CN104350351A - Heat exchanger - Google Patents
Heat exchanger Download PDFInfo
- Publication number
- CN104350351A CN104350351A CN201380029506.9A CN201380029506A CN104350351A CN 104350351 A CN104350351 A CN 104350351A CN 201380029506 A CN201380029506 A CN 201380029506A CN 104350351 A CN104350351 A CN 104350351A
- Authority
- CN
- China
- Prior art keywords
- heat exchanger
- raceway groove
- medium
- wall
- housing
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
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Classifications
-
- 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
- F28F9/001—Casings in the form of plate-like arrangements; Frames enclosing a heat exchange core
-
- 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
- F28F9/0265—Header boxes; End plates with static flow control means, e.g. with means for uniformly distributing heat exchange media into conduits by using guiding means or impingement means inside the header box
-
- 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
- F28D21/00—Heat-exchange apparatus not covered by any of the groups F28D1/00 - F28D20/00
- F28D21/0017—Flooded core heat exchangers
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- 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
- F28D7/00—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
- F28D7/16—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being arranged in parallel spaced relation
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- 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
- F28D9/0006—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 plate-like or laminated conduits being enclosed within a pressure vessel
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F13/00—Arrangements for modifying heat-transfer, e.g. increasing, decreasing
- F28F13/06—Arrangements for modifying heat-transfer, e.g. increasing, decreasing by affecting the pattern of flow of the heat-exchange media
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)
- Details Of Heat-Exchange And Heat-Transfer (AREA)
Abstract
The invention relates to a heat exchanger (1) for indirect heat transfer between a first medium (F1) and a second medium (F2), comprising: a shell (2) which has a shell space (3) for receiving the first medium (F1), a heat transfer block (4) which is disposed in the shell space (3) and which during correct operation is surrounded by the first medium (F1), wherein the heat transfer block (4) is designed to cool the second medium (F2) against the first medium (F1), such that a gaseous phase of the first medium (G1) forms in the shell space (3). According to the invention a collecting channel (5) located in the shell space (3) is provided for drawing off the gaseous phase of the first medium (G1) from the shell space (3).
Description
Technical field
The present invention relates to heat exchanger as described in the preamble according to claim 1.
Background technology
The feature of this heat exchanger is described in 67 pages of Fig. 9-1 in 2010 " The Standards of The Brazed Aluminium Plate-Fin Heat Exchanger Manufacturer ' s Association (ALPEMA) " of the 3rd edition.It has the housing enclosing shell space, also has at least one heat transfer block (" core body "), and it to be configured in described shell space and to be designed to the heat exchanger of tabular.This design of heat exchanger is also referred to as " core body is in housing " or " block is in housing " heat exchanger.
Adopt this heat exchanger, first medium especially can with second medium (such as, the gas phase be liquefied or cooled liquid phase) directly conduct heat, wherein, first medium defines the outdoor bathing place of coated heat transfer block during heat exchanger operation, and (vertically) is from bottom to rising (thermosyphon action) in heat transfer block, wherein, second medium preferably with first medium with adverse current or the mode of crossing current conduct heat directed in block.Occur in the first medium of gas phase this collection process above heat transfer block in shell space, and be drawn out of by least one Outlet connector be arranged on housing, and another procedure of processing can be supplied to by (outside) collection raceway groove being arranged on the outside of housing.
Due to the extraction of such gas phase, in shell space, develop the velocity field of the isomery of the gas phase of advancing towards Outlet connector, this weakens the quality of the gas-liquid separation in shell space.This effect can be offset by the change of the quantity of Outlet connector or size, but is only cancelled limited scope, particularly because the flow behavior in collected outside raceway groove also works to the velocity field of the gas phase in shell space.In addition, Outlet connector is the piezoresistive components part of (" core body is in the housing ") heat exchanger of the type mentioned in introductory section, thus involves great expense, must increase production cost when multiple Outlet connector.In addition, by the upside making Outlet connector position be fixed on housing, in structure peripheral parts (such as, cold box, field pipe) period, the free degree is decreased.
Summary of the invention
From here on, therefore the present invention provides the heat exchanger improved for the problems referred to above based on this object.
This problem is solved by the heat exchanger of the feature with claim 1.
Therefore, provide collection channel be arranged in shell space and be designed to extract gas phase out from shell space.
According to one embodiment of present invention, also provide multiple heat transfer block or plate heat exchanger in shell space, it such as can be in parallel or in series operated.
