CN107208986B - Including liquid-refrigerant distributing device heat exchanger - Google Patents
Including liquid-refrigerant distributing device heat exchanger Download PDFInfo
- Publication number
- CN107208986B CN107208986B CN201680007397.4A CN201680007397A CN107208986B CN 107208986 B CN107208986 B CN 107208986B CN 201680007397 A CN201680007397 A CN 201680007397A CN 107208986 B CN107208986 B CN 107208986B
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- Prior art keywords
- fin
- heat exchanger
- overflow openings
- aperture
- distributor
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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
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
- F25J3/02—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
- F25J3/04—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air
- F25J3/04636—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air using a hybrid air separation unit, e.g. combined process by cryogenic separation and non-cryogenic separation techniques
-
- 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
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J5/00—Arrangements of cold exchangers or cold accumulators in separation or liquefaction plants
- F25J5/002—Arrangements of cold exchangers or cold accumulators in separation or liquefaction plants for continuously recuperating cold, i.e. in a so-called recuperative heat exchanger
- F25J5/005—Arrangements of cold exchangers or cold accumulators in separation or liquefaction plants for continuously recuperating cold, i.e. in a so-called recuperative heat exchanger in a reboiler-condenser, e.g. within a column
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D9/00—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
- F28D9/0062—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits for one heat-exchange medium being formed by spaced plates with inserted elements
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F9/00—Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
- F28F9/02—Header boxes; End plates
- F28F9/026—Header boxes; End plates with static flow control means, e.g. with means for uniformly distributing heat exchange media into conduits
- F28F9/027—Header boxes; End plates with static flow control means, e.g. with means for uniformly distributing heat exchange media into conduits in the form of distribution pipes
- F28F9/0273—Header boxes; End plates with static flow control means, e.g. with means for uniformly distributing heat exchange media into conduits in the form of distribution pipes with multiple holes
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F9/00—Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
- F28F9/02—Header boxes; End plates
- F28F9/026—Header boxes; End plates with static flow control means, e.g. with means for uniformly distributing heat exchange media into conduits
- F28F9/0278—Header boxes; End plates with static flow control means, e.g. with means for uniformly distributing heat exchange media into conduits in the form of stacked distribution plates or perforated plates arranged over end plates
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F9/00—Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
- F28F9/22—Arrangements for directing heat-exchange media into successive compartments, e.g. arrangements of guide plates
-
- 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
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J2250/00—Details related to the use of reboiler-condensers
- F25J2250/02—Bath type boiler-condenser using thermo-siphon effect, e.g. with natural or forced circulation or pool boiling, i.e. core-in-kettle heat exchanger
-
- 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
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J2250/00—Details related to the use of reboiler-condensers
- F25J2250/04—Down-flowing type boiler-condenser, i.e. with evaporation of a falling liquid film
-
- 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
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J2290/00—Other details not covered by groups F25J2200/00 - F25J2280/00
- F25J2290/32—Details on header or distribution passages of heat exchangers, e.g. of reboiler-condenser or plate heat exchangers
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
This heat exchanger (2) includes :-parallel-plate (11,12), these parallel-plates limit the liquid-refrigerant passage (20) of (X) in a longitudinal direction, and-the fin (21,22 that extends in each access (20) in the transverse direction (Y) orthogonal with longitudinal direction (X), 23,24), each fin (21,22,23,24) there is the aperture for liquid refrigerant flowing.At least one low portion of at least one fin (21,22,23,24) and the plate being fixed on the low portion define the assignment channel for guiding the liquid refrigerant in the transverse direction (Y).Aperture at least one described fin (21,22,23,24) is formed by the overflow openings in the upper part.When the hydraulically full refrigerant of the or each assignment channel, which flows through these overflow openings.
Description
The present invention relates to a kind of heat exchanger, which includes being configured for distributing liquid refrigerant handing in heat
Distributor in parallel operation.The heat exchanger particularly can be to be made in the column for carrying out air separation by low temperature distillation
Evaporator, to ensure column liquid in containers (such as liquid by the heat exchange with heat production gas (such as air or nitrogen)
Oxygen) evaporation.
The present invention is particularly used for cryogenic gas separation, especially for producing the Cryogenic air point of the gaseous state oxygen of pressurization
In field from (known with the acronym " ASU " for air gas separation unit).Particularly, the present invention can apply
In the heat exchanger for evaporating liquid flow such as oxygen, nitrogen and/or argon and the heat exchange with gas.
If the heat exchanger is located in the container of distillation column, it may be constructed the evaporator as thermal siphon operation
(wherein immersing the exchanger along the liquid bath that the column declines) or by directly being supplied by the liquid fallen in the column
Film evaporation and/or pass through recirculation pump run evaporator.
Technology currently used for these phase transformation exchangers is that have the technology of the aluminium exchanger of brazing sheet and fin, this causes
The device of the highly compact of big exchange area is provided.These exchangers include plate, are inserted into fin between the plates, are consequently formed
The stacking of evaporation flow paths and condensation pass, which is intended for evaporation liquid refrigerant and the alternate path is purport
For condensing heat production gas.
WO-A-2011110782 describes a kind of distributor, which includes limiting for liquid refrigerant
The parallel-plate of access, and extend in each access and there is the aperture for distributing liquid refrigerant in a lateral direction
Several fins.
However, the distribution of liquid refrigerant in a lateral direction is not substantially uniformity in the distributor of the prior art
's.When the region of exchanger does not receive enough liquid refrigerants, since dry blowing is sent out, the solid deposits of impurity may be sent out
It is raw.The solid deposits of such impurity produce the risk of explosion under certain operating conditions of heat exchanger.
Known solution is by the puncture aperture group in the parallel-plate of distributor from document EP-A-0130122
At to ensure liquid refrigerant along the rough predistribution of the access for the liquid.However, along exchanger arrangement
The quantity in aperture is limited, and so as not to complicate production or structure is made to die down, and makes the effect of the allocation criterion of liquid
Fruit is still insufficient.
