CN109140836A - Flash Type economizer suitable for refrigeration unit - Google Patents
Flash Type economizer suitable for refrigeration unit Download PDFInfo
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- CN109140836A CN109140836A CN201811338894.XA CN201811338894A CN109140836A CN 109140836 A CN109140836 A CN 109140836A CN 201811338894 A CN201811338894 A CN 201811338894A CN 109140836 A CN109140836 A CN 109140836A
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- 238000005057 refrigeration Methods 0.000 title claims abstract description 32
- 239000007788 liquid Substances 0.000 claims abstract description 66
- 238000005192 partition Methods 0.000 claims abstract description 44
- 238000005452 bending Methods 0.000 claims abstract description 31
- 239000003507 refrigerant Substances 0.000 claims description 86
- 238000000926 separation method Methods 0.000 claims description 17
- 239000000203 mixture Substances 0.000 claims description 13
- 238000003466 welding Methods 0.000 claims description 11
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 5
- 230000000694 effects Effects 0.000 description 9
- 230000006835 compression Effects 0.000 description 6
- 238000007906 compression Methods 0.000 description 6
- 238000001816 cooling Methods 0.000 description 6
- 241000521257 Hydrops Species 0.000 description 5
- 206010030113 Oedema Diseases 0.000 description 5
- 238000000034 method Methods 0.000 description 5
- 230000001502 supplementing effect Effects 0.000 description 5
- 238000010586 diagram Methods 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 3
- 230000008569 process Effects 0.000 description 3
- 239000000463 material Substances 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 235000017166 Bambusa arundinacea Nutrition 0.000 description 1
- 235000017491 Bambusa tulda Nutrition 0.000 description 1
- 241001330002 Bambuseae Species 0.000 description 1
- 235000015334 Phyllostachys viridis Nutrition 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 238000004378 air conditioning Methods 0.000 description 1
- 239000011425 bamboo Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 210000004243 sweat Anatomy 0.000 description 1
- 238000010977 unit operation Methods 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B39/00—Evaporators; Condensers
- F25B39/02—Evaporators
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B43/00—Arrangements for separating or purifying gases or liquids; Arrangements for vaporising the residuum of liquid refrigerant, e.g. by heat
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- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Mechanical Engineering (AREA)
- Thermal Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Analytical Chemistry (AREA)
- Power Engineering (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
The present invention discloses the Flash Type economizer suitable for refrigeration unit, including cylinder, first end cover, second end cover, inlet tube, outlet tube, escape pipe, partition, the first separating plate and the second horizontal separating plate are provided on cylinder, close to first end cover and close to the top of cylinder, escape pipe is located at the top of cylinder and close to second end cover inlet tube；Outlet tube is connected to the bottom of cylinder, and second separating plate one end is connect with the top of the first separating plate, the other end and second end cover connect, and is evenly arranged with several through-holes on the first separating plate and the second separating plate；First baffle and second baffle are also connected on the inner wall of cylinder, the connection of the bottom end seal of first baffle one end and partition, the other end of first baffle has downward bending, and second baffle one end is connect with second end cover, and the other end of second baffle has downward bending.The present invention is suitable for the Flash Type economizer outlet of refrigeration unit without liquid, at low cost.
Description
Technical field
The present invention relates to technical field of refrigeration equipment, more particularly to the Flash Type economizer for being suitable for refrigeration unit.
Background technique
Flash Type economizer (also known as flash tank, province's function device) is that one kind is extensive in refrigerating and air conditioning industry cold water heat pump unit
The energy saver that unit operation efficiency can be improved of application, in two stages of compression two-stage throttle refrigeration system, Flash Type economy
Device is typically provided at after a nuclear one-stage throttling device, and refrigerant liquid throttles by a nuclear one-stage throttling device, forms gas-liquid two-phase system
Cryogen enters in Flash Type economizer cylinder through inlet tube, and the gaseous parts in refrigerant pass through setting in economizer cylinder
Structure is completely separated with liquid part, and the gas separated enters in the gas supplementing opening of compressor through escape pipe, with compressor from
Evaporator is drawn through the intermediate pressure refrigerant gas mixing formed after low-pressure stage first compression and enters hiigh pressure stage second compression again；
The refrigerant liquid separated is flowed out by outlet tube, and evaporator sweat cooling is entered after second throttle.Due to by primary
The liquid refrigerant enthalpy of throttling reduces, so the two stages of compression two-stage throttle refrigeration system of configuration Flash Type economizer is than list
Grade compression single-stage throttle refrigeration system refrigerating capacity increases, and compressor consumption power increasing degree is smaller, so that unit can be improved
Operational efficiency, and the increase rate of operational efficiency increases with the difference of evaporating pressure and condensing pressure and is dramatically increased.
