 202 at top, a length of 120mm of the isocon 202 of bottommost.
From above-described embodiment, by the isocon of diverter being set to the isocon with different length so that
The cold medium flux being assigned in each heat exchanger tube of dry evaporator by isocon keeps uniformly, it is possible to makes full use of each and changes
The heat exchange area of heat pipe, thus it is effectively improved the heat exchange efficiency of dry evaporator.
Embodiment 2
This utility model embodiment provides a kind of diverter, wherein, the isocon internal diameter of the diverter of embodiment 2 and enforcement
Difference in example 1, other structures can be same as in Example 1.
Fig. 5 is a side view of the diverter of this utility model embodiment 2, and Fig. 6 is dividing of this utility model embodiment 2
One front view of stream device.As shown in Figure 5 and Figure 6, diverter 300 includes: flow distribution plate 301 and setting on flow distribution plate 301
Multiple isocons 302, wherein, the plurality of isocon 302 includes the isocon of at least two length, and, the plurality of isocon
302 isocons including at least two internal diameter size.
So, by the isocon of diverter being set to the isocon with different length and different inner diameters so that logical
Cross isocon to be assigned to the cold medium flux in each heat exchanger tube of dry evaporator and keep uniform further, it is possible to the most abundant
Utilize the heat exchange area of each heat exchanger tube, thus improve the heat exchange efficiency of dry evaporator further.
In the present embodiment, in multiple isocons 302, the internal diameter of the isocon of different inner diameters size can be according to actual needs
And arrange, such as, the excursion of the internal diameter of multiple isocons 302 is 0.8mm～3.0mm.
In the present embodiment, the proportionate relationship between the isocon quantity of different inner diameters size can set according to actual needs
Put, such as, in the case of multiple isocons 102 include the isocon of two kinds of internal diameter sizes, dividing both internal diameter sizes
The quantity of flow tube is set to equal.
As shown in Figure 5 and Figure 6, multiple isocons 302 include the first length isocon 302-1 and the second length isocon
302-2, wherein, has the first internal diameter (in the first length isocon 302-1 is also called first with the first length isocon 302-1
Footpath isocon) and the second length isocon 302-2 has the second internal diameter, and (the second length isocon 302-2 is also called the second internal diameter
Isocon) as a example by be illustrated, wherein, the internal diameter of the first internal diameter isocon is more than the internal diameter of the second internal diameter isocon.Such as Fig. 5
Shown in Fig. 6, flow distribution plate 301 has multiple through hole 303, and multiple isocons 302 are correspondingly arranged with multiple through holes 303, many
The internal diameter size of the isocon 302 of the corresponding setting of size of individual through hole 303 is consistent, wherein, and the hole 303-1's on top
The first internal diameter that size has with the first length isocon 302-1 is consistent, and the size of the hole 303-2 of bottom is divided with the second length
The second internal diameter that flow tube 302-2 has is consistent, wherein, after this diverter is installed to dry evaporator, is positioned at bottom
The second length isocon 302-2 be positioned at the bottom of dry evaporator.
In the present embodiment, flow distribution plate 301 and the material of multiple isocon 303, and flow distribution plate 301 and multiple isocons
The method of attachment of 303 can be identical with the record in embodiment 1, and here is omitted.
In the present embodiment, with have the first length isocon 302-1 of short length there is the first bigger internal diameter and
Have as a example by the second length isocon 302-2 of long length has the second less internal diameter and be illustrated, but, isocon
Internal diameter size can not also carry out this corresponding setting with its length, the isocon of which kind of length has the internal diameter of which kind of size
Can arrange according to actual needs, if enable to by isocon be assigned in each heat exchanger tube of dry evaporator cold
Matchmaker's flow keeps uniformly.
In the present embodiment, the proportionate relationship between the first internal diameter and the second internal diameter can be arranged according to actual needs, example
As, the first internal diameter is 1.5～3 times of the second internal diameter.
In the present embodiment, the concrete numerical value of the first internal diameter and the second internal diameter can be arranged according to actual needs, such as, the
One internal diameter is 1.0mm～3.0mm, and the second internal diameter is 0.8mm～2.0mm.