The purpose of the present invention completely or partially solves the above problems specifically by distributor is provided, in this point
Distribution with liquid refrigerant in device is as uniform as possible.
For this purpose, the heat exchanger is configured for heat from least the purpose of the present invention is a kind of heat exchanger
A kind of heat production fluid such as nitrogen is transmitted at least one cryogenic fluid such as oxygen, which includes at least peace parallel to each other
The plate of row, to limit conduction liquid body on the longitudinal direction for being configured for generally extending in vertical direction during operation
The First Series access of refrigerant, each access is limited between two continuous slabs, and is configured for generally at this
Longitudinal direction uploads the second series access of artificial delivery hot fluid, and each access is limited between two continuous slabs, second system
The access of column is inserted between the two paths of the First Series；At least one is used for the entrance of liquid refrigerant, the entrance
It is configured as that only the liquid refrigerant being poured into the access of the First Series；And only exist in the upper end of the exchanger
Distributor in the access of the First Series, the distributor include
The fin generally extended in one of the First Series or each access in a lateral direction, the transverse direction
It is orthogonal with the longitudinal direction and parallel with these plates, each passageways house of First Series phase each other on the longitudinal direction
After several fins, each fin have is configured as allow liquid refrigerant flow aperture；
At least one fin has upper part and low portion, when the distributor is in operation and the longitudinal direction
When extending on the vertical direction, the height of the upper part is greater than the height of the low portion,
At least one described low portion and the plate being fixed at least one described low portion limit at least
One is configured for the assignment channel of the conduction liquid cryogen in the transverse direction,
The aperture of at least one fin is formed by the overflow openings being located at least one described upper part, these
Overflow openings are configured such that the liquid refrigerant is via this when at least one described assignment channel hydraulically full refrigerant
A little overflow openings flowings.
In other words, the or each assignment channel forms a type of slot, and the slot is in these overflow openings and the lower part
Extend between part and the crosspoint for the plate being fixed on this low portion.When the distributor in operation, should or
Each assignment channel is generally horizontal.
Therefore, the or each assignment channel is with the permission that cooperates of the overflow openings of the one or more fin in the transverse direction side
The liquid refrigerant is distributed as homogeneously as possible upwards, and the solid deposits of impurity in the heat exchanger are restricted or prevented in this
Risk.
These plates extend on two dimensions (length and width) on the longitudinal direction and the transverse direction respectively.Every
In a access, these fins have elongated form and extend in the width of two continuous slabs (transverse direction).
When the distributor is in operation, which is vertical.The liquid refrigerant is under gravity generally
It is flowed on the longitudinal direction.Therefore, which generally vertically flows on descent direction.
Variant according to the present invention, the distributor may include the plate quantity greater than 20 or even greater than 100.Therefore,
It is folded that these plates form sheetpile, defines the access for the liquid refrigerant between the plates, in some cases be used for
The conduit of the heat production fluid replaces.The distributor can have greater than 10 or even greater than 50 liquid refrigerant number of vias
Amount.
In operation, which passes through the distributor.The distributor, which includes, i) is configured for the liquid
The upstream portion and ii of the entrance of refrigerant) be configured for the liquid refrigerant outlet downstream part.These fins exist
Extend between the upstream portion and the downstream part.
Variant according to the present invention, each access have flat parallelepiped form.Since each access is with flat
Flat shape, so the distance between two continuous slabs is small compared with the length and width of each continuous slab.Preferably,
The all or some of these fins extend to next plate from a plate.In other words, these fins are contacted with two plates.It is this
Construction allows in these fin brazeds to two plates, and which increase the mechanical strengths of the distributor.
In this application, term " ... direction on " refer to it is substantially parallel or basic with another direction or plane
Upper conllinear direction.
According to one embodiment of present invention, the volume of corresponding assignment channel be total volume less than 15%, it is preferably small
In 10%, which is delimited by following item:
- i) fin with overflow openings,
- ii) it is fixed to the plate on the low portion of the fin with overflow openings, and
- iii) be located at the fin with overflow openings fast upstream fin.
Therefore, because the volume of the assignment channel, these fins with overflow openings cannot cause too big load to be damaged
It loses.Low-load loss avoids the flowing for reducing the liquid refrigerant by these fins with overflow openings, this allows this
The optimum apjustment of flowing.Therefore, these have the function of that the fin of overflow openings is completed to distribute the liquid refrigerant, only generate low
Load loss.Each assignment channel is by least one low portion and by being fixed at least one described low portion
Plate limits.
According to an embodiment of the invention, these overflow openings are evenly distributed on fin in the transverse direction.
Therefore, equally distributed overflow openings allow the maximum distributing uniformity of the liquid refrigerant.Alternatively, certain
A little overflow openings can be unevenly distributed in the transverse direction.
According to one embodiment of present invention, aperture opening ratio, the aperture opening ratio include
It is located at the gross area of the overflow openings in the fin with overflow openings as molecule, and
The gross area in the face of the fin with overflow openings as denominator,
It is between 10% and 50%, preferably between 20% and 40%.
Therefore, the load loss that such aperture opening ratio helps to make the fin by these with overflow openings to generate is minimum
Change, while ensuring enough flowings in the distributor.
According to one embodiment of present invention, each overflow openings have in 1.5mm2With 10.0mm2Between, preferably exist
2.0mm2With 5.0mm2Between area.
Therefore, such area avoids floods each overflow openings completely, this helps not reduce through each fin
The flowing of liquid refrigerant.
Variant according to the present invention, some overflow openings have for example circular form of ellipse.Therefore, such shape mentions
Progressively increased overflow openings width is supplied, when the flowing of liquid refrigerant increases, which has limited the liquid refrigerants
Highly.
Variant according to the present invention, some overflow openings have the triangle shape for being directed toward at least one low portion
Formula.Therefore, such shape provides progressively increased overflow openings width, when the flowing of liquid refrigerant increases, this limit
The height of the liquid refrigerant is made.
