EP3438596B1 - Improved fluid distributor - Google Patents
Improved fluid distributor Download PDFInfo
- Publication number
- EP3438596B1 EP3438596B1 EP17184287.5A EP17184287A EP3438596B1 EP 3438596 B1 EP3438596 B1 EP 3438596B1 EP 17184287 A EP17184287 A EP 17184287A EP 3438596 B1 EP3438596 B1 EP 3438596B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- fluid
- distributor assembly
- openings
- fluid distributor
- inlet
- 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.)
- Active
Links
- 239000012530 fluid Substances 0.000 title claims description 118
- 238000003475 lamination Methods 0.000 claims description 43
- 239000003507 refrigerant Substances 0.000 claims description 21
- 230000008878 coupling Effects 0.000 claims description 11
- 238000010168 coupling process Methods 0.000 claims description 11
- 238000005859 coupling reaction Methods 0.000 claims description 11
- 238000004891 communication Methods 0.000 claims description 5
- 238000009826 distribution Methods 0.000 claims description 5
- 230000002093 peripheral effect Effects 0.000 claims description 4
- 125000006850 spacer group Chemical group 0.000 description 6
- 238000000034 method Methods 0.000 description 3
- 230000003750 conditioning effect Effects 0.000 description 2
- 230000002787 reinforcement Effects 0.000 description 2
- 238000009827 uniform distribution Methods 0.000 description 2
- 241000217377 Amblema plicata Species 0.000 description 1
- 238000013019 agitation Methods 0.000 description 1
- 230000003042 antagnostic effect Effects 0.000 description 1
- 230000004888 barrier function Effects 0.000 description 1
- 230000005465 channeling Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 238000003754 machining Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000001681 protective effect Effects 0.000 description 1
- 238000011144 upstream manufacturing Methods 0.000 description 1
Images
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
- F28F9/02—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
-
- 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
- F25B39/028—Evaporators having distributing means
-
- 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
- F25B2500/00—Problems to be solved
- F25B2500/18—Optimization, e.g. high integration of refrigeration components
Definitions
- the present invention relates to the field of aeraulic systems, in particular of conditioning systems.
- the present invention more specifically, relates to a fluid distributor assembly suitable for use in a heat exchanger, in particular an evaporator.
- Heat exchangers used in conditioning systems are devices that, in the most general terms, comprise a casing - or mantle - inside which is housed a tube bundle. Within the tube bundle, a service fluid flows to exchange heat with a process fluid at a different temperature.
- the service fluid is typically an evaporating refrigerant fluid that circulates inside the tube bundle and cools the process fluid.
- the latter passes externally to the tube bundle housed within the mantle, passing through the heat exchanger.
- a supply pipe feeds the heat exchanger with refrigerant fluid, engaging it at a head unit - or manifold - thereof.
- the exchanger is generally equipped with a dedicated distributor device.
- JPH1089885 discloses a tank for a heat exchanger wherein an inlet section is equipped with a junction element provided with sacrificial corrosion members.
- the known distributor devices typically provide a plurality of fed conduits each engaging a respective tubular element of the tube bundle. Solutions of this type however have the drawback of being constructively complex due to expensive and sophisticate mechanical machining of the fed conduits connecting structure in order to maintain desired outlet conditions while conveying the fluid in each tube of the bundle.
- the technical problem placed and solved by the present invention is then to provide a fluid distributor assembly, in particular a refrigerant fluid, within the tube bundle of a heat exchanger that allows to overcome the above-illustrated drawbacks with reference to the prior art.
- the fluid distributor assembly according to present invention is structurally simple and economical to be realized, due to the presence of a lamination unit housed in a seat of the head unit in such a way that, a mixing chamber of refrigerant fluid that feeds the latter is defined.
- the fluid distributor assembly comprises direction means provided with an impact surface and configured so as to direct the fluid outflowing from said lamination unit along a substantially orthogonal direction with respect to a fluid inlet direction into apertures of the tube plate engaging the tube bundle of the exchanger.
- This solution overcome the need to provide complex, tricky and high-costly working process of single-engagements conduits intended to engage a respective tubular element of the tube bundle to feed each tube individually. Furthermore, the presence of said direction means allows to create fluid agitation conditions in the mixing chamber prior to its entry into the tube bundle. Particularly, said orthogonal flow to the fluid inlet direction into the tube plate is generated so as to sequentially lick the tube plate apertures and to allow each tube to suck the required amount of refrigerant, according to a kind of dynamical "self-regulation".
- FIG 1 an exploded view of a preferred embodiment of a fluid distributor assembly 1, in particular a refrigerant fluid, according to the present invention is illustrated by way of example and not for limitative purposes.
- the distributor assembly 1 of the present invention is intended for a preferred use in heat exchangers, preferably evaporators, such as direct evaporators.