Usually, the heat exchanger of this tabular has multiple plates of configuration parallel to each other, and defines a large amount of heat exchanger channels of the medium for participating in heat exchange.A preferred embodiment of the heat exchanger of tabular has multiple corrugated plating (so-called fin), it is all configured between the plate of the parallel separation of two of plate heat exchanger in each case, wherein, two outermost layers of this plate heat exchanger are formed by cover plate.Like this, medium is formed between every two plates be separated or between the plate be separated and cover plate, because configure fin between which in each case by its a large amount of parallel channel flowed or heat exchanger channels.The medium flowed in adjacent heat exchanger channels thus can exchanged heat indirectly.Towards sidepiece, between the plate of every two adjacent separation, or between cover plate and the plate of adjacent separation, be preferably provided with band (hurdle, so-called side), for closing corresponding heat exchanger channels.Cover plate, separating plate, fin and hurdle, side are preferably produced by aluminium, and are such as welded together in stove.By having the collector of the correspondence of connector, medium can be introduced in heat exchanger channels or from these passages and be drawn out of.
The housing of heat exchanger especially can have encirclement (circle) cylindrical wall, and it is preferably oriented to the longitudinal axis (axle of cylindricality) making wall or housing and extends along horizontal direction under the configuration status of the particular design of heat exchanger.Housing preferably has wall relative to each other, and it is on end face, is connected on this wall, and extends transverse to level or the longitudinal axis.
Described collection raceway groove for extracting the gas phase of first medium out is preferably connected (such as by pipe) to Outlet connector in the mode of guide of flow, this Outlet connector is especially configured in the upside of described housing, and the gas phase of first medium can be drawn out of by those Outlet connector from shell space.
In one embodiment of the invention, collect raceway groove to extend along bearing of trend, this bearing of trend be oriented to be parallel with housing the longitudinal axis (axle of cylindricality) or along horizontal direction, and the tubulose (circle) in this case, preferably had transverse to described bearing of trend (longitudinal axis) or box-like (rectangle) cross section.
Collect raceway groove (configuration status about the particular design of heat exchanger) to be preferably vertically configured in shell space at the ullage of first medium or above heat transfer block, the gas phase making (from the heat transfer block) of first medium to increase contacts with collection raceway groove.
Collect raceway groove and preferably have the wall enclosing the inner space of collecting raceway groove, gas phase can flow towards described Outlet connector in this inner space.In this case, the upside of collecting the sensing heat exchanger of each wall of raceway groove or the part be vertically directed upwards towards are called as the upside of collecting raceway groove, and therefore the part be oppositely arranged of collecting the downside of the sensing heat exchanger of the wall of raceway groove constitutes the downside of collecting raceway groove.The upper side and lower side of collecting raceway groove is connected to each other preferably by the sidewall collecting raceway groove, and this sidewall extends along the longitudinal axis of housing.In end, collect raceway groove and preferably limited by end face relative to each other, this end face relative to each other all makes upside, downside and sidewall be connected to each other in each case.
Modification of the present invention provides in addition, and one or more in the above-mentioned part of the wall of described collection raceway groove can be formed by the housing of heat exchanger.The upside of collecting the upside of raceway groove or the wall of collection raceway groove is preferably formed by housing.Thus this sidewall and end face are correspondingly attached on housing away from shell space.
In order to extract gas phase out, described collection raceway groove preferably has multiple ingate, and it is especially formed on the downside (bottom) of collection raceway groove, and, be also formed in if suitable on the sidewall relative to each other of collection raceway groove.In this case, the ingate be formed on the bottom of collecting raceway groove is preferably slit-like design, and the ingate be arranged on sidewall preferably has circular contour (such as, hole).
Preferably, the interval in adjacent entries hole and the interval that is especially arranged on the ingate on downside are reduced towards the respective end face collecting raceway groove.That is, compared with two that more configure towards the middle part of collecting raceway groove with (about bearing of trend) adjacent ingates, closer to two of an end face location of collecting raceway groove adjacent ingate raceway grooves preferably along collecting the bearing of trend of raceway groove about having less interval each other.