According to one embodiment of present invention, between being measured in the transverse direction between two continuous overflow openings
Every being between 1mm and 6mm.
Therefore, such interval assists in ensuring that liquid refrigerant evenly distributing in the transverse direction, while making to pass through this
The load loss that a little fins with overflow openings generate minimizes.
Variant according to the present invention, the interval is constant for the overflow openings of at least one fin.
Therefore, such interval facilitates the distributing uniformity for making the liquid refrigerant in transverse direction maximization.
In one embodiment of the invention, in i) overflow openings and ii) it is fixed at least one described low portion
On plate between minimum range between 1mm and 4mm, for corresponding fin overflow openings it is most of or all, should
Minimum range is preferably identical.
Therefore, such minimum range allows assignment channel to have relatively large volume, this allows to limit in the distributor
The fin with overflow openings quantity.
According to one embodiment of present invention, several fins are with the corresponding upper part with overflow openings.
In other words, there are several allocated phases of the liquid refrigerant, this help keeps the uniformity of this distribution maximum
Change.
According to one embodiment of present invention, these overflow openings being present in fin are relative to being present in adjacent fins
In these overflow openings in the transverse direction offset orientation.
Therefore, such offset between overflow openings helps to increase point of the liquid refrigerant in the transverse direction
With uniformity.
According to one embodiment of present invention, described between these overflow openings being present in two adjacent fins
Offset accounts between the 40% and 60% of the length at the interval.
In other words, the overflow openings of the continuous fin of two be arranged in being substantially offset from one another on the longitudinal direction.
Therefore, the value of such offset between overflow openings helps point for making the liquid refrigerant in the transverse direction
It is maximized with uniformity.
According to one embodiment of present invention, at least one fin has flat pattern and extends until described two
Continuous slab and each of described two continuous slabs are obliquely run out to, so as to vertical with these plates and the transverse direction
Plane in section in form closed bevel, the oblique angle preferably between 30 ° and 60 °, further preferably at 40 ° and
Between 50 °.
Therefore, such flat inclined fin occupies relatively small space and is readily attached on these plates.
According to one embodiment of present invention, each fin, which has, is parallel to the longitudinal direction between 4mm and 10mm
Length, and each fin has the width for being parallel to the transverse direction between 4mm and 10mm, and each fin being capable of example
Such as there is equal length and width.
Therefore, such length and width allows a large amount of fin to be incorporated in the distributor, and which increase the liquid systems
The distributing uniformity of cryogen.
Variant according to the present invention, each fin have for example by being brazed the fixed part being fixed on plate.
Therefore, such fixed part allows each fin to be attached on these plates in a simple manner.
Variant according to the present invention, one and preferably each overflow openings are by openings (through orifice)
It limits.Alternatively, at least one overflow openings can be by extending until the recess at the edge of corresponding fin limits.
According to one embodiment of present invention, which includes at least one fin, which has
Aperture and the upstream for being placed on fin of the one or more with overflow openings, these apertures are distributed in the transverse direction
On, the quantity of the overflow openings of each fin is 3 times bigger than the quantity in the aperture of each fin, preferably 5 times big.
Therefore, these fins with aperture can complete control into the distributor by generating high load loss
The function of the flowing of liquid refrigerant, and these have the fin for overflowing opening complete while generating only low-load loss on the contrary
At distribution function.Which has limited the quantity for the component being mounted in the distributor, because due to the fin with aperture,
It does not need to provide perforation stick (such as in WO-A-2011110782) to generate high load loss.
Variant according to the present invention, at least two fins have aperture, and the quantity in the aperture of each fin is being from upstream to
Increase on the direction in downstream.
Therefore, these fins with aperture allow access into the best control of the flowing of the liquid refrigerant of the distributor
System.
Variant according to the present invention, be located at most upstream the fin with aperture transverse direction on measure, two
Being located at interval between 40mm and 60mm between a continuous aperture, and in the transverse direction for the fin with aperture for being located at most downstream
Measured on direction, being located at interval between 6mm and 20mm between two continuous apertures.
Therefore, fin with aperture positioned at most upstream has least aperture, and has hole positioned at most downstream
The fin of mouth has most apertures, these fins with overflow openings are in the fin with aperture positioned at most downstream
Downstream.
Therefore, the load loss that the fin by these with aperture generates is from upstream to downstream and reduces, and the liquid refrigerating
The distributing uniformity of agent increases.
Variant according to the present invention, at least one fin, other than these overflow openings, can have at least one
The purge hole arranged at the bottom of the low portion.Then, the assignment channel is by several part shapes being split into two halves by purge hole
At the liquid refrigerant can flow through the purge hole.Such purge hole allows the emptying of the assignment channel.Advantageously, should
Or the area of each purge hole is less than the area of overflow openings.Therefore, there is relatively low flow velocity by the flowing of the purge hole,
This avoidance breakout passes through the flowing of each overflow openings close to the purge hole.
Variant according to the present invention, for giving these openings of fin or the gross area of these overflow openings in the longitudinal direction
Increase on direction, is preferably increased by increasing quantity and/or the area that these are open.
In this way, the liquid decline in the distributor is remoter, and the spacing between these openings is smaller.Start
When, if liquid poorly distributes, it is forced laterally to recycle the adjacent apertures until same fin.It is open at two
Between distance it is bigger, reallocation on the width is more effective.
Secondly, the purpose of the present invention is a kind of for distributing the distribution method of liquid refrigerant, this point in a heat exchanger
Method of completing the square the following steps are included:
Implement distributor according to the present invention,
Liquid refrigerant is transmitted in each access and generally in a longitudinal direction,
Allow liquid refrigerant via the fin with aperture orifice flow,
Each assignment channel is filled, so that liquid refrigerant is flowed via these overflow openings.