It is entered in Flash Type economizer cylinder as gas-liquid two-phase cold-producing medium constantly passes through inlet tube, liquid refrigerant is not
The disconnected bottom for being gathered in cylinder, is then flowed out by outlet tube.The refrigerant liquid level for being gathered in cylinder body bottom will receive constantly
The big ups and downs generated by the impact of the gas-liquid two-phase cold-producing medium of inlet tube entrance, liquid level big ups and downs will lead to first
Walking isolated liquid refrigerant can be involved in refrigerant gas stream again with the different droplet morphology of particle size, and Flash Type passes through in addition
Space is originally narrower in Ji device, if not can be carried out thorough gas-liquid separation, will inevitably lead to a large amount of refrigerants
Drop enters compressor gas supplementing opening from Flash Type economizer escape pipe, and compressor is the mechanical device of compressed gas, tonifying Qi band
The consequence of liquid is that compressor consumption power is caused to increase and be easy to damage running gear in compressor.
The good material filling type demister of gas-liquid separation effect or filter is arranged in existing Flash Type economizer near gas outlet
Net etc. avoids mending gas carrying liquid, although however demister or strainer are arranged near gas outlet can prevent from mending gas carrying liquid, by
Demister is flowed through in refrigerant gas or strainer generates larger pressure drop and makes the refrigerant gas pressure into compressor gas supplementing opening
It reduces, so that air compensation be made to reduce.Test data shows the every reduction 20kPa of economizer outlet pressure, into compressor gas supplementing opening
Gas mass flow will reduce 4% or so, will lead to compressor cooling capacity and operational efficiency and meanwhile reduce by 2.5% or so；And it sets
The purpose for setting economizer is after the cost for having paid the structural complexity and cost that increase unit, it is necessary to obtain unit efficiency
The income significantly improved with cooling capacity, and refrigerant gas generated inside economizer larger pressure drop and setting Flash Type economizer with
The original intention for improving cooling capacity and operational efficiency is runed counter to.
Summary of the invention
The object of the present invention is to provide the Flash Type economizers for being suitable for refrigeration unit, exist to solve the above-mentioned prior art
The problem of, guarantee the complete gas-liquid separation of refrigerant for entering Flash Type economizer, and under the premise of avoiding mending gas carrying liquid as far as possible
The pressure drop of less refrigerant gas.
To achieve the above object, the present invention provides following schemes: the present invention provides the Flash Type for being suitable for refrigeration unit
Economizer, including horizontal cylinder, described cylinder one end is provided with first end cover, the other end is provided with second end cover, the cylinder
Inlet tube, outlet tube and escape pipe are provided on body, the inlet tube is close to the first end cover and close to the top of the cylinder
Portion, the escape pipe are located at the top of the cylinder and close to the second end covers；Be connected on the inner wall of the cylinder partition,
First separating plate and the second horizontal separating plate, first separating plate and the partition be located at same perpendicular and it is described every
Between the bottom end of plate and the top of first separating plate exist interval, the perpendicular be located at the inlet tube and it is described out
Between tracheae and close to the inlet tube, the outlet tube between first separating plate and the second end cover, it is close
It the second end cover and is connected to the bottom of the cylinder, the top of second separating plate one end and first separating plate connects
Connect, the other end is connect with the second end cover, be evenly arranged on first separating plate and second separating plate several
A through-hole.
First baffle and second baffle, the first baffle and the second baffle are also connected on the inner wall of the cylinder
The horizontal and described first baffle is located at the lower section of the second baffle, and described first baffle one end and the bottom end of the partition are close
There is interval between the second end cover and the second end cover and have in envelope connection, the other end of the first baffle
Downward bending, described second baffle one end are connect with the second end cover, the other end of the second baffle and close to described
There is interval between partition and the partition and there is downward bending.
Preferably, the inlet tube is horizontally disposed, and the outlet tube and the escape pipe are vertically arranged.
Preferably, the top edge of the inlet tube is 20 ~ 50mm, the feed liquor at a distance from the top inner wall of the cylinder
The end that pipe is located at the intracorporal one end of the cylinder is chamfer, and the angle of the beveling is 30 ~ 60 degree, and the inlet tube is located at the cylinder
The shortest distance of the inner wall of the end of intracorporal one end and the cylinder is 40 ~ 80mm, and the caliber of the inlet tube must guarantee to make
The flow velocity of cryogen gas-liquid mixture is 4 ~ 8m/s.
Preferably, the curved bending radius of the escape pipe is 90 degree, and the horizontal component of the escape pipe is located at described
In cylinder, and the top edge of the horizontal component of the escape pipe is 20 ~ 50mm at a distance from the top inner wall of the cylinder, described
The length of the horizontal component of escape pipe is 50 ~ 100mm, and the air inlet of the horizontal component of the escape pipe is towards the second end
It covers and is 100 ~ 150mm at a distance from the inner wall of the second end cover, refrigerant gas is not higher than 6m/ in the flow velocity of escape pipe
s。
Preferably, the inner wall of first separating plate, second separating plate and the cylinder surrounds surge chamber, and described
The edge that one separating plate is connect with the cylinder is arc-shaped, and the top of first separating plate is in horizontal linear, institute
The second separating plate is stated to be rectangle；The height of first separating plate is 20 ~ 50mm, and the aperture of the through-hole is 3 ~ 8mm, adjacent
It is all on first separating plate and second separating plate that the spacing of two through-holes need to guarantee that refrigerant liquid flows through
The mean flow rate of through-hole is between 0.3 ~ 0.7m/s.