The quantity of ingate, distribution, size and/or shape are preferably chosen as that to make to be configured to numerical value in the velocity field of the gas phase of collecting the first medium in raceway groove consistent as much as possible.In addition, according to an aspect of the present invention, the cross-sectional area (and profile, if properly) collecting raceway groove (perpendicular to collecting in the plane of bearing of trend of raceway groove) is selected by this way: the flow field of the gas phase of uniform as far as possible first medium is based upon collects in raceway groove and in shell space.Preferably, collect cross section the widening/strengthening towards Outlet connector of raceway groove, and/or the restriction configuration structure of the ingate in collection raceway groove, shape and size contribute to this.
In addition, housing can also have multiple Outlet connector originally, and it can be connected to collects on raceway groove, as described above, or on multiple collection raceway grooves of the type illustrated before can being connected to.
These position, sizes and being oriented in of collecting raceway grooves are preferably selected in this case like this, make to be established as with the velocity field of the gas phase of the first medium in respective collection raceway groove in shell space numerically consistent as far as possible.
In addition, at least one Outlet connector described (or, even multiple Outlet connector) can be configured in the upper and lower of the encirclement wall of housing and side part according to the present invention, or be configured in an end-face wall of housing.
Further details of the present invention and advantage should be illustrate in greater detail by the accompanying drawing explanation below exemplary embodiments with reference to accompanying drawing.Be disclosed in these external claims of enclosing of favourable embodiment of the present invention.
Accompanying drawing explanation
In the drawings:
Fig. 1 shows the sectional view according to heat exchanger of the present invention;
Fig. 2 shows another sectional view of the heat exchanger according to Fig. 1; With
Fig. 3 shows the sectional view of the collection raceway groove of the heat exchanger according to Fig. 1 and 2.
Detailed description of the invention
Composition graphs 2 and 3, Fig. 1 show heat exchanger 1, and it has (circle) cylindrical shell 2 of horizontal lying, and this housing 2 defines the shell space 3 of this heat exchanger 1.In this case, housing 2 has the cylindrical wall 14 of encirclement, and it is limited by two walls 15 relative to each other at end face.
Heat transfer block 4 is configured in the shell space 3 surrounded by housing 2.In this case, it can be the plate heat exchanger with multiple parallel heat exchanger channels.
The heat exchanger 4 of this tabular has multiple corrugated plating (so-called fin) in this case, and it is all configured between the flat plate separated of two of plate heat exchanger 4 in each case.Like this, passage parallel in a large number or heat exchanger channels are formed between every two separate plates (or a separate plates and a cover plate, see below), and corresponding medium can flow through described passage.Two outermost layers are formed by the cover plate of plate heat exchanger, and sealed strip (so-called " hurdle, side ") is arranged between every two adjacent plates separated or between the plate separated and cover plate towards sidepiece.
Shell space 3 is filled with first medium F1 during heat exchanger 1 operates, the liquid phase L1 of first medium F1 is made to form the outdoor bathing place surrounding heat transfer block or plate heat exchanger 4, wherein, the gas phase G1 of the first medium F1 developed during operation can be gathered in shell space 3 above liquid phase L1.
First medium (liquid phase L1) F1 (in the heat exchanger channels of association) can rise in heat transfer block 4, and in this process because the indirect heat transfer by second medium F2 is partly evaporated, this second medium F2 will be cooled and such as flow over directed with first medium F1 in the heat exchanger channels of the association of heat transfer block 4.Can discharge in the upper end of block 4 at the gas phase G1 of the first medium F1 produced during this period, and rise with the speed v determined in the shell space 3 of heat exchanger 1.
Second medium F2 is directed into by suitable entrance O (such as by the connector on top cover) and conducts heat in block or plate heat exchanger 4, and is drawn out of from block 4 by outlet O ' (such as by corresponding top cover and the connector be connected on it) after the heat exchanger channels by association.
On the upside 8 of heat exchanger 1, housing 2 in the face of shell space 3 inner side 2a on, configuration be box-packed collection raceway groove 5, it extends along bearing of trend 7.This collection raceway groove 5 is especially elongated design in this case, and thus along bearing of trend 7 than with the direction of bearing of trend 7 transverse direction, there is larger expansion.
Collect raceway groove 5 and also there is wall W, which defines the inner space I collecting raceway groove 5 out, and the gas phase G1 of first medium F1 is extracted from shell space 3 by this inner space.Wall W has upside 9 especially, when this is current, upside 9 is formed by housing 2, and also has two sidewalls 11 extended from it, and this sidewall 11 is extended along bearing of trend 7 and is connected to each other by the bottom (downside) 10 relative with upside 9 of collecting raceway groove 5.In addition, collect raceway groove 5 or its wall W and there are two end face 11a, 11b, its along bearing of trend 7 relative to each other arrange.