Have as a example by the isocon of two kinds of internal diameters by multiple isocons 302 in fig. 5 and fig. and be illustrated, but, this
Isocon 302 in embodiment can also be the isocon with three kinds or more internal diameter, for example, it is possible to by multiple shuntings
The internal diameter of pipe 302 is arranged along the direction (above-below direction in Fig. 5) parallel with the surface of flow distribution plate and is gradually reduced, such as,
The internal diameter of multiple isocons 302 is gradually reduced in the range of 0.8mm～3.0mm.
From above-described embodiment, by be set to the isocon of diverter to have different length and different inner diameters point
Flow tube so that the cold medium flux being assigned in each heat exchanger tube of dry evaporator by isocon keeps uniformly, it is possible to fully
Utilize the heat exchange area of each heat exchanger tube, thus improve the heat exchange efficiency of dry evaporator.
Embodiment 3
This utility model embodiment provides a kind of dry evaporator, and this dry evaporator includes diverter, this diverter
Structure is identical with the record in embodiment 1 or embodiment 2 with function, and here is omitted.
Fig. 7 is the structure chart of the dry evaporator of this utility model embodiment 3.As it is shown in fig. 7, dry evaporator 700 wraps
Include: protecgulum 701, the coolant import 702 being positioned on protecgulum 701, diverter 703, tube sheet 704, multiple heat exchanger tube 705, deflection plate
706, cylinder 707, bonnet 708, refrigerant exit 709, chilled water inlet 710 and chilled water outlet 711, wherein, diverter 703
Being arranged on tube sheet 704, multiple isocons of diverter 703 are connected with multiple heat exchanger tubes 705 respectively.
In the present embodiment, the structure of diverter 703 is identical with the record of embodiment 1 or embodiment 2, the most superfluous
State.
In the present embodiment, protecgulum 701, coolant import 702, tube sheet 704, multiple heat exchanger tube 705, deflection plate 706, cylinder
707, bonnet 708, refrigerant exit 709, chilled water inlet 710 and chilled water outlet 711 can use existing structure.
In the present embodiment, the length of the isocon bottom dry evaporator 700 can be set greater than dry type evaporation
The length of the isocon at device 700 top.
Such that make the liquid refrigerants bulk deposition of input dry evaporator in the bottom of dry evaporator, do owing to inciting somebody to action
The length of the isocon bottom formula vaporizer 700 is set greater than the length of the isocon at dry evaporator 700 top so that logical
Cross the cold medium flux that isocon is assigned in each heat exchanger tube and keep uniformly, it is possible to make full use of the heat-transfer surface of each heat exchanger tube
Long-pending, thus improve the heat exchange efficiency of dry evaporator.
In the present embodiment, it is also possible to the internal diameter of the isocon bottom dry evaporator 700 is set smaller than dry type and steams
Send out the internal diameter of the isocon at device 700 top.In such manner, it is possible to further improve the heat exchange efficiency of dry evaporator.
From above-described embodiment, by the isocon of diverter being set to the isocon with different length so that
The cold medium flux being assigned in each heat exchanger tube of dry evaporator by isocon keeps uniformly, it is possible to makes full use of each and changes
The heat exchange area of heat pipe, thus improve the heat exchange efficiency of dry evaporator.
Above in association with specific embodiment, this utility model is described, but those skilled in the art should be clear
Chu, these descriptions are all exemplary, are not the restriction to this utility model protection domain.Those skilled in the art can root
According to spirit of the present utility model and principle, this utility model being made various variants and modifications, these variants and modifications are also in this reality
With in novel scope.
Claims (19)
1. a diverter, it is characterised in that described diverter includes: flow distribution plate and on described flow distribution plate arrange multiple points
Flow tube, wherein, the plurality of isocon includes the isocon of at least two length.
Diverter the most according to claim 1, it is characterised in that the plurality of isocon include the first length isocon and
Second length isocon, the length of described second length isocon is more than the length of described first length isocon.
Diverter the most according to claim 2, it is characterised in that the length of described second length isocon is described first
1.5～3 times of the length of length isocon.