Preferably, the edge that the partition is connect with the cylinder is arc-shaped, and the bottom end of the partition is in horizontal
Linear, the height of the partition need to guarantee that refrigerant gas passes through the partition, first separating plate and the cylinder
The flow velocity that inner wall is formed by region is 0.5 ~ 1m/s.
Preferably, the length of the first baffle need to guarantee refrigerant gas by first baffle, the second end cover and
The flow velocity that the inner wall of the cylinder is formed by region is 1 ~ 1.5m/s；The first baffle is connect with the inner wall of the cylinder
It is respectively arranged with 2 ~ 4 holes on two sides, is 100 ~ 200mm at a distance from the partition close to the hole of the partition,
The shape in the hole is semicircle, triangle or rectangular；It is fully welded between the partition and the inner wall of the cylinder, the first gear
The inner wall spot welding of plate and the cylinder, and guarantee that the width in gap between the first baffle and the inner wall of the cylinder is little
In 1mm, refrigerant gas is in the first airflow channel that second separating plate, the first baffle and the cylinder are surrounded
Flow velocity be 0.5 ~ 1m/s；The length of the bending of the first baffle need to guarantee that refrigerant gas passes through the folding of the first baffle
The flow velocity that the inner wall of curved end, second separating plate and the cylinder is formed by region is no more than 2m/s, and described first
The angle of the bending of baffle is 60 ~ 120 degree.
Preferably, 2 ~ 4 holes are respectively arranged on two sides that the second baffle is connect with the inner wall of the cylinder,
The hole close to the port of the escape pipe is 50 ~ 100mm at a distance from the port of the escape pipe, and the shape in the hole is
Semicircle, triangle or rectangular；The length of the second baffle must guarantee refrigerant gas by the second baffle, it is described every
The flow velocity in the region between the inner wall of plate and the cylinder is 1 ~ 1.5m/s；The inner wall point of the second baffle and the cylinder
Weldering, and guarantee the width in gap between the second baffle and the inner wall of the cylinder no more than 1mm, the first baffle,
What the second airflow channel and the second baffle and the cylinder that the second baffle and the cylinder are constituted were constituted
The flow velocity of refrigerant gas is 0.5 ~ 1m/s in third airflow channel；The length of the bending of the second baffle need to guarantee refrigerant
Flow velocity of the gas in the region between the inner wall of the end of the bending of the second baffle, the first baffle and the cylinder
No more than 2m/s, the angle of the bending of the second baffle is 60 ~ 120 degree.
The Flash Type economizer that the present invention is suitable for refrigeration unit achieves following technical effect compared with the existing technology:
The Flash Type economizer that the present invention is suitable for refrigeration unit can be realized that refrigerant is thorough, complete gas-liquid separation, avoid
The risk of gas carrying liquid is mended, and the pressure drop of refrigerant gas is very small.The present invention is suitable for the Flash Type economizer of refrigeration unit
In the refrigerant liquid that surge chamber assembles cylinder body bottom formed by the first separating plate of setting and the second separating plate and cylinder
It will not be impacted by the gas-liquid two-phase cold-producing medium that inlet tube enters and generate big ups and downs, be weighed again so as to avoid liquid refrigerant
Newly it is involved in refrigerant gas stream；And the present invention is suitable for the dress such as the not set demister of Flash Type economizer and strainer of refrigeration unit
It sets, it is at low cost, and significantly improve cooling capacity and operational efficiency.
Detailed description of the invention
It in order to more clearly explain the embodiment of the invention or the technical proposal in the existing technology, below will be to institute in embodiment
Attached drawing to be used is needed to be briefly described, it should be apparent that, the accompanying drawings in the following description is only some implementations of the invention
Example, for those of ordinary skill in the art, without any creative labor, can also be according to these attached drawings
Obtain other attached drawings.
Fig. 1 is the structural schematic diagram for the Flash Type economizer that the present invention is suitable for refrigeration unit；
Fig. 2 is the partial structure diagram for the Flash Type economizer that the present invention is suitable for refrigeration unit；
Fig. 3 is the structural schematic diagram of present invention first baffle suitable for the Flash Type economizer of refrigeration unit；
Fig. 4 is the structural schematic diagram of present invention second baffle suitable for the Flash Type economizer of refrigeration unit；
Wherein, 1- first end cover, 2- inlet tube, 3- cylinder, 4- escape pipe, 5- second end cover, 6- outlet tube, 7- second baffle,
8- first baffle, the second separating plate of 9-, the first separating plate of 10-, 11- partition.
Specific embodiment
Following will be combined with the drawings in the embodiments of the present invention, and technical solution in the embodiment of the present invention carries out clear, complete
Site preparation description, it is clear that described embodiments are only a part of the embodiments of the present invention, instead of all the embodiments.It is based on
Embodiment in the present invention, it is obtained by those of ordinary skill in the art without making creative efforts every other
Embodiment shall fall within the protection scope of the present invention.