The invention further relates to a kind of heat exchanger, which is configured as heat from least one heat production fluid
(such as nitrous oxide) is transmitted at least one cryogenic fluid (such as oxygen), which includes at least one heat exchange list
Member, at least one liquid refrigerant entrance, the heat exchanger are characterized in that including according to any one of preceding claims institute
The distributor stated, the distributor are arranged to for liquid refrigerant to be supplied to the heat exchange unit.
Therefore, such heat exchanger limits or avoids the risk of the solid deposits of impurity in the heat exchanger, with
And the risk therefore exploded under some operating conditions.
Above-mentioned embodiment and variant can in isolation or with it is any technically can the combination of property use.
From being described below of only providing as non-limiting examples and with reference to attached drawing, it will be clear that ground understand the present invention and
Its advantage will occur, in the drawings:
- Fig. 1 is a part of the distributor of first embodiment according to the present invention perpendicular to the flat of transverse direction
Diagrammatic section view in face；
- Fig. 2 is diagrammatic section view of the distributor part in the plane II in Fig. 1 in Fig. 1, and plane II is flat
Row is in the longitudinal direction and transverse direction；
- Fig. 3 be include first embodiment according to the present invention distributor heat exchanger a part vertical
Diagrammatic section view in the plane of the transverse direction；
- Fig. 4 is analogous to the view of Fig. 1, shows the function of the distributor of Fig. 3；
- Fig. 5 is analogous to the view of Fig. 2, shows the function of the distributor of Fig. 3；
- Fig. 6 and Fig. 7 is the view for being analogous respectively to Fig. 1 and Fig. 2, shows point of second embodiment according to the present invention
A part with device；
- Fig. 8 and Fig. 9 is the view for being analogous respectively to Fig. 1 and Fig. 2, shows point of third embodiment according to the present invention
A part with device；
- Figure 10 is analogous to the view of Fig. 1, shows one of the distributor of fourth embodiment according to the present invention
Point；
- Figure 11 is analogous to the view of Figure 10, shows one of the distributor of fifth embodiment according to the present invention
Point；
- Figure 12 is analogous to the view of Figure 10, shows one of the distributor of sixth embodiment according to the present invention
Point；
- Figure 13 is analogous to the view of Fig. 1, shows one of the distributor of seventh embodiment according to the present invention
Point；
- Figure 14 is analogous to the view of Fig. 1, shows one of the distributor of the 8th embodiment according to the present invention
Point；And
- Figure 15 shows distribution method according to the present invention.
Fig. 1,2 and 3 show distributor 1, which is configured for liquid refrigerant F1 (in such case
Lower liquid oxygen) it is assigned in heat exchanger 2.Heat exchanger 2 is configured for heat from heat production fluid F2 (in this gaseous nitrogen atmosphere)
It is transmitted to the cryogenic fluid (in this oxygen).Before transmitting heat, liquid refrigerant F1 (Fig. 3) is in the appearance for belonging to heat exchanger 2
It receives in slot 3.
Distributor 1 includes the plate 11,12,13,14 and equivalent of arrangement parallel to each other.Distributor 1 includes being equal to greatly
About 200 stacking plate quantity.Each of these plates 11,12,13,14 prolong on two dimensions (length and width) respectively
It stretches, the two dimensions are respectively defined in longitudinal direction X and transverse direction Y.
Transverse direction Y is orthogonal with longitudinal direction X and parallel with these plates 11,12,13,14.When distributor 1 is operating
When middle, longitudinal direction X is vertical.Liquid refrigerant F1 generally flows on longitudinal direction X under gravity.Therefore, liquid
Refrigerant F1 generally vertically flows on descent direction.
These plates 11,12,13,14, which are arranged to limit, is configured for the conduction liquid body generally on longitudinal direction X
The access 20,30 and equivalent of refrigerant F1.Each access 20 or 30 is limited between two continuous slabs 11,12,13,14.
Each access 20,30 has flat parallelepiped form.It is at a distance between two continuous slabs 11 and 12 and each continuous
It is small that the length (on the X of direction) of plate 11 or 12 is compared with width (in the Y direction).In heat exchanger 2, it to be used for liquid system
The access 20,30 of cryogen F1 replaces with the access (not shown) of the flat parallelepiped form for the heat production fluid.
Distributor 1 further includes fin 21,22,23,24 and 31,32,33,34, these fins are respectively in each access 20
With 30 in generally extend in transverse direction Y.Fin 21,22,23,24 extends in access 20, and fin 31,32,33,34
Extend in access 30.In each access 20 or 30, fin 21,22,23,24,31,32,33 and 34 has elongated form simultaneously
And extend in the transverse direction Y of two continuous slabs 11 and 12 or 13 and 14.
Each fin 21,22,23,24,31,32,33 or 34 has flat pattern and extends until two continuous slabs
11 and 12 or 13 and 14.Each fin 21 or equivalent obliquely run out to every in the two continuous slabs 11 and 12 or 13 and 14
One, to form closed bevel in the section in the plane (plane of Fig. 1 herein) vertical with these plates and transverse direction Y
A21.Oblique angle A21 is 45 ° herein.
Each fin 21 or equivalent have the length X21 for being parallel to longitudinal direction X, which is equal to 5mm herein.Each
Fin 21 or equivalent have the width Y21 for being parallel to transverse direction Y, which is equal to 5mm herein and is therefore equal to length
X21.Each fin 21 or equivalent have flat herein and are fixed to consolidating in respective plate 11 or equivalent by soldering
Determine part 21.5.All fins 21,22,23,24 extend from a plate 11 until next plate 12.In other words, these wings
Piece 21,22,23,24 is contacted with two plates 11 and 12.These fins 21,22,23,24 are soldered on the two plates 11 and 12.
Each access 20 or 30 accommodates four fins herein, is 21,22,23,24 and 31,32,33,34 respectively, these
Fin follows one another on longitudinal direction X.Each fin 21 or equivalent have aperture 40, these apertures are configured to permit liquid
Cryogen F1 is flowed by corresponding fin 21 or equivalent.