In order to extract the gas phase G1 of first medium F1 out from shell space 3, now collect raceway groove 5 sidewall 11 and/or on the downside of it on 10, provide slit-like ingate 12 (being the slit-like ingate on downside 10 in current situations), gas phase G1 enters into by this ingate and collects raceway groove 5.In this case, ingate 12 is along bearing of trend 7 configuration adjacent each other, wherein, along bearing of trend 7 adjacent ingate 13 between distance preferably in each case from Outlet connector 6 towards collecting two end face 11a of raceway groove 5,11b reduces.In this case, the longitudinal axis of these ingates 12 all extends transverse to the bearing of trend 7 collecting raceway groove 5 in each case.
In addition, in each case, on the sidewall 11 collecting raceway groove 5 and/or on downside 10, provide circular entry 13 (being the circular entry 13 on sidewall 11 in the current situation), it is also along bearing of trend 7 configuration adjacent each other.In addition, preferably all reduce from Outlet connector 6 towards two the end face 11a collecting raceway groove 5,11b in each case along the distance of bearing of trend 7 between adjacent ingate 12.
Collect the Outlet connector 6 that raceway groove 5 is also connected to housing 2 open in the upside 9 of collecting raceway groove 5, make by ingate 12,13 enter into collect raceway groove 5 inner space I first medium F1 gas phase G1 by Outlet connector 6 from collection raceway groove 5 be drawn out of.
Outlet connector 6 is preferably configured in the middle part of collecting raceway groove 5 along bearing of trend 7, wherein, the downside 10 of described collection raceway groove 5 preferably has two part 10a, 10b, they are downward-sloping towards Outlet connector 6, and preferably connect in the below of described Outlet connector 6.
Collect the cross section of raceway groove 5 in each case along the direction of Outlet connector 6 from collecting the end face 11a of raceway groove 5,11b increases (widening), with the velocity field v of the gas phase G1 of the uniform as far as possible first medium F1 of (and in shell space 3) acquisition in collection raceway groove 5.
Reference numerals list
| 1 | Heat exchanger |
| 2 | Housing |
| 2a | Inner side |
| 3 | Shell space |
| 4 | Heat transfer block |
| 5 | Collect raceway groove |
| 6 | Outlet connector |
| 7 | Bearing of trend |
| 8 | The upside of housing |
| 9 | Collect the upside of raceway groove |
| 10 | Collect the downside of raceway groove |
| 10a，10b | The part of bottom |
| 11 | Collect the sidewall of raceway groove |
| 11a，11b | End face |
| 12 | Slit-like ingate |
| 13 | Circular entry |
| 14 | The encirclement wall of housing |
| 15 | The end-face wall of housing |
| 16 | The downside of housing |
| F1 | First medium |
| G1 | The gas phase of first medium |
| L1 | The liquid phase of first medium |
| F2 | Second medium |
| I | Inner space |
| O | For the entrance of second medium |
| O′ | For the outlet of second medium |
| V | The velocity field of gas phase G1 |
Claims (17)
1. one kind for the heat exchanger (1) of the indirect heat transfer between first medium (F1) and second medium (F2), has:
-housing (2), it has the shell space (3) for receiving described first medium (F1),
-at least one heat transfer block (4), it is configured in described shell space (3), and surrounded by described first medium (F1) during specified design operation, wherein, described heat transfer block (4) is designed under the effect of described first medium (F1), make described second medium (F2) cool and/or liquefy at least in part, the gas phase (G1) of described first medium is formed in described shell space (3) thus, wherein, at least one heat transfer block (4) described is plate heat exchanger
It is characterized in that
Arrange the collection raceway groove (5) being used for the described gas phase (G1) of extracting described first medium from described shell space (3) out, it is positioned at described shell space (3).
2. heat exchanger according to claim 1, it is characterized in that, described heat transfer block (4) is designed so that described first medium (F1) can rise during described heat exchanger (1) operation in described heat transfer block (4), wherein, described heat transfer block (4) is especially designed in described heat transfer block (4) to guide described second medium (F2) with the mode of described first medium (F1) adverse current or crossing current.
3. the heat exchanger according to claims 1 or 2, is characterized in that, multiple heat transfer blocks (4) of plate heat exchanger form are configured in described shell space.