- the distributor assembly 1 is shown in association with a tube plate 100, the latter being an element to which the distributor assembly 1 is intended to be coupled.
- the tube plate 100 is a plate with a circular geometry, exemplifying the tubular plates used in the considered technical field.
- the tube plate 100 shown is not limitative for the purposes of the present invention.
- the distributor assembly 1 comprises a head unit 10 - or manifold - configured to receive the refrigerant fluid inletting the heat exchanger and is intended to be coupled to the tube plate 100 at a coupling surface - denoted with reference A - thereof.
- the head unit 10 therefore comprises at least one inlet 11 port, in fluid communication with the inlet refrigerant fluid flow, which allows the latter to enter said head unit 10.
- the head unit 10 is thus a hollow element, that is an element in which is defined a transit region 12 through which the inlet fluid flow passes towards the tube plate 100.
- the inlet 11 in the head unit 10 are intended to be two, however, in other embodiments, said inlet can be different in numbers, for example one or four, depending on the operating modes of the exchanger in which the distributor assembly according to the present invention will be mounted.
- the coupling surface A - also with reference to the shown examples - is a peripheral region of the head unit 10 and of the respective tube plate 100, shaped so as to flange the above-mentioned two elements together.
- this peripheral region defines a circular crown, however, different coupling geometries are possible.
- the tube plate 100 of a heat exchanger comprises a zone having a plurality of apertures - or housings 101 - configured to put in fluid communication said head inlet 11 and tubes of the exchanger.
- each aperture of said plurality is suitable for coupling with respective tubular elements (not shown in the figures) within which, in use, the refrigerant fluid flows.
- the plurality of housings 101 - which in the examples are a plurality of through holes 101a of the plate 100 - are configured to allow the refrigerant fluid inletting the head unit 10 passing towards tubular elements which typically engage with their terminal end the plate 100 at said housings, and which form the tube bundle housed within the exchanger's casing.
- housings 101 are obtained only on a portion of the plate 100, particularly on the portion corresponding to one of the two inlet 11 of the head unit 10.
- the distributor assembly 1 can be coupled with a tube plate 100 having a housings distribution different from that one illustrated.
- the head unit 10 is further provided with a seat 13 adapted to receive a lamination unit 20, in particular of a plate-shaped geometry, which lamination unit 20 is positioned in said seat 13 so as to divide the transit region 12 of the head unit 10 in a first collecting chamber 14 and in an outlet region 15 of the refrigerant fluid.
- the plate-shaped lamination unit 20 comprises an inlet surface 21, an outlet surface 22 and one or more openings 23 to allow the fluid entering the head unit 10 to pass there through.
- the first collecting chamber 14 is comprised between the inlet 11 adapted to receive the fluid entering the head unit 10 and said inlet surface 21.
- the outlet surface 22 of the plate-shaped lamination unit 20 faces toward said outlet region 15 of the refrigerant fluid.
- Said one or more openings 23 are appropriately sized to obtain a pressure drop across the lamination unit 20.
- the overall configuration of the distributor assembly 1 being such that, in condition of said head unit 10 coupled to the tube plate 100, a second mixing chamber 30 is defined at said outlet region 15 among said coupling surface A, said lamination unit 20 and the tube plate 100, so that the fluid, in use, sequentially crosses the first collecting chamber 14, the one or more openings 23 in the lamination unit 20 and subsequently the second mixing chamber 30.
- the fluid is so administered into tubes connected to the tube plate 100.
- the first collecting chamber 14 and the second mixing chamber 30 are preferably consecutive with each other and said outlet region 15 is adjacent to said outlet surface 22.
- first collecting chamber 14 and the second mixing chamber 30 are preferably arranged in sequence with respect to a fluid flow direction ⁇ as defined by the head inlet 11.
- the lamination unit 20 thus allows expansion of the refrigerant fluid in the second mixing chamber 30 with respect to the condition in which the fluid is in the first collecting chamber 14.
- the refrigerant fluid flow F entering the inlet 11 of the head unit 10 reaches the lamination unit 20 and crosses said one or more openings 23 of the latter being subjected to a pressure drop causing it to expand into the second mixing chamber 30 and to generate a turbulent flow regime.
- mixing chamber 30 permits to improve the refrigerant fluid flow F' conditions before its inlet into the exchanger tube bundle, namely achieving a uniform mixing of the latter entering the through holes 101a of the tube plate 100.
- the lamination unit 20 is locked to the seat 13 of the head unit 10 onto shoulders 13a thereof. It is preferably fixed to the latter in a removable manner, by means of fastening means known to the skilled person in the field.
- a spacer is configured to allow the fastening of the lamination unit 20 to the seat 13, wherein said spacer comprises a first and a second portion.