In the example of Fig. 1 to Fig. 5, each fin 21,22,23,24,31,32,33 or 34 has 21.1 and of upper part
Equivalent and low portion 21.2 and equivalent.(Fig. 4 and Fig. 5), upper part 21.1 when the distributor is in operation
Height be greater than low portion 21.2 height.
Each low portion 21.2 or equivalent, and the respective plate 11 or equivalent that are fixed on low portion 21.2
Define the assignment channel 42 for being configured for the conduction liquid cryogen F1 in transverse direction Y.
In the example of Fig. 1 to Fig. 5, the aperture 40 of each fin 21 or equivalent is by being located at each respective upper part
21.1 or equivalent in overflow openings 40 formation.All fins 21 and equivalent are with corresponding upper with overflow openings 40
Portion part 21.1 and equivalent.For significantly reason is understood, all overflow openings 40 are not marked on Fig. 1 to Fig. 5.
The overflow openings 40 of each fin 21 or equivalent are configured such that when the hydraulically full refrigerant of assignment channel 42
When F1, liquid refrigerant F1 is flowed via overflow openings 40.
All overflow openings 40, which all have, herein is directed toward the triangular shaped of each respective lower part 21.2.These overflows
Opening 40 is evenly distributed on corresponding fin 21 or equivalent in transverse direction Y at this.
The interval D 40 between two continuous overflow openings 40 measured in the transverse direction be herein it is constant and
And 4mm is equal to for the overflow openings 40 of each fin 21 or equivalent.
In addition, in i) overflow openings 40 and ii) it is fixed to the most narrow spacing between the plate 11 on respective lower part 21.2
It is equal to 3mm from H40.This minimum range H40 is identical (permanent for all overflow openings 40 of corresponding fin 21 or equivalent
Fixed).
In the example of Fig. 1 to 5, these overflow openings 40 for being present in fin 21 are relative to being present in adjacent fins 22
In these offset orientations in transverse direction Y of overflow openings 40.It is opened in the overflow being present in two adjacent fins 21 and 22
Offset D40/2 between mouth 40 accounts for the 50% of the length of interval D 40 herein.
Each overflow openings 40 have herein is equal to 4mm2Area.Aperture opening ratio, the aperture opening ratio include
The gross area for being located at the fin 21 with overflow openings 40 or the overflow openings 40 in equivalent is used for molecule, and
And
The gross area in the face 21.0 of this fin 21 is used for denominator,
It is equal to 20% herein.
The function of distributor 1 is illustrated in greater detail in Fig. 4 and Fig. 5.Liquid refrigerant F1 is shown as shade.Such as Fig. 4
Shown with Fig. 5, liquid refrigerant F1 by each 40 overflow of overflow openings, and fill these fins 21,22,23,24,31,
32,33 and 34 each assignment channel 42.
If Fig. 4 and Fig. 5 are shown, the volume (being shown as shade on Fig. 4 or Fig. 5) of each assignment channel 42 is less than total volume
The 10% of (grid is shown as on Fig. 4), the total volume are delimited by following item:
I) there is the corresponding fin 222 of overflow openings 240,
Ii the plate 11) being fixed on the low portion of this fin 222, and
Iii) positioned at the fin 221 of the fast upstream of fin 222.
Figure 15 shows according to the present invention for distributing liquid refrigerant F1 to the distribution method in heat exchanger 2.
The distribution method particularly the following steps are included:
1001) implement distributor 1,
1002) liquid refrigerant F1 is transmitted in access 20 and 30 and generally on longitudinal direction X,
1003) liquid refrigerant F1 is allowed to pass through the flowing in the aperture of fin 21 and equivalent with opening 40,
1004) each assignment channel 42 is filled, so that liquid refrigerant F1 flows through these overflow openings 40；Step
1004) mode of operation shown in Fig. 4 and Fig. 5 is generated.
When distributor 1 is in operation, each assignment channel 42 is generally horizontal.Each assignment channel 42 and this
The cooperation permission of a little overflow openings 40 distributes liquid refrigerant F1 as homogeneously as possible in transverse direction Y.
If Fig. 3 is shown, heat exchanger 2 includes the heat exchange unit shown partially with the reference number 4 in Fig. 3.In addition, heat is handed over
Parallel operation 2 includes the entrance for heat production fluid F2 and the entrance 8 for liquid refrigerant F1.Entrance 8 is at this by perforation stick 9
Perforation formed.
Heat exchanger 2 further includes the distributor 1 for being configured as liquid refrigerant F1 being supplied to heat exchange unit 4.?
In this case, heat exchanger 2 includes that holding tank 3 stores liquid in the holding tank before flow direction distributor 1
Refrigerant F1.In operation, liquid refrigerant F1 passes through distributor 1.
Second and third embodiments of the invention have shared following characteristics, for given fin 121,122,123,124,
The gross area of all overflow openings 140,240,241 increases from the top to the bottom.This can be by increasing these quantity being open
And/or area is realized.
Fig. 6 and Fig. 7 shows a part of the distributor 101 of second embodiment according to the present invention.In distributor
In the case that 101 are similar to distributor 1, the description above with respect to Fig. 1 to Fig. 5 distributor 1 provided can be arrived by modulation
On distributor 101, other than significant difference explained below.
Have in structure or function with the component of the identical or corresponding distributor 101 of the component of distributor 1 and increases
100 identical numeric reference number.Therefore, we have plate 111,112, fin 121,122,123,124, overflow openings
140 and assignment channel 142.
Distributor 101 and distributor 1 are the difference is that these overflow openings 140 have elliptical shape.However,
Such as in distributor 101, each aperture of each fin 121,122,123,124 forms overflow openings 140.