Diverter the most according to claim 2, it is characterised in that a length of 10mm of described first length isocon～
80mm, a length of 20mm～120mm of described second length isocon.
Diverter the most according to claim 1, it is characterised in that the length of the plurality of isocon along with described shunting
The direction that the surface of plate is parallel is gradually increased.
Diverter the most according to claim 4, it is characterised in that the length of the plurality of isocon along with described shunting
The direction that the surface of plate is parallel is gradually increased in the range of 10mm～120mm.
Diverter the most according to claim 1, it is characterised in that the plurality of isocon includes at least two internal diameter size
Isocon.
Diverter the most according to claim 6, it is characterised in that the plurality of isocon include the first internal diameter isocon and
Second internal diameter isocon, the internal diameter of described first internal diameter isocon is more than the internal diameter of described second internal diameter isocon.
Diverter the most according to claim 8, it is characterised in that the internal diameter of described first internal diameter isocon is described second
1.5～3 times of the internal diameter of internal diameter isocon.
Diverter the most according to claim 8, it is characterised in that the internal diameter of described first internal diameter isocon be 1.0mm～
3.0mm, the internal diameter of described second internal diameter isocon is 0.8mm～2.0mm.
11. diverters according to claim 7, it is characterised in that the internal diameter of the plurality of isocon along with described point
The direction that the surface of stream plate is parallel is gradually reduced.
12. diverters according to claim 11, it is characterised in that the internal diameter of the plurality of isocon along with described point
The direction that the surface of stream plate is parallel is gradually reduced in the range of 0.8mm～3.0mm.
13. diverters according to claim 1, it is characterised in that the excursion of the length of the plurality of isocon is
10mm～120mm, and/or, the excursion of the internal diameter of the plurality of isocon is 0.8mm～3.0mm.
14. diverters according to claim 1, it is characterised in that have multiple through hole on described flow distribution plate are described many
Individual isocon is correspondingly arranged with the plurality of through hole respectively, the isocon of the corresponding setting of size of described through hole interior
Footpath size is consistent.
15. diverters according to claim 1, it is characterised in that described flow distribution plate is rustless steel flow distribution plate, described shunting
Pipe is rustless steel isocon.
16. diverters according to claim 1, it is characterised in that described flow distribution plate and described isocon pass through Laser Welding
Connect and connect.
17. 1 kinds of dry evaporators, it is characterised in that described dry evaporator includes according to any one in claim 1-16
Described diverter and multiple heat exchanger tube, wherein, multiple isocons of described diverter are respectively with the plurality of heat exchanger tube even
Connect.
18. dry evaporators according to claim 17, it is characterised in that being arranged in the plurality of isocon is described
The length of the isocon bottom dry evaporator is more than the length of the isocon being arranged on described dry evaporator top.
19. dry evaporators according to claim 18, it is characterised in that being arranged in the plurality of isocon is described
The internal diameter of the isocon bottom dry evaporator is less than the internal diameter of the isocon being arranged on described dry evaporator top.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620745253.6U CN205825508U (en) | 2016-07-15 | 2016-07-15 | Diverter and dry evaporator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620745253.6U CN205825508U (en) | 2016-07-15 | 2016-07-15 | Diverter and dry evaporator |
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| Publication Number | Publication Date |
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| CN205825508U true CN205825508U (en) | 2016-12-21 |
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ID=57563158
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| Application Number | Title | Priority Date | Filing Date |
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| CN201620745253.6U Active CN205825508U (en) | 2016-07-15 | 2016-07-15 | Diverter and dry evaporator |
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| CN (1) | CN205825508U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2022022144A1 (en) * | 2020-07-29 | 2022-02-03 | 约克广州空调冷冻设备有限公司 | Evaporator |
-
2016
- 2016-07-15 CN CN201620745253.6U patent/CN205825508U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2022022144A1 (en) * | 2020-07-29 | 2022-02-03 | 约克广州空调冷冻设备有限公司 | Evaporator |
| TWI804896B (en) * | 2020-07-29 | 2023-06-11 | 大陸商約克廣州空調冷凍設備有限公司 | Evaporator |
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