4. according to the heat exchanger one of aforementioned claim Suo Shu, it is characterized in that, described collection raceway groove (5) is connected at least one Outlet connector (6) of being arranged on described housing (2), and the described gas phase (G1) of described first medium is drawn out of from described shell space (3) through described collection raceway groove (5) by described at least one Outlet connector (6).
5. heat exchanger according to claim 4, it is characterized in that, described collection raceway groove (5) has wall (W), which defines the inner space (I) of described collection raceway groove (5), the described gas phase (G1) of described first medium can towards described Outlet connector (6) flowing in described inner space (I), and the bearing of trend (7) of level that described wall (W) stretches along the upside (8) along described housing (2) extends.
6. heat exchanger according to claim 5, is characterized in that, it is especially the cross section of box-like or tubulose transverse to described bearing of trend (7) that described collection raceway groove (5) has.
7. according to the heat exchanger one of claim 5 and 6 Suo Shu, it is characterized in that, the downside (10) that the described wall (W) of described collection raceway groove (5) has upside (9) and is oppositely arranged, wherein, described upside (9) and described downside (10) are connected to each other by the sidewall (11) relative to each other of the described wall (W) of described collection raceway groove (5).
8. heat exchanger according to claim 7, it is characterized in that, a part of the described wall (W) of described collection raceway groove (5), the upside (9) of especially described wall (W), is formed by described housing (2).
9. the heat exchanger according to claim 7 or 8, it is characterized in that, it is especially the ingate (12) of slit-like that the described downside (10) of described collection raceway groove (5) and/or described sidewall (11) have multiple, and the described gas phase (G1) of described first medium flows in described collection raceway groove (5) by described ingate.
10. the heat exchanger according to claim 4 and 9, it is characterized in that, described collection raceway groove (5) has two end face (11a, 11b), its along described bearing of trend (7) relative to each other arrange, wherein, the described interval of adjacent ingate (12) is reduced towards described respective end face (11a, 11b).
11. according to the heat exchanger one of claim 7 to 10 Suo Shu, it is characterized in that, it is especially circular ingate (13) that the described downside (10) of described collection raceway groove (5) and/or described sidewall (11) have multiple, and the described gas phase (G1) of described first medium flows in described collection raceway groove (5) by described ingate.
12. according to the heat exchanger described in claim 4 to 6, it is characterized in that, the described cross section of described collection raceway groove (5) increases towards described Outlet connector (6), makes the velocity field (v) of the described gas phase (G1) of the described first medium in described collection raceway groove (5) keep numerical value substantially constant.
13., according to the heat exchanger one of aforementioned claim Suo Shu, is characterized in that, described heat exchanger (1) has the additional Outlet connector (6) be connected to each other by described collection raceway groove (5).
14. according to the heat exchanger one of aforementioned claim Suo Shu, it is characterized in that, described heat exchanger (1) has a large amount of collection raceway grooves (5), and it is all connected at least one Outlet connector (6) in each case.
15. according to the heat exchanger one of aforementioned claim Suo Shu, it is characterized in that, the cylindricality that described housing (2) has transverse to described bearing of trend (7) surrounds wall (14), and it makes described two end-face wall (15) of described housing (2) be connected to each other.
16. heat exchangers according to claim 4 and 15, it is characterized in that, described at least one Outlet connector (6) is configured on the described encirclement wall (W) of described housing (2), especially (8 are configured in the upper part of the described wall (14) of described housing (2), side part or lower part, 16), or described at least one Outlet connector (6) is configured in the described end-face wall (15) of described housing (2).
17. heat exchangers according to claim 9 or 11, it is characterized in that, the described quantity of the described ingate (12,13) on described collection raceway groove (5), distribution, size and/or shape are selected like this: make the described velocity field (v) of the described gas phase (G1) of described first medium in described collection raceway groove (5) and especially also in described shell space (3) numerical value set up basically identically.