Overflow openings of these fins 121,123 with identical quantity, but the area of the opening 140 of lower fins 123
Less than the area of the opening 140 of upper fins 123.The opening 140 of fin 121 is less, but they have and lower fins 122
The identical shape of shape.Opening for fin 123 and 124 is also such case.The gross area of these openings is in the exchange
Increase (i.e. downwards) on the direction (descent direction on Fig. 7) for being from upstream to downstream during the operation of device.
Fig. 8 and Fig. 9 shows a part of the distributor 201 of third embodiment according to the present invention.In distributor
In the case that 201 are similar to distributor 101, the description above with respect to Fig. 6 and Fig. 7 distributor 101 provided can be turned
It is transferred on distributor 201, other than significant difference explained below.
Have in structure or function with the component of the identical or corresponding distributor 201 of the component of distributor 101 and increases
100 identical numeric reference number is added.Therefore, we have plate 211,212, fin 221,222,223,224, overflow openings
240 and assignment channel 242.
Distributor 201 is different from distributor 101, because two fins 221 and 222, which have, does not form overflow openings
240 aperture 241.Only fin 223 and 224 has overflow openings 240.In fact, these apertures 241 are in fin 221 and 222
On quantity it is seldom so that these apertures 241 are submerged when distributor 201 is in operation.
These fins 221 and 222 are placed on the upstream of these fins 223 and 224 with overflow openings 240.Aperture
241 are distributed in the transverse direction.The quantity of the overflow openings 240 of each fin 223 or 224 is than each fin 221 or 222
The quantity in aperture 241 is 5 times big.
The quantity in the aperture 241 of each fin 221 or 222 is during the operation of the exchanger in the side for being from upstream to downstream
Increase (i.e. downwards) on (descent direction on Fig. 9).In the wing with aperture 241 for being located at most upstream (at the top of Fig. 9)
Interval Ds 241.1 measuring in the transverse direction of piece 221, between two continuous apertures 241 are equal to 51mm herein.In fact,
Spacing 11-12 between plate 11 and 12 is approximately equal to 51mm.In the cross for the fin 222 with aperture 241 for being located at most downstream
Interval Ds 241.2 measuring on direction, between two continuous apertures 241 are equal to 20mm herein.
Compared with distributor 1, when distributor 201 is in operation, the fin 221 and 222 with aperture 241 can be with
The function of completing the flow velocity for the liquid refrigerant that control enters distributor 201 while high load loss is being generated, and is being had
The fin 223 and 224 of overflow openings 240 completes distribution function while only generating low-load loss on the contrary.
Figure 10 shows a part of the distributor 301 of fourth embodiment according to the present invention.In 301 class of distributor
In the case where being similar to distributor 1, the description above with respect to Fig. 1 to Fig. 5 distributor 1 provided can be filled by modulation to distribution
It sets on 301, other than significant difference explained below.
Have in structure or function with the component of the identical or corresponding distributor 301 of the component of distributor 1 and increases
300 identical numeric reference number.Therefore, we have a plate 311,312, access 320 and fin 321,322,323,
324。
Distributor 301 is different from distributor 1, because of 311 and of these fins 321,322,323,324 and these plates
312 are arranged in the region that wherein access 320 is relatively wide distributor 301, because the region is not used for heat production stream
The conduit of body F2.In fact, each conduit for heat production fluid F2 is blocked by plug 350, and for heat production fluid F2's
The outlet (not shown) of conduit is located on the side of distributor 301.
Therefore, at the level of these fins 321,322,323,324, these accesses 320 can be arranged at distribution dress
It sets in the 301 entire height measured in a direction z, and these accesses 20 and 30 are handed over the corresponding pipe for heat production fluid F2
It replaces.For example, the spacing 311-312 between these plates 311 and 312 is approximately equal to 110mm, and between these plates 11 and 12
Spacing 11-12 is approximately equal to 51mm.
Therefore, the fixed part of each fin 321,322,323,324 is relatively small, and this reduce in the plate and the wing
The stress in fillet weld formed between piece.
In addition, these fins 321,322,323,324 can have as first embodiment (Fig. 1 to 5: overflow by constant number
Stream opening) or such as the aperture of configuration and overflow openings in 3rd embodiment (Fig. 8 and Fig. 9: orifice number progressively increases).
Figure 11 shows a part of the distributor 401 of fifth embodiment according to the present invention.Distributor 401 will
The spacing wherein between plate 411 and 412 be it is big (such as: the fin 421 arranged in region 110mm)
With 422,
With wherein access 420 be shrink (such as: 55mm) (because being deposited for the replacing for conduit of heat production fluid F2
) region in the fin 423,424 that arranges and equivalent combination.
Each conduit for heat production fluid F2 is blocked by plug 450, and the outlet of the conduit for heat production fluid F2
(not shown) is located on the side of distributor 401.
The fin 421,422 being arranged in the wide region of access 420 can have aperture but no overflow openings, and by
The fin 423,424 being arranged in the narrow region of access 420 can have overflow openings.
Figure 11 shows a part of the distributor 501 of sixth embodiment according to the present invention.Distributor 501 with point
It is similar with device 1.Distributor 501 includes plate 511,512 and equivalent, for the entrance 508 of liquid refrigerant, fin 521
And equivalent, and for blocking the plug 550 for being used for the conduit of heat production fluid F2.
Distributor 501 is different from distributor 1, because wherein arranging the region of holding tank 503 than wherein arranging to accommodate
The region of slot 3 is wider, this allows the increase at a distance between these plates 511 and 512 and each aperture forms and is used for liquid
The entrance 508 of refrigerant.Therefore, it has been reduced or avoided as in each of these apertures of the capillarity from soldering
The risk divided or blocked completely.In addition, this wider region allows to limit bigger aperture for the flowing of liquid refrigerant.
Naturally, the present invention is not limited to specific examples that is described herein and showing.Without departing from such as by appended
In the case where the scope of the present invention that claims limit, it is also contemplated that those skilled in the art's other changes in power
Body or embodiment.