The object of the present invention is to provide the Flash Type economizers for being suitable for refrigeration unit, to solve of the existing technology ask
Topic guarantees the complete gas-liquid separation of refrigerant for entering Flash Type economizer, and less as far as possible under the premise of avoiding mending gas carrying liquid
The pressure drop of refrigerant gas.
In order to make the foregoing objectives, features and advantages of the present invention clearer and more comprehensible, with reference to the accompanying drawing and specific real
Applying mode, the present invention is described in further detail.
As shown in Fig. 1 ~ 4, the Flash Type economizer that the present embodiment is suitable for refrigeration unit includes horizontal cylinder 3, cylinder 3
Left end is provided with first end cover 1, right end is provided with second end cover 5, and inlet tube 2, outlet tube 6 and escape pipe are provided on cylinder 3
4, close to first end cover 1 and close to the top of cylinder 3, escape pipe 4 is located at the top of cylinder 3 and close to second end cover inlet tube 2
5；Be connected on the inner wall of cylinder 3 partition 11, the first separating plate 10 and level the second separating plate 9, the first separating plate 10 and every
There is interval, perpendicular position between same perpendicular and the bottom end of partition 11 and the top of the first separating plate 10 in plate 11
Between inlet tube 2 and escape pipe 4 and close to inlet tube 2, outlet tube 6 between the first separating plate 10 and second end cover 5, lean on
Nearly second end cover 5 and be connected to the bottom of cylinder 3,9 left end of the second separating plate connect with the top of the first separating plate 10, right end and
Second end cover 5 connects, and is evenly arranged with several through-holes on the first separating plate 10 and the second separating plate 9；
It is also connected with first baffle 8 and second baffle 7 on the inner wall of cylinder 3, first baffle 8 and second baffle 7 are horizontal and the
One baffle 8 is located at the lower section of second baffle 7, and 8 left end of first baffle is connect with the bottom end seal of partition 11, the right side of first baffle 8
There is interval between second end cover 5 and second end cover 5 and there is downward bending, 7 right end of second baffle and second end cover
There is interval between the left end of second baffle 7 and close partition 11 and partition 11 and there is downward bending in 5 connections.
The region that second separating plate 9, first baffle 8 and cylinder 3 surround is the first airflow channel, first baffle 8, second gear
Plate 7 and 3 area defined of cylinder are the second airflow channel, and the region that second baffle 7 and cylinder 3 surround is logical for third air-flow
Road.
In the present embodiment, inlet tube 2 is horizontally disposed, and outlet tube 6 and escape pipe 4 are vertically arranged；The top of inlet tube 2
Edge is 30mm at a distance from the top inner wall of cylinder 3, and inlet tube 2 is located at the end beveling of one end in cylinder 3, the angle of beveling
α is 45 degree, and it is 60mm that inlet tube 2, which is located at the end of one end in cylinder 3 and the shortest distance of the inner wall of cylinder 3, inlet tube 2
Caliber must guarantee that the flow velocity of refrigerant air-liquid mixture is 6m/s.If in end face of the inlet tube 2 inside cylinder 3 and cylinder 3
Wall it is concordant go deep into that the distance inside cylinder 3 is smaller or 2 top edge of inlet tube at a distance from 3 top inner wall of cylinder more than 50mm or
Refrigerant flow rates are less than normal, generally parabolically can fall into 3 bottom of cylinder by shape after refrigerant outflow inlet tube 2, liquid level can be because of system
The impact of cryogen and fluctuate aggravation, be unfavorable for the raising of gas-liquid separation effect.The setting of the inlet tube 2 of above-mentioned the present embodiment can
Guarantee to act on after the tangential direction of refrigerant air-liquid mixture from 3 inner wall of cylinder enters Flash Type economizer cylinder 3 in centrifugal force
Under with certain speed along 3 inner wall of cylinder formed annularly flow, with realize gas-liquid mixture first time separation.