- the first portion is internally hollow and configured to engage a through hole 101a of the tube plate 100 and the second portion remains outside of the tube plate in such a way as to maintain the lamination unit in abutment onto said shoulders 13a of the head unit 10, spaced from the tube plate 100.
- More than one spacer can be provided, the number of which is function of the operative condition of the distributor.
- said spacers are provided in a homogeneous chessboard-like distribution.
- the lamination unit 20 is however secured in such a way as to make the collecting chamber 14 hermetic, to avoid possible undesired fluid leaks towards the second mixing chamber 30.
- the lamination unit 20 can also be made in a single piece with the head unit 10 at said seat 13.
- the plate-shaped lamination unit 20 - or at least its outlet surface 22 - lies on a plane substantially parallel to the coupling surface A with the tube plate 100.
- the fluid F' outflows from the lamination unit 20 at equidistant points from the through holes 101a of said tube plate 100, further favoring a uniform mixing of the fluid F' entering the latter.
- said one or more openings of the lamination unit 20, are denoted by reference 23.
- said openings 23 comprise a plurality of circular geometric through holes, and are apt to put in fluid communication the first collecting chamber 14 with the second mixing chamber 30.
- At least one of said one or more openings 23 comprise an elongated shape, for examples like a single slot, or through holes of other geometric shapes than the circular shape.
- Said one or more openings may have, for example, a passageway configured so as to impart a substantially orthogonal direction to the fluid F' outflowing from the outlet surface 22 with respect to the direction of the fluid F inletting the lamination unit 20.
- the amount and geometry of said one or more openings is a function of the operating conditions of the exchanger and of the desired fluid F pressure drop across the lamination unit 20.
- Said one or more openings 23 are preferably distributed along a peripheral edge of the plate-shaped lamination unit 20, preferably in such a way as to do not directly face one or more of the through holes 101a of the tube plate 100, as provided by the embodiment of figures 7 and 8 .
- said one or more openings 23 are arranged laterally with respect to an input fluid flow F having a direction ⁇ as imparted by said head inlet 11.
- the fluid distributor assembly 1 further comprises direction means provided with an impact surface 241, 26 configured so as to direct the fluid outflowing from said outlet surface 22 along a substantially orthogonal direction with respect to a fluid inlet direction ⁇ into said apertures 101.
- Said direction means allow to generate an orthogonal flow F' with respect to the fluid inlet direction ⁇ into the tube plate 100 so as to sequentially lick said apertures 101.
- Each tube of the tube bundle of the exchanger is therefore able to suck the required amount of refrigerant, according to a kind of dynamical "self-regulation".
- said orthogonal flow F' with respect to said direction ⁇ is achieved by providing an antagonistic element positioned downstream the expansion of the flow outflowing the outlet surface 22.
- the apertures 101 of the tube plate 100 are arranged laterally with respect to a positioning of each of said one or more openings 23 of the lamination unit 20.
- said direction means comprises an impact surface 26 of the tube plate 100 facing toward said second mixing chamber 30.
- each of said apertures 101 and each of said one or more openings 23 is such that they do not directly face to each other, namely said one or more openings 23 face directly towards a portion of the tube plate 100 lacking of apertures 101a.
- the flow outflowing from the latter collides with the impact surface 26 that is configured to give to the flow F' an orthogonal direction to the fluid inlet direction ⁇ into the apertures 101.
- said impact surface 26 of the tube plate 100 comprises said coupling surface A or lies in a plane comprising the latter, as illustrated with reference to the embodiment shown in figure 8 .
- the surface of the tube plate 100 facing toward the second mixing chamber 30 is provided with apertures 101 distributed on opposite sides.
- said impact surface 26 is positioned in a central region of the tube plate 100, namely between said apertures 101.
- the one or more openings 23 of the lamination unit 20 are arranged in such a way as to face said central region of the tube plate 100.
- the impact surface 26 is arranged along a substantially orthogonal direction with respect to a fluid inlet direction into said apertures 101.
- the direction of the refrigerator fluid flow entering the apertures 101 is identifiable by a coordinate system of three axes mutually orthogonal to each other, as shown in the figures.
- the fluid inlet direction ⁇ into the apertures 101 is parallel to axis z that is substantially orthogonal to axis x and y which comprise the plane containing the fluid F' direction, as directed by the impact surface 26.
- refrigerant fluid flow F enters the inlet 11 along the direction ⁇ that coincides with a direction parallel to the z axis
- other embodiments may have different directions of the fluid flow F that enters the inlet 11 than the one shown.
- the positioning of the openings 23 is such that the they directly faces towards one or more of the through holes 101a of the tube plate 100.
- said direction means comprises flow deviation members 24, 25 arranged onto the outlet surface 22 of said lamination unit 20.
- said flow deviation members comprises a wall 24 configured in such a way as to prevent a direct channeling of the fluid F' into the through holes 101a of the tube plate 100.