Therefore, as the alternative solution of embodiments described above, these fins be can have in addition to flat and inclination
Outer profile.For example, Figure 13 shows a part of distributor 601, wherein these fins are flat and by oblique stripes
It and is horizontal Cross slat composition when the distributor is in operation.Similarly, Figure 13 shows the one of distributor 601
Part, these fins are flat and sinusoidal in the distributor.
Claims (23)
1. a kind of heat exchanger (2), which is configured for for heat being transmitted to from least one heat production fluid (F2)
At least one cryogenic fluid as liquid refrigerant (F1), the heat exchanger (2) include arrangement parallel to each other plate (3,11,
12,13,14) it, is uploaded to limit the longitudinal direction for being configured for generally extending in vertical direction during operation (X)
Each access (20,30) of the First Series access (20,30) of drain cryogen (F1), First Series is limited at continuously
Between two plates (11,12-13,14), and limits and be configured for generally uploading artificial delivery hot fluid in the longitudinal direction (X)
Second series access, each access of second series is limited between continuous two plates, the access quilt of the second series
It is inserted between the two paths of the First Series；At least one is used for the entrance (8 of liquid refrigerant (F1)；508), the entrance
It is configured as that only the liquid refrigerant being poured into the access of the First Series；And in the upper end of the heat exchanger only
Distributor in the access of the First Series, the distributor include generally on transverse direction (Y) in first system
Column one or each access (20,30) in extend fin (21,22,23,24-31,32,33,34), the transverse direction with should
Longitudinal direction (X) it is orthogonal and with these plates (11,12,13,14) in parallel, each accesses (20,30) of the First Series accommodates
The several fins (21-24,31-34) to follow one another on the longitudinal direction (X),
It is characterized in that,
Each fin (21-24,31-34) has the aperture for being configured as allowing the liquid refrigerant (F1) to flow；
At least one fin (21,22,23,24) has upper part (21.1) and low portion (21.2), when the distributor
(1) when the in operation and longitudinal direction extends in vertical direction, the height of the upper part (21.1) is greater than the lower part
The partially height of (21.2),
The low portion (21.2) and the plate (12) being fixed on the low portion (21.2) restriction are configured to use
In at least one assignment channel (42 of the conduction liquid cryogen (F1) in the transverse direction (Y)；142；242),
The aperture of at least one fin (21,22,23,24) is by the overflow openings in the upper part (21.1)
(40；140；240) it is formed, these overflow openings (40) are configured such that when at least one described assignment channel (42) is full of liquid
When cryogen (F1), which flows via these overflow openings (40).
2. heat exchanger as described in claim 1, wherein corresponding assignment channel (42；142；242) volume is less than total volume
15%, which is delimited by following item:
I) there is the fin (22) of overflow openings (40),
Ii the plate (11)) being fixed on the low portion of the fin (22) with overflow openings (40), and
Iii) it is located at the fin (21) of the fast upstream of the fin with overflow openings (40).
3. heat exchanger as claimed in claim 1 or 2, wherein these overflow openings (40) are uniform in the transverse direction (Y)
Ground is distributed on fin (21,22,23,24).
4. heat exchanger as claimed in claim 1 or 2, wherein aperture opening ratio, the aperture opening ratio include
The overflow openings (40 being located in the fin (21,22,23,24) with overflow openings；140；240) gross area conduct
Molecule, and
Fin (21,22,23,24) has overflow openings (40；140；240) gross area in face as denominator,
The aperture opening ratio is between 10% and 50%.
5. heat exchanger as claimed in claim 1 or 2, wherein each overflow openings (40；140；240) have in 1.5mm2 With
10.0mm2 Between area.
6. heat exchanger as described in claim 1, wherein in the transverse direction between continuous two overflow openings (40)
(Y) interval (D40) measured on is between 1mm and 6mm.
7. heat exchanger as claimed in claim 1 or 2, wherein in overflow openings (40) and being fixed to the low portion
(21.2) minimum range (H40) between the plate (12) between 1mm and 4mm, for corresponding fin (21,22,23,
24) the most of or entirety of overflow openings (40), which is identical.
8. heat exchanger as claimed in claim 6, wherein several fins (21,22,23,24) with overflow with opening accordingly
The upper part (21.1) of mouth (40).
9. heat exchanger as claimed in claim 8, wherein these overflow openings (40) being present in fin (21) relative to
It is present in the offset orientation (D40/2) in the transverse direction (Y) of these overflow openings (40) in adjacent fins (22).
10. heat exchanger as claimed in claim 9, wherein in these overflows being present in two adjacent fins (21,22)
The offset (D40/2) between opening (40) accounts between the 40% and 60% of the length of the interval (D40).
11. heat exchanger as claimed in claim 1 or 2, wherein at least one fin (21,22,23,24) has flat pattern
And extend up to continuous two plates (11,12,13,14) and obliquely run out to continuous two plates (11,
Each of 12,13,14), so as in the plane vertical with these plates (11,12,13,14) and the transverse direction (Y)
Closed bevel (A21) is formed in section.
12. heat exchanger as claimed in claim 1 or 2, wherein each fin (21,22,23,24) has in 4mm and 10mm
Between the length (X21) for being parallel to the longitudinal direction (X), and wherein each fin (21,22,23,24) have 4mm with
The width (Y21) for being parallel to the transverse direction (Y) between 10mm, each fin (21,22,23,24) have equal length
(X21) and width (Y21).
13. heat exchanger as described in claim 1, which includes at least one fin (121,122；221,222),
At least one fin has aperture (141；241) and the one or more is placed on overflow openings (140；240)
Fin (123,124；223,224) upstream, these apertures (141；241) it is distributed in the transverse direction (Y), each fin
Overflow openings (140；240) aperture (141 of the quantity than each fin；241) quantity is 3 times big.
14. heat exchanger (2) as described in claim 1, wherein for giving fin, the gross area of these overflow openings passes through
Increase quantity and/or the area of these overflow openings to increase on the longitudinal direction (X).