The inner wall of first separating plate 10, the second separating plate 9 and cylinder 3 surrounds surge chamber, and the first separating plate 10 connects with cylinder 3
The edge connect is arc-shaped, and the top of the first separating plate 10 is in horizontal linear, and the second separating plate 9 is rectangle；First
The height of separating plate 10 is 30mm, and the aperture of through-hole is 5mm, and the spacing of two neighboring through-hole need to guarantee that refrigerant liquid flows through the
The mean flow rate of one separating plate 10 and all through-holes on the second separating plate 9 is 0.5m/s.If the first separating plate 10 and second
The aperture of through-hole on separating plate 9 is too small and/or hole count is very few, will result in refrigerant liquid and is not easily accessible surge chamber, can make
At liquid is lacked at outlet tube 6, to guarantee not lack liquid at outlet tube 6, need to increase the refrigerant level height in Flash Type economizer,
But it is easy to cause the first airflow channel to be occupied by a large amount of refrigerant air-liquid mixtures in this way and influences gas-liquid separation effect, finally lead
Flash Type economizer is caused to go out gas carrying liquid；If the aperture of the first separating plate 10 and the through-hole on the second separating plate 9 is excessive and/or hole
Number is excessive, is easy to cause surge chamber not have due buffer function, refrigerant air-liquid mixture flows fast speed, wherein mixing
Miscellaneous gaseous refrigerant has little time evolution and is just involved in outlet tube 6 and flows out economizer, causes to cause unit cold for liquid band gas
Amount decaying is equally also required to increase the liquid level of refrigerant in Flash Type economizer to guarantee that liquid is without gas out, final same
Sample will lead to out gas carrying liquid；Therefore, it is necessary to according to the actual situation to the total of the through-hole on the first separating plate 10 and the second separating plate 9
Sectional area is reasonably designed.Spot welding mode is taken to connect between first separating plate 10 and the second separating plate 9 and the inner wall of cylinder 3
It connects rather than is fully welded, be because spot welding is while it is not guaranteed that the position that need to be connected is fully sealed, but inherently due to surge chamber
By with multiple through-holes the first separating plate 10 and the space that forms of the second separating plate 9, by welding insufficient institute's shape at spot welding
At gap be equivalent to the number of openings of the first separating plate 10 and the second separating plate 9 and slightly increase, do not influence gas-liquid separation effect,
And spot welding can also save wlding and working hour, effectively reduce the manufacturing cost of Flash Type economizer.
When refrigerant air-liquid mixture passes through the first separating plate 10 and the second separating plate 9, by the first separating plate 10 and the
The blocking of two separating plates 9, flowing velocity slows down, fluctuating range reduces, the gaseous refrigerant contained in refrigerant air-liquid mixture
The refrigerant drop for having the more sufficient time to escape from the hole of the second separating plate 9, and separating in flow process is from
Surge chamber is flowed into the hole of two separating plates 9, refrigerant liquid slowly flows in surge chamber and flows out economy through outlet tube 6
Device, to realize second of separation of refrigerant air-liquid mixture.
The edge that partition 11 is connect with cylinder 3 is arc-shaped, and the bottom end of partition 11 is in horizontal linear, partition 11
Height need to guarantee that the flow velocity in the region between the inner wall that refrigerant gas passes through partition 11, the first separating plate 10 and cylinder 3 is 0.5
~ 1m/s sinks if the flow velocity of refrigerant gas is excessively high herein wherein the refrigerant drop swept along has been difficult to time enough
It lowers, in some instances it may even be possible to which the refrigerant drop for occurring being deposited to 9 surface of the second separating plate is rolled up by the air-flow of high flow velocities again
Enter the situation in air-flow；If refrigerant gas flow velocity is too low, illustrate that this regional space is larger, it is logical to may result in other air-flows
Road space is influenced final gas-liquid separation effect by compression, it is also possible to 3 diameter of cylinder be caused to become larger and influence Flash Type economy
The manufacturing cost of device.
The length of first baffle 8 need to guarantee that refrigerant gas passes through the inner wall institute of first baffle 8, second end cover 5 and cylinder 3
The flow velocity in the region of formation is 1 ~ 1.5m/s；It is respectively arranged with 2 on two sides that first baffle 8 is connect with the inner wall of cylinder 3 ~
4 holes are 100 ~ 200mm at a distance from partition 11 close to the hole of partition 11, and the shape in hole is semicircle, and the radius in hole is 6mm；
On the one hand aperture herein can be directly entered the second airflow channel along hole to avoid gas-liquid mixture, if it is most left in first baffle 8
End and 11 junction aperture of partition, a small amount of refrigerant air-liquid mixture of inlet tube 2 will be directly entered the second air-flow along this hole
On the other hand channel avoids on first baffle 8 generation hydrops phenomenon, due in the second airflow channel airflow direction be to the left,
And the droplet settling in gas is also the process gradually settled, and the right end that first end plate is arranged in hole is then easy to cause first gear
Hydrops on plate 8, hydrops are easy to be involved in air-flow again when air-flow is flowed up by the bending part of first baffle 8.
It is fully welded between partition 11 and the inner wall of cylinder 3, the inner wall spot welding of first baffle 8 and cylinder 3, and guarantees first baffle
The width in the gap between 8 and the inner wall of cylinder 3 is not more than 1mm, and refrigerant gas is in the second separating plate 9, first baffle 8 and cylinder
The flow velocity in the first airflow channel that body 3 is surrounded is 0.5 ~ 1m/s.The length of the bending of first baffle 8 need to guarantee refrigerant gas
The flow velocity in the region between inner wall that body passes through the end of the bending of first baffle 8, the second separating plate 9 and cylinder 3 is no more than 2m/
S, the angle beta of the bending of first baffle 8 are 90 degree；It can make refrigerant gas stream stream by the bending structure of 8 right end of first baffle
Dynamic direction deflects, and the refrigerant drop wherein swept along is made to be thrown to first baffle 8, barrel or due to the effect of inertia force
It is separated from refrigerant gas on two separating plates 9, so that refrigerant gas stream realizes third time gas-liquid separation.