- said wall 24 protrudes from the outlet surface 22 of the lamination unit 20 in correspondence of its openings 23, specifically it is arranged laterally to said one or more openings 23.
- the wall 24 comprises said impact surface 241 positioned in front of said one or more openings and in such a way as to hinder the fluid flow - outflowing from said one or more openings 23 - to directly enter into at least one of the through holes 101.
- said wall 24 has a "L"-shaped geometry, provided with a proximal lateral portion 242 connected to the impact surface 241.
- the impact surface 241 is configured as a distal portion of said "L"-shaped geometry facing toward said one or more openings and arranged substantially parallel to and spaced from the outlet surface 22.
- the flow direction of the fluid F' is forced into a region of the second mixing chamber 30 comprising the openings 23 and only one of the sides of the plane comprised by the x, y axis, as defined by the interception with the proximal lateral portion 242.
- said proximal lateral portion 242 operates such as a barrier.
- the wall 24 is configured so as to confer to the fluid F' a direction substantially parallel to the development direction of the outlet surface 22.
- said flow deviation members comprise an impact surface provided with one or more connecting portions configured to connect the impact surface to said outlet surface 22 in such a way as to allow the fluid F' outflowing along each of the direction comprised in the x, y plane.
- the impact surface can be positioned in front of and spaced from the openings 23, in such a way as to cover them entirely.
- Said impact surface can be connected to the outlet surface 22 by means of two end opposite walls.
- each of said two end opposite walls develops along a direction parallel to each other and to x axis and/or along an orthogonal direction with respect to the distribution of the openings 23.
- said impact surface can be connected to the outlet surface 22 by means of said two end opposite walls and by a further wall interposed between them, also in order to confer a structural reinforcement to the connection.
- the fluid F' is therefore allowed to outflowing from the lamination unit along a substantially orthogonal direction with respect to the fluid inlet direction ⁇ into apertures of the tube plate 100, without being blocked by side walls that narrow its circulation inside the second mixing chamber 30.
- embodiments may be provided with said wall 24 even though said one or more openings 23 of the lamination unit 20 are arranged such as to do not directly face the through holes 101a of the tube plate 100 when the distributor assembly 1 is flanged to the latter.
- said flow deviation members further comprises one or more ridges 25 - or turbo-stroke ridges - embossed on the outlet surface 22 of the lamination unit 20.
- Said one or more ridges 25 are preferably arranged along an orthogonal transvers direction relative to the direction of fluid outflowing from said one or more openings 23 of the lamination unit 20.
- Said one or more ridges 25 may protrude from the outlet surface 22 with different heights and have sections with polygonal or curvilinear geometries.
- Said ridges can also be made in a single piece with the lamination unit 20 or fixed to the latter, the amount of which is function of the desired outlet conditions to be conferred to the fluid flow F'.
- Said ridges can be also designed for the purpose to gain a structural reinforcement of the lamination unit 20 and eventually can be configured as spacer between the tube plate 100 and the outlet surface 22.
- ridges 25' are arranged along a longitudinal direction with respect to the flow F'.
- the flow F' is orthogonal to the fluid inlet direction ⁇ into the tube plate 100 so as to sequentially lick said apertures 101.
- said ridges 25' are spaced from and parallel to each other in such a way as to define a plurality of lanes 25".
- Each of said ridges 25' has a length preferably shorter than the length of the lamination unit 20, considering the latter length comprised between the shoulders 13a of the head unit 10 and parallel to the direction of the fluid flow F'.
- the ridges 25' allow to divide the second mixing chamber 30 in such a way as to constrain the fluid F', outflowing from said one or more openings 23, in a plurality of delimited regions.
- Each region of said plurality preferably developing along a main developing direction that is substantially parallel to the direction x, as above defined and also with reference to figure 2 and 10 .
- the presence of ridges 25' advantageously allows to avoid the fluid to move towards and stagnate into an area 15' of the second mixing chamber 30 which is far located from the openings 23 of tube plate 100.
- each of the ridges 25' preferably projects from the outlet surface 22 in such a way as to maintain the latter and the tube plate 100 spaced therebetween.
- Said spacing advantageously, allows the fluid to reach every tubular member of the tube bundle even in case of a bad distribution upstream of said one or more openings 23.
- ridges 25' can be configured as spacer between the tube plate 100 and the outlet surface 22. Said spacing can be obtained, for example, by providing a battlement shape along the length of ridges 25' properly dimensioned to contact in selected points the tube plate 100.
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Details Of Heat-Exchange And Heat-Transfer (AREA)
Description
- The present invention relates to the field of aeraulic systems, in particular of conditioning systems.
- The present invention, more specifically, relates to a fluid distributor assembly suitable for use in a heat exchanger, in particular an evaporator.