15. heat exchanger (2) as claimed in claim 13, wherein these overflow for giving fin (121,122,123,124)
The gross area of stream opening (40,140,240) and aperture (241) or these overflow openings (140,240) is by increasing these overflows
The quantity and/or area in opening or aperture increase on the longitudinal direction (X).
16. heat exchanger (2) as described in claim 1, wherein the heat production fluid is nitrogen.
17. heat exchanger (2) as described in claim 1, wherein the liquid refrigerant is oxygen.
18. heat exchanger (2) as claimed in claim 2, wherein corresponding assignment channel (42；142；242) volume is less than total
The 10% of volume.
19. heat exchanger (2) as claimed in claim 4, wherein the aperture opening ratio is between 20% and 40%.
20. heat exchanger as claimed in claim 5, wherein each overflow openings (40；140；240) have in 2.0mm2With
5.0mm2Between area.
21. heat exchanger as claimed in claim 11, wherein the closed bevel (A21) is between 30 ° and 60 °.
22. heat exchanger as claimed in claim 11, wherein the closed bevel (A21) is between 40 ° and 50 °.
23. heat exchanger as claimed in claim 13, wherein the overflow openings (140 of each fin；240) quantity is than each
The aperture (141 of fin；241) quantity is 5 times big.
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| FR1550960 | 2015-02-06 | ||
| FR1550960A FR3032521B1 (en) | 2015-02-06 | 2015-02-06 | HEAT EXCHANGER COMPRISING A REFRIGERANT LIQUID DISPENSING DEVICE |
| PCT/EP2016/052524 WO2016124748A1 (en) | 2015-02-06 | 2016-02-05 | Heat exchanger comprising a liquid-refrigerant distribution device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN107208986A CN107208986A (en) | 2017-09-26 |
| CN107208986B true CN107208986B (en) | 2019-08-06 |
Family
ID=53404659
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201680007397.4A Active CN107208986B (en) | 2015-02-06 | 2016-02-05 | Including liquid-refrigerant distributing device heat exchanger |
Country Status (5)
| Country | Link |
|---|---|
| US (1) | US20180023899A1 (en) |
| EP (1) | EP3254045B1 (en) |
| CN (1) | CN107208986B (en) |
| FR (1) | FR3032521B1 (en) |
| WO (1) | WO2016124748A1 (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108088278B (en) * | 2018-01-26 | 2023-09-19 | 上海交通大学 | Plate-fin heat exchanger fin assembly for improving uneven distribution of liquid and heat exchanger |
| CN113670099A (en) * | 2021-07-02 | 2021-11-19 | 广州华工机动车检测技术有限公司 | Liquid cooling plate structure of power battery |
| CN115324280B (en) * | 2022-08-24 | 2023-12-05 | 中国建筑第五工程局有限公司 | Super-strength uniform partial pressure positioning type steel structure column |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0130122B1 (en) * | 1983-06-24 | 1988-09-14 | L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude | Device for evaporating a liquid by heat exchange with a second fluid and air distillation unit comprising such a device |
| CN101949663A (en) * | 2010-09-13 | 2011-01-19 | 三花丹佛斯（杭州）微通道换热器有限公司 | Refrigerant guide pipe and heat exchanger with same |
| FR2957142A1 (en) * | 2010-03-08 | 2011-09-09 | Air Liquide | HEAT EXCHANGER |
| CN102538560A (en) * | 2010-12-30 | 2012-07-04 | 林德股份公司 | Distribution system and heat exchanger apparatus |
Family Cites Families (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3568462A (en) * | 1967-11-22 | 1971-03-09 | Mc Donnell Douglas Corp | Fractionating device |
| FI93773C (en) * | 1994-03-09 | 1995-05-26 | Shippax Ltd Oy | Heat exchanger element |
| US5438836A (en) * | 1994-08-05 | 1995-08-08 | Praxair Technology, Inc. | Downflow plate and fin heat exchanger for cryogenic rectification |
| US5704417A (en) * | 1996-08-23 | 1998-01-06 | Gas Research Institute | Perforated fin heat and mass transfer device |
| WO2011110782A1 (en) * | 2010-03-08 | 2011-09-15 | L'Air Liquide, Société Anonyme pour l'Etude et l'Exploitation des Procédés Georges Claude | Heat exchanger |
-
2015
- 2015-02-06 FR FR1550960A patent/FR3032521B1/en not_active Expired - Fee Related
-
2016
- 2016-02-05 US US15/547,314 patent/US20180023899A1/en not_active Abandoned
- 2016-02-05 EP EP16703139.2A patent/EP3254045B1/en not_active Not-in-force
- 2016-02-05 CN CN201680007397.4A patent/CN107208986B/en active Active
- 2016-02-05 WO PCT/EP2016/052524 patent/WO2016124748A1/en active Application Filing
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0130122B1 (en) * | 1983-06-24 | 1988-09-14 | L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude | Device for evaporating a liquid by heat exchange with a second fluid and air distillation unit comprising such a device |
| FR2957142A1 (en) * | 2010-03-08 | 2011-09-09 | Air Liquide | HEAT EXCHANGER |
| CN101949663A (en) * | 2010-09-13 | 2011-01-19 | 三花丹佛斯（杭州）微通道换热器有限公司 | Refrigerant guide pipe and heat exchanger with same |
| CN102538560A (en) * | 2010-12-30 | 2012-07-04 | 林德股份公司 | Distribution system and heat exchanger apparatus |
Also Published As
| Publication number | Publication date |
|---|---|
| EP3254045A1 (en) | 2017-12-13 |
| FR3032521A1 (en) | 2016-08-12 |
| FR3032521B1 (en) | 2017-02-17 |
| CN107208986A (en) | 2017-09-26 |
| US20180023899A1 (en) | 2018-01-25 |
| EP3254045B1 (en) | 2019-01-02 |
| WO2016124748A1 (en) | 2016-08-11 |
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