2 ~ 4 holes are respectively arranged on two sides that second baffle 7 is connect with the inner wall of cylinder 3, hole is located proximate to
The port of escape pipe 4 and be 50 ~ 100mm at a distance from the port of escape pipe 4, the shape in hole is semicircle, and the radius in hole is
6mm；Why here aperture is because if selection 7 rightmost of second baffle and 5 junction aperture of second end cover, lower part
On a small quantity be mingled with drop air-flow be easy along this hole bypass enter third airflow channel；If opened in 7 left end of second baffle
Hole, since airflow direction is to the right, and the droplet settling in gas is also the process gradually settled, is easy to cause second baffle 7
Upper hydrops, hydrops are easy to be involved in gas again when air-flow enters escape pipe 4 and lead to gas carrying liquid out.
The inner wall spot welding of second baffle 7 and cylinder 3, and guarantee the width in the gap between second baffle 7 and the inner wall of cylinder 3
Degree is not more than 1mm, the second airflow channel and second baffle 7 and cylinder that first baffle 8, second baffle 7 and cylinder 3 are constituted
The flow velocity of refrigerant gas is 0.5 ~ 1m/s in the 3 third airflow channels constituted；The length of the bending of second baffle 7 needs to guarantee
Flow velocity of the refrigerant gas in the region between the inner wall of the end of the bending of second baffle 7, first baffle 8 and cylinder 3 is not
More than 2m/s, the angle of the bending of second baffle 7 is 90 degree.It can make refrigerant by the bending structure of 7 left end of second baffle
Air current flow direction deflects, and the refrigerant drop wherein swept along is made to be thrown to first baffle 8, due to the effect of inertia force
It is separated from refrigerant gas on two baffles 7, partition 11 or barrel.The length of second baffle 7 must guarantee that refrigerant gas is logical
The flow velocity for crossing the region between the inner wall of second baffle 7, partition 11 and cylinder 3 is 1 ~ 1.5m/s；Refrigerant gas stream is in the second gas
Circulation road and the equal slow flow of third airflow channel, but refrigerant gas stream 7 bending part of second baffle deflecting meeting so that refrigeration
Refrigerant drop in agent air-flow separates under the action of inertia force with refrigerant gas stream, and refrigerant gas stream is in 7 folding of second baffle
The deflecting twice of crook realizes the 4th time and the 5th gas-liquid separation.
The inner wall spot welding of first baffle 8 and second baffle 7 and cylinder 3 is equally beneficial for gas-liquid separation, and save wlding and
Working hour reduces the manufacturing cost of Flash Type economizer.
The bending radius of the bend pipe of escape pipe 4 is 90 degree, and the horizontal tube of escape pipe 4 is located in cylinder 3, and horizontal tube is upper
Edge is 30mm at a distance from the top inner wall of cylinder 3, and the length of horizontal tube is 70mm, and the air inlet of horizontal tube is towards second end
Lid 5 and at a distance from the inner wall of second end cover 5 be 120mm, refrigerant gas escape pipe 4 flow velocity be not higher than 6m/s；So
The direction that the flow velocity of gas in escape pipe 4 can be reduced and change gas in escape pipe 4 is set, to guarantee that refrigerant gas is flowing
Last time gas-liquid separation is carried out before Flash Type economizer, out to ensure outlet without liquid.
Refrigerant air-liquid mixture can be with centrifugal, again Flash Type economizer of the present embodiment suitable for refrigeration unit
The various ways such as power sedimentation, deflecting carry out sufficient gas-liquid separation, reach outlet under the premise of not using material filling type demister
Without the effect of liquid, while guaranteeing that fluid resistance loss of the refrigerant in Flash Type economizer reduces to the greatest extent, so as to avoid
The refrigerant gas for entering compressor gas supplementing opening from Flash Type economizer gas outlet causes shadow with reliability service of the liquid to compressor
It rings, while significantly improving cooling capacity and operational efficiency again, and reduce the manufacturing cost of Flash Type economizer.
The shape in hole of the present invention on first baffle 8 and second baffle 7 the Flash Type economizer of refrigeration unit
The hole on first baffle 8 and second baffle 7 is set other shapes, such as triangle by the semicircle being not limited in the present embodiment
Shape and rectangular also possible, only tri-angle-holed and square hole sectional area need to be with the sectional area of semi-circular hole in the present embodiment
Quite.
In the description of the present invention, it should be noted that term "top", "bottom", "lower", "left", "right", "vertical", " water
It is flat ", the orientation or positional relationships of the instructions such as "inner" be to be based on the orientation or positional relationship shown in the drawings, be merely for convenience of describing
The present invention and simplified description, rather than the device or element of indication or suggestion meaning must have a particular orientation, with specific
Orientation construction and operation, therefore be not considered as limiting the invention.In addition, term " first ", " mat woven of fine bamboo strips two " are only used for describing
Purpose is not understood to indicate or imply relative importance.