- Heat exchangers used in conditioning systems are devices that, in the most general terms, comprise a casing - or mantle - inside which is housed a tube bundle. Within the tube bundle, a service fluid flows to exchange heat with a process fluid at a different temperature.
- In some heat exchangers, such as evaporators, the service fluid is typically an evaporating refrigerant fluid that circulates inside the tube bundle and cools the process fluid. The latter passes externally to the tube bundle housed within the mantle, passing through the heat exchanger.
- Generally, a supply pipe feeds the heat exchanger with refrigerant fluid, engaging it at a head unit - or manifold - thereof. In order to canalize the refrigerant fluid into the tube bundle, the exchanger is generally equipped with a dedicated distributor device.
- For example, JPH1089885 discloses a tank for a heat exchanger wherein an inlet section is equipped with a junction element provided with sacrificial corrosion members.
- Structurally, the known distributor devices typically provide a plurality of fed conduits each engaging a respective tubular element of the tube bundle. Solutions of this type however have the drawback of being constructively complex due to expensive and sophisticate mechanical machining of the fed conduits connecting structure in order to maintain desired outlet conditions while conveying the fluid in each tube of the bundle.
- Moreover, such solution often does not guarantee uniform distribution of the flow of refrigerant fluid in the tube bundle, significantly decreasing the performance of the heat exchanger in which the above mentioned type of distributors are mounted.
- The technical problem placed and solved by the present invention is then to provide a fluid distributor assembly, in particular a refrigerant fluid, within the tube bundle of a heat exchanger that allows to overcome the above-illustrated drawbacks with reference to the prior art.
- This problem is solved by a distributor assembly according to
claim 1. Additional preferred features of the present invention are defined in the depending claims. - The fluid distributor assembly according to present invention is structurally simple and economical to be realized, due to the presence of a lamination unit housed in a seat of the head unit in such a way that, a mixing chamber of refrigerant fluid that feeds the latter is defined.
- More in detail, the fluid distributor assembly comprises direction means provided with an impact surface and configured so as to direct the fluid outflowing from said lamination unit along a substantially orthogonal direction with respect to a fluid inlet direction into apertures of the tube plate engaging the tube bundle of the exchanger.
- This solution overcome the need to provide complex, tricky and high-costly working process of single-engagements conduits intended to engage a respective tubular element of the tube bundle to feed each tube individually. Furthermore, the presence of said direction means allows to create fluid agitation conditions in the mixing chamber prior to its entry into the tube bundle. Particularly, said orthogonal flow to the fluid inlet direction into the tube plate is generated so as to sequentially lick the tube plate apertures and to allow each tube to suck the required amount of refrigerant, according to a kind of dynamical "self-regulation".
- In this way, a uniform distribution of the fluid flow into the tube bundle is favored and the efficiency of the exchanger in which the fluid distributor assembly according to the present invention is mounted significantly improves.
- Other advantages, features and operation modes of the present invention will be made apparent from the following detailed description of some embodiments thereof, given by way of example and not for limitative purposes.
- Reference will be made to the figures of the annexed drawings, wherein:
-
figure 1 shows an exploded view of a preferred embodiment of a fluid distributor assembly according to the present invention; -
figure 2 shows an enlarged view of a section offigure 1 , wherein a first component - the lamination unit - of the distributor assembly is partially housed in the latter; -
figure 3 shows a side view of a portion of the distributor assembly according to the present invention shown infigure 1 ; -
figure 4 shows a front view of the distributor assembly offigure 1 ; -
figures 5 and 6 show a section of a portion of a side view of the distributor assembly offigure 1 respectively in a uncoupled and coupled condition; -
figures 7 and 8 respectively show an exploded view of a further embodiment of a fluid distributor assembly according to the present invention and a section of a portion of a side view of the distributor assembly offigure 7 in a coupled condition; -
Figures 9 and 10 respectively show an exploded view of a further embodiment of a fluid distributor assembly according to the present invention and a section of a portion of a side view of the distributor assembly offigure 9 in a coupled condition. - The present invention will be described hereinafter by referring to the above-mentioned figures.