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE102012011328A DE102012011328A1 (en) | 2012-06-06 | 2012-06-06 | Heat exchanger |
| DE102012011328.5 | 2012-06-06 | ||
| PCT/EP2013/001670 WO2013182314A1 (en) | 2012-06-06 | 2013-06-06 | Heat exchanger |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN104350351A true CN104350351A (en) | 2015-02-11 |
| CN104350351B CN104350351B (en) | 2017-08-15 |
Family
ID=46758579
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201380029506.9A Expired - Fee Related CN104350351B (en) | 2012-06-06 | 2013-06-06 | Heat exchanger |
Country Status (10)
| Country | Link |
|---|---|
| US (1) | US20150153115A1 (en) |
| EP (1) | EP2859295B1 (en) |
| JP (1) | JP6116681B2 (en) |
| KR (1) | KR20150030229A (en) |
| CN (1) | CN104350351B (en) |
| AU (1) | AU2013270937B2 (en) |
| DE (1) | DE102012011328A1 (en) |
| ES (1) | ES2598837T3 (en) |
| MX (1) | MX344387B (en) |
| WO (1) | WO2013182314A1 (en) |
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| US10378837B2 (en) * | 2014-05-01 | 2019-08-13 | Conocophillips Company | Liquid drains in core-in-shell heat exchanger |
| JP2016014495A (en) * | 2014-07-01 | 2016-01-28 | ダイキン工業株式会社 | Falling film evaporator |
| FR3038037B1 (en) | 2015-06-29 | 2018-04-20 | Trane International Inc. | SUCTION DUCT AND DUAL SUCTION DUCT FOR AN IMMERSION EVAPORATOR |
| WO2016102047A1 (en) * | 2014-12-23 | 2016-06-30 | Linde Aktiengesellschaft | Heat exchanger, in particular block-in-shell heat exchanger comprising a separating unit for separating a gaseous phase from a liquid phase and for distributing the liquid phase |
| WO2016102045A1 (en) * | 2014-12-23 | 2016-06-30 | Linde Aktiengesellschaft | Core-in-shell heat exchanger comprising a conducting device for better distribution of the medium in the separation chamber |
| CN105509370B (en) * | 2016-01-14 | 2017-11-03 | 北京瑞宝利热能科技有限公司 | A kind of Combined aluminum alloy heat exchanger and its system |
| CN108662812B (en) | 2017-03-31 | 2022-02-18 | 开利公司 | Flow balancer and evaporator having the same |
| EP3629688A1 (en) * | 2018-09-27 | 2020-04-01 | Siemens Aktiengesellschaft | Power converter with a separate interior |
| US20220316646A1 (en) | 2019-11-15 | 2022-10-06 | Linde Gmbh | Transition component having insulation |
| US20230392837A1 (en) * | 2022-06-03 | 2023-12-07 | Trane International Inc. | Evaporator charge management and method for controlling the same |
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| US20050039486A1 (en) * | 2002-01-17 | 2005-02-24 | York Refrigeration Aps | Submerged evaporator with integrated heat exchanger |
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2012
- 2012-06-06 DE DE102012011328A patent/DE102012011328A1/en not_active Withdrawn
-
2013
- 2013-06-06 US US14/406,417 patent/US20150153115A1/en not_active Abandoned
- 2013-06-06 JP JP2015515424A patent/JP6116681B2/en active Active
- 2013-06-06 WO PCT/EP2013/001670 patent/WO2013182314A1/en active Application Filing
- 2013-06-06 KR KR20157000268A patent/KR20150030229A/en not_active Application Discontinuation
- 2013-06-06 EP EP13730801.1A patent/EP2859295B1/en not_active Not-in-force
- 2013-06-06 MX MX2014014454A patent/MX344387B/en active IP Right Grant
- 2013-06-06 AU AU2013270937A patent/AU2013270937B2/en not_active Ceased
- 2013-06-06 CN CN201380029506.9A patent/CN104350351B/en not_active Expired - Fee Related
- 2013-06-06 ES ES13730801.1T patent/ES2598837T3/en active Active
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Also Published As
| Publication number | Publication date |
|---|---|
| EP2859295B1 (en) | 2016-08-03 |
| AU2013270937A1 (en) | 2014-12-04 |
| KR20150030229A (en) | 2015-03-19 |
| ES2598837T3 (en) | 2017-01-30 |
| JP2015518953A (en) | 2015-07-06 |
| AU2013270937B2 (en) | 2017-07-27 |
| MX344387B (en) | 2016-12-14 |
| DE102012011328A1 (en) | 2013-12-12 |
| CN104350351B (en) | 2017-08-15 |
| MX2014014454A (en) | 2015-02-12 |
| EP2859295A1 (en) | 2015-04-15 |
| WO2013182314A1 (en) | 2013-12-12 |
| US20150153115A1 (en) | 2015-06-04 |
| JP6116681B2 (en) | 2017-04-19 |
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