Specific examples are applied in the present invention, and principle and implementation of the present invention are described, above embodiments
Illustrate to be merely used to help understand method and its core concept of the invention；At the same time, for those skilled in the art, according to
According to thought of the invention, there will be changes in the specific implementation manner and application range.In conclusion the content of the present specification
It should not be construed as limiting the invention.
Claims (8)
1. being suitable for the Flash Type economizer of refrigeration unit, it is characterised in that: including horizontal cylinder, cylinder one end setting
There is first end cover, the other end to be provided with second end cover, be provided with inlet tube, outlet tube and escape pipe on the cylinder, it is described into
Close to the first end cover and close to the top of the cylinder, the escape pipe is located at the top of the cylinder and close to institute liquid pipe
State second end cover；Be connected on the inner wall of the cylinder partition, the first separating plate and level the second separating plate, described first point
It is located between the bottom end of same perpendicular and the partition and the top of first separating plate from plate and the partition and exists
Interval, the perpendicular is between the inlet tube and the escape pipe and close to the inlet tube, the outlet tube position
Between first separating plate and the second end cover, close to the second end cover and being connected to the bottom of the cylinder, institute
State that second separating plate one end is connect with the top of first separating plate, the other end is connect with the second end cover, described first
Several through-holes are evenly arranged on separating plate and second separating plate,
First baffle and second baffle, the first baffle and the equal water of the second baffle are also connected on the inner wall of the cylinder
The flat and described first baffle is located at the lower section of the second baffle, the bottom end seal company of described first baffle one end and the partition
It connects, the other end of the first baffle has interval between the second end cover and the second end cover and has downward
Bending, described second baffle one end connect with the second end cover, the other end of the second baffle and close to the partition,
There is interval between the partition and there is downward bending.
2. the Flash Type economizer according to claim 1 suitable for refrigeration unit, it is characterised in that: the inlet tube water
Flat setting, the outlet tube and the escape pipe are vertically arranged.
3. the Flash Type economizer according to claim 2 suitable for refrigeration unit, it is characterised in that: the inlet tube
Top edge is 20 ~ 50mm at a distance from the top inner wall of the cylinder, and the inlet tube is located at the end of the intracorporal one end of the cylinder
Portion's beveling, the angle of the beveling are 30 ~ 60 degree, the inlet tube be located at the intracorporal one end of the cylinder end and the cylinder
Inner wall the shortest distance be 40 ~ 80mm, the caliber of the inlet tube must guarantee refrigerant air-liquid mixture flow velocity be 4 ~ 8m/
s。
4. the Flash Type economizer according to claim 2 suitable for refrigeration unit, it is characterised in that: the escape pipe
The bending radius of bending part is 90 degree, and the horizontal component of the escape pipe is located in the cylinder, and the water of the escape pipe
The top edge of flat part is 20 ~ 50mm, the length of the horizontal component of the escape pipe at a distance from the top inner wall of the cylinder
For 50 ~ 100mm, the air inlet of the horizontal component of the escape pipe towards the second end cover and in the second end cover
The distance of wall is 100 ~ 150mm, and refrigerant gas is not higher than 6m/s in the flow velocity of escape pipe.
5. the Flash Type economizer according to claim 1 suitable for refrigeration unit, it is characterised in that: first separation
The inner wall of plate, second separating plate and the cylinder surrounds surge chamber, the side that first separating plate is connect with the cylinder
Edge is arc-shaped, and the top of first separating plate is in horizontal linear, and second separating plate is rectangle；Described
The height of one separating plate is 20 ~ 50mm, and the aperture of the through-hole is 3 ~ 8mm, and the spacing of the two neighboring through-hole need to guarantee to make
Cryogen liquid flows through the mean flow rate of first separating plate and all through-holes on second separating plate in 0.3 ~ 0.7m/s
Between.
6. the Flash Type economizer according to claim 1 suitable for refrigeration unit, it is characterised in that: the partition and institute
The edge for stating cylinder connection is arc-shaped, and the bottom end of the partition is in horizontal linear, and the height of the partition needs to guarantee
Refrigerant gas by the inner wall of the partition, first separating plate and the cylinder be formed by region flow velocity be 0.5 ~
1m/s。
7. the Flash Type economizer according to claim 1 suitable for refrigeration unit, it is characterised in that: the first baffle
Length need to guarantee that refrigerant gas is formed by region by the inner wall of first baffle, the second end cover and the cylinder
Flow velocity is 1 ~ 1.5m/s；2 ~ 4 holes are respectively arranged on two sides that the first baffle is connect with the inner wall of the cylinder,
Be 100 ~ 200mm with the partition at a distance from close to the hole of the partition, the shape in the hole be semicircle, triangle or
It is rectangular；It is fully welded, the inner wall spot welding of the first baffle and the cylinder, and guarantees between the partition and the inner wall of the cylinder
The width in the gap between the first baffle and the inner wall of the cylinder is not more than 1mm, and refrigerant gas is at described second point
The flow velocity in the first airflow channel surrounded from plate, the first baffle and the cylinder is 0.5 ~ 1m/s；The first gear
The length of the bending of plate need to guarantee end, second separating plate and the institute of bending of the refrigerant gas by the first baffle
The inner wall for stating cylinder is formed by the flow velocity in region and is no more than 2m/s, and the angle of the bending of the first baffle is 60 ~ 120 degree.