- By referring to
figure 1 , an exploded view of a preferred embodiment of afluid distributor assembly 1, in particular a refrigerant fluid, according to the present invention is illustrated by way of example and not for limitative purposes. - The
distributor assembly 1 of the present invention is intended for a preferred use in heat exchangers, preferably evaporators, such as direct evaporators. - In the embodiments illustrated, the
distributor assembly 1 is shown in association with atube plate 100, the latter being an element to which thedistributor assembly 1 is intended to be coupled. - The
tube plate 100 is a plate with a circular geometry, exemplifying the tubular plates used in the considered technical field. However, thetube plate 100 shown is not limitative for the purposes of the present invention. - In particular, the
distributor assembly 1 comprises a head unit 10 - or manifold - configured to receive the refrigerant fluid inletting the heat exchanger and is intended to be coupled to thetube plate 100 at a coupling surface - denoted with reference A - thereof. - The
head unit 10 therefore comprises at least oneinlet 11 port, in fluid communication with the inlet refrigerant fluid flow, which allows the latter to entersaid head unit 10. - Internally, the
head unit 10 is thus a hollow element, that is an element in which is defined atransit region 12 through which the inlet fluid flow passes towards thetube plate 100. - In the showed examples, the
inlet 11 in thehead unit 10 are intended to be two, however, in other embodiments, said inlet can be different in numbers, for example one or four, depending on the operating modes of the exchanger in which the distributor assembly according to the present invention will be mounted. - Typically, the coupling surface A - also with reference to the shown examples - is a peripheral region of the
head unit 10 and of therespective tube plate 100, shaped so as to flange the above-mentioned two elements together. - In the illustrated examples, this peripheral region defines a circular crown, however, different coupling geometries are possible.
- In any case, and as well-known to the skilled person in the field, the
tube plate 100 of a heat exchanger comprises a zone having a plurality of apertures - or housings 101 - configured to put in fluid communication saidhead inlet 11 and tubes of the exchanger. - That is, each aperture of said plurality is suitable for coupling with respective tubular elements (not shown in the figures) within which, in use, the refrigerant fluid flows.
- The plurality of housings 101 - which in the examples are a plurality of through
holes 101a of the plate 100 - are configured to allow the refrigerant fluid inletting thehead unit 10 passing towards tubular elements which typically engage with their terminal end theplate 100 at said housings, and which form the tube bundle housed within the exchanger's casing. - For the sake of an easy depiction, in showed examples said
housings 101 are obtained only on a portion of theplate 100, particularly on the portion corresponding to one of the twoinlet 11 of thehead unit 10. However, it is to be understood that thedistributor assembly 1 can be coupled with atube plate 100 having a housings distribution different from that one illustrated. - Also with reference to
figure 5 and 6 , thehead unit 10 is further provided with aseat 13 adapted to receive alamination unit 20, in particular of a plate-shaped geometry, whichlamination unit 20 is positioned in saidseat 13 so as to divide thetransit region 12 of thehead unit 10 in afirst collecting chamber 14 and in anoutlet region 15 of the refrigerant fluid. - The plate-
shaped lamination unit 20 comprises aninlet surface 21, anoutlet surface 22 and one ormore openings 23 to allow the fluid entering thehead unit 10 to pass there through. - The
first collecting chamber 14 is comprised between theinlet 11 adapted to receive the fluid entering thehead unit 10 and saidinlet surface 21. - The
outlet surface 22 of the plate-shaped lamination unit 20 faces toward saidoutlet region 15 of the refrigerant fluid. - Said one or
more openings 23 are appropriately sized to obtain a pressure drop across thelamination unit 20. - The overall configuration of the
distributor assembly 1 being such that, in condition of saidhead unit 10 coupled to thetube plate 100, asecond mixing chamber 30 is defined at saidoutlet region 15 among said coupling surface A, saidlamination unit 20 and thetube plate 100, so that the fluid, in use, sequentially crosses thefirst collecting chamber 14, the one ormore openings 23 in thelamination unit 20 and subsequently thesecond mixing chamber 30. - The fluid is so administered into tubes connected to the
tube plate 100. - The
first collecting chamber 14 and thesecond mixing chamber 30 are preferably consecutive with each other and saidoutlet region 15 is adjacent to saidoutlet surface 22. - In particular, the
first collecting chamber 14 and thesecond mixing chamber 30 are preferably arranged in sequence with respect to a fluid flow direction α as defined by thehead inlet 11. - Under operating conditions of the
distributor assembly 1, thelamination unit 20 thus allows expansion of the refrigerant fluid in thesecond mixing chamber 30 with respect to the condition in which the fluid is in thefirst collecting chamber 14. - More in detail, and with reference to
figure 2 and6 , the refrigerant fluid flow F entering theinlet 11 of thehead unit 10 reaches thelamination unit 20 and crosses said one ormore openings 23 of the latter being subjected to a pressure drop causing it to expand into thesecond mixing chamber 30 and to generate a turbulent flow regime. - The presence of said
mixing chamber 30 permits to improve the refrigerant fluid flow F' conditions before its inlet into the exchanger tube bundle, namely achieving a uniform mixing of the latter entering the throughholes 101a of thetube plate 100. - The
lamination unit 20, as shown in the examples, is locked to theseat 13 of thehead unit 10 ontoshoulders 13a thereof. It is preferably fixed to the latter in a removable manner, by means of fastening means known to the skilled person in the field. - According to one embodiment a spacer is configured to allow the fastening of the
lamination unit 20 to theseat 13, wherein said spacer comprises a first and a second portion. - The first portion is internally hollow and configured to engage a through
hole 101a of thetube plate 100 and the second portion remains outside of the tube plate in such a way as to maintain the lamination unit in abutment onto saidshoulders 13a of thehead unit 10, spaced from thetube plate 100. - On a side of said second portion, an opening in fluid communication with said first portion is obtained, in order to allow the refrigerant fluid flowing toward the through
hole 101a to enter thereof. - More than one spacer can be provided, the number of which is function of the operative condition of the distributor. Preferably, said spacers are provided in a homogeneous chessboard-like distribution.
- In a preferred embodiment, the
lamination unit 20 is however secured in such a way as to make the collectingchamber 14 hermetic, to avoid possible undesired fluid leaks towards thesecond mixing chamber 30. - In other embodiments, the
lamination unit 20 can also be made in a single piece with thehead unit 10 at saidseat 13. - Preferably, with reference to the examples illustrated in the figures, the plate-shaped lamination unit 20 - or at least its outlet surface 22 - lies on a plane substantially parallel to the coupling surface A with the
tube plate 100. According to said configuration, advantageously the fluid F' outflows from thelamination unit 20 at equidistant points from the throughholes 101a of saidtube plate 100, further favoring a uniform mixing of the fluid F' entering the latter. - With reference to
figure 2 and6 , said one or more openings of thelamination unit 20, are denoted byreference 23. In the examples illustrated, saidopenings 23 comprise a plurality of circular geometric through holes, and are apt to put in fluid communication the first collectingchamber 14 with thesecond mixing chamber 30. - Alternative embodiments can also provide that at least one of said one or
more openings 23 comprise an elongated shape, for examples like a single slot, or through holes of other geometric shapes than the circular shape. - Said one or more openings may have, for example, a passageway configured so as to impart a substantially orthogonal direction to the fluid F' outflowing from the
outlet surface 22 with respect to the direction of the fluid F inletting thelamination unit 20. - In any case, the amount and geometry of said one or more openings is a function of the operating conditions of the exchanger and of the desired fluid F pressure drop across the
lamination unit 20. - Said one or
more openings 23 are preferably distributed along a peripheral edge of the plate-shapedlamination unit 20, preferably in such a way as to do not directly face one or more of the throughholes 101a of thetube plate 100, as provided by the embodiment offigures 7 and 8 . - Preferably, said one or
more openings 23 are arranged laterally with respect to an input fluid flow F having a direction α as imparted by saidhead inlet 11. - It is to be appreciated that the
fluid distributor assembly 1 further comprises direction means provided with animpact surface 241, 26 configured so as to direct the fluid outflowing from saidoutlet surface 22 along a substantially orthogonal direction with respect to a fluid inlet direction β into saidapertures 101. - Said direction means allow to generate an orthogonal flow F' with respect to the fluid inlet direction β into the
tube plate 100 so as to sequentially lick saidapertures 101. - Each tube of the tube bundle of the exchanger is therefore able to suck the required amount of refrigerant, according to a kind of dynamical "self-regulation".
- In general terms, said orthogonal flow F' with respect to said direction β is achieved by providing an antagonistic element positioned downstream the expansion of the flow outflowing the
outlet surface 22. - With reference to the embodiment shown in
figures 7 and 8 , theapertures 101 of thetube plate 100 are arranged laterally with respect to a positioning of each of said one ormore openings 23 of thelamination unit 20. - According to said positioning, said direction means comprises an impact surface 26 of the
tube plate 100 facing toward said second mixingchamber 30. - In other words, the mutual position of each of said
apertures 101 and each of said one ormore openings 23 is such that they do not directly face to each other, namely said one ormore openings 23 face directly towards a portion of thetube plate 100 lacking ofapertures 101a. - The flow outflowing from the latter collides with the impact surface 26 that is configured to give to the flow F' an orthogonal direction to the fluid inlet direction β into the
apertures 101. - Preferably said impact surface 26 of the
tube plate 100 comprises said coupling surface A or lies in a plane comprising the latter, as illustrated with reference to the embodiment shown infigure 8 . - In one embodiment - not illustrated - the surface of the
tube plate 100 facing toward thesecond mixing chamber 30 is provided withapertures 101 distributed on opposite sides. In this case, said impact surface 26 is positioned in a central region of thetube plate 100, namely between saidapertures 101. - Accordingly to this embodiment, the one or
more openings 23 of thelamination unit 20 are arranged in such a way as to face said central region of thetube plate 100. - Preferably, the impact surface 26 is arranged along a substantially orthogonal direction with respect to a fluid inlet direction into said
apertures 101. - According to this feature, the direction of the refrigerator fluid flow entering the
apertures 101 is identifiable by a coordinate system of three axes mutually orthogonal to each other, as shown in the figures. - The fluid inlet direction β into the
apertures 101 is parallel to axis z that is substantially orthogonal to axis x and y which comprise the plane containing the fluid F' direction, as directed by the impact surface 26. - Although in the examples the refrigerant fluid flow F enters the
inlet 11 along the direction α that coincides with a direction parallel to the z axis, other embodiments may have different directions of the fluid flow F that enters theinlet 11 than the one shown. - Referring now to