8. the Flash Type economizer according to claim 1 suitable for refrigeration unit, it is characterised in that: the second baffle
2 ~ 4 holes are respectively arranged on two sides connecting with the inner wall of the cylinder, close to the described of the port of the escape pipe
Hole is 50 ~ 100mm at a distance from the port of the escape pipe, and the shape in the hole is semicircle, triangle or rectangular；Described
The length of two baffles must guarantee the area between the inner wall that refrigerant gas passes through the second baffle, the partition and the cylinder
The flow velocity in domain is 1 ~ 1.5m/s；The inner wall spot welding of the second baffle and the cylinder, and guarantee the second baffle with it is described
The width in the gap between the inner wall of cylinder is not more than 1mm, and the first baffle, the second baffle and the cylinder are constituted
The second airflow channel and the third airflow channel that is constituted of the second baffle and the cylinder in refrigerant gas stream
Speed is 0.5 ~ 1m/s；The length of the bending of the second baffle need to guarantee the end of bending of the refrigerant gas in the second baffle
The flow velocity in region between the inner wall at end, the first baffle and the cylinder is no more than 2m/s, the folding of the second baffle
Curved angle is 60 ~ 120 degree.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811338894.XA CN109140836A (en) | 2018-11-12 | 2018-11-12 | Flash Type economizer suitable for refrigeration unit |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811338894.XA CN109140836A (en) | 2018-11-12 | 2018-11-12 | Flash Type economizer suitable for refrigeration unit |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN109140836A true CN109140836A (en) | 2019-01-04 |
Family
ID=64808207
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201811338894.XA Withdrawn CN109140836A (en) | 2018-11-12 | 2018-11-12 | Flash Type economizer suitable for refrigeration unit |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN109140836A (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN110307742A (en) * | 2019-07-26 | 2019-10-08 | 杭州中泰深冷技术股份有限公司 | The plate-fin heat exchanger and heat-exchange method of multi-stage separation |
| CN111721037A (en) * | 2019-03-22 | 2020-09-29 | 浙江盾安机电科技有限公司 | Economizer component and refrigerating unit with same |
| CN112082294A (en) * | 2020-09-22 | 2020-12-15 | 浙江国祥股份有限公司 | Gas-liquid separator with vertical partition plate |
| CN115143669A (en) * | 2022-06-29 | 2022-10-04 | 浙江国祥股份有限公司 | Flash evaporation type economizer with ball float valve and control method thereof |
| CN115479418A (en) * | 2022-08-04 | 2022-12-16 | 宁波拓普集团股份有限公司 | Gas-liquid separator for automobile air conditioner heat management system |
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| CN102914101A (en) * | 2012-10-24 | 2013-02-06 | 重庆美的通用制冷设备有限公司 | Flash type economizer |
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Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111721037A (en) * | 2019-03-22 | 2020-09-29 | 浙江盾安机电科技有限公司 | Economizer component and refrigerating unit with same |
| CN111721037B (en) * | 2019-03-22 | 2022-08-30 | 浙江盾安机电科技有限公司 | Economizer component and refrigerating unit with same |
| CN110307742A (en) * | 2019-07-26 | 2019-10-08 | 杭州中泰深冷技术股份有限公司 | The plate-fin heat exchanger and heat-exchange method of multi-stage separation |
| CN112082294A (en) * | 2020-09-22 | 2020-12-15 | 浙江国祥股份有限公司 | Gas-liquid separator with vertical partition plate |
| CN115143669A (en) * | 2022-06-29 | 2022-10-04 | 浙江国祥股份有限公司 | Flash evaporation type economizer with ball float valve and control method thereof |
| CN115143669B (en) * | 2022-06-29 | 2024-06-04 | 浙江国祥股份有限公司 | Flash type economizer with float valve and control method thereof |
| CN115479418A (en) * | 2022-08-04 | 2022-12-16 | 宁波拓普集团股份有限公司 | Gas-liquid separator for automobile air conditioner heat management system |
| CN115479418B (en) * | 2022-08-04 | 2024-05-10 | 宁波拓普集团股份有限公司 | Gas-liquid separator for automobile air conditioner thermal management system |
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Address after: 116630, No. 106, Liaohe East Road, Dalian economic and Technological Development Zone, Liaoning Applicant after: Iceberg cold and hot technology Co.,Ltd. Address before: 116630, No. 106, Liaohe East Road, Dalian economic and Technological Development Zone, Liaoning Applicant before: DALIAN REFRIGERATION Co.,Ltd. |
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Application publication date: 20190104 |