figure 3 and 4 , wherein in the latter figure saidtube plate 100 is represented in transparency to show thelamination unit 20. - In this example, referring also to
figures 5 and 6 , the positioning of theopenings 23 is such that the they directly faces towards one or more of the throughholes 101a of thetube plate 100. - According to this embodiment, said direction means comprises
flow deviation members outlet surface 22 of saidlamination unit 20. - Preferably, said flow deviation members comprises a
wall 24 configured in such a way as to prevent a direct channeling of the fluid F' into the throughholes 101a of thetube plate 100. - With further reference to
figure 2 , saidwall 24 protrudes from theoutlet surface 22 of thelamination unit 20 in correspondence of itsopenings 23, specifically it is arranged laterally to said one ormore openings 23. - Preferably, the
wall 24 comprises saidimpact surface 241 positioned in front of said one or more openings and in such a way as to hinder the fluid flow - outflowing from said one or more openings 23 - to directly enter into at least one of the throughholes 101. - Preferably, said
wall 24 has a "L"-shaped geometry, provided with a proximallateral portion 242 connected to theimpact surface 241. - The
impact surface 241 is configured as a distal portion of said "L"-shaped geometry facing toward said one or more openings and arranged substantially parallel to and spaced from theoutlet surface 22. - In this example, the flow direction of the fluid F' is forced into a region of the
second mixing chamber 30 comprising theopenings 23 and only one of the sides of the plane comprised by the x, y axis, as defined by the interception with the proximallateral portion 242. - In other words, said proximal
lateral portion 242 operates such as a barrier. - Different geometries of said
wall 24 are possible. Preferably thewall 24 is configured so as to confer to the fluid F' a direction substantially parallel to the development direction of theoutlet surface 22. - In a further embodiment - not shown in the figures - said flow deviation members comprise an impact surface provided with one or more connecting portions configured to connect the impact surface to said
outlet surface 22 in such a way as to allow the fluid F' outflowing along each of the direction comprised in the x, y plane. - For example, the impact surface can be positioned in front of and spaced from the
openings 23, in such a way as to cover them entirely. Said impact surface can be connected to theoutlet surface 22 by means of two end opposite walls. - Preferably, each of said two end opposite walls develops along a direction parallel to each other and to x axis and/or along an orthogonal direction with respect to the distribution of the
openings 23. - More preferably, said impact surface can be connected to the
outlet surface 22 by means of said two end opposite walls and by a further wall interposed between them, also in order to confer a structural reinforcement to the connection. - Advantageously, in this way the fluid F' is therefore allowed to outflowing from the lamination unit along a substantially orthogonal direction with respect to the fluid inlet direction β into apertures of the
tube plate 100, without being blocked by side walls that narrow its circulation inside thesecond mixing chamber 30. - In any case, embodiments may be provided with said
wall 24 even though said one ormore openings 23 of thelamination unit 20 are arranged such as to do not directly face the throughholes 101a of thetube plate 100 when thedistributor assembly 1 is flanged to the latter. - Preferably, said flow deviation members further comprises one or more ridges 25 - or turbo-stroke ridges - embossed on the
outlet surface 22 of thelamination unit 20. - Said one or
more ridges 25 are preferably arranged along an orthogonal transvers direction relative to the direction of fluid outflowing from said one ormore openings 23 of thelamination unit 20. - Said one or
more ridges 25 may protrude from theoutlet surface 22 with different heights and have sections with polygonal or curvilinear geometries. - Said ridges can also be made in a single piece with the
lamination unit 20 or fixed to the latter, the amount of which is function of the desired outlet conditions to be conferred to the fluid flow F'. - Said ridges can be also designed for the purpose to gain a structural reinforcement of the
lamination unit 20 and eventually can be configured as spacer between thetube plate 100 and theoutlet surface 22. - With now reference to the embodiment shown in
figure 9 and 10 , ridges 25' are arranged along a longitudinal direction with respect to the flow F'. The flow F' is orthogonal to the fluid inlet direction β into thetube plate 100 so as to sequentially lick saidapertures 101. - Accordingly to this embodiment, said ridges 25' are spaced from and parallel to each other in such a way as to define a plurality of
lanes 25". - Each of said ridges 25' has a length preferably shorter than the length of the
lamination unit 20, considering the latter length comprised between theshoulders 13a of thehead unit 10 and parallel to the direction of the fluid flow F'. - In the example depicted there are three ridges 25' defining four
lanes 25". - However, other embodiments may be provided with different numbers of ridges 25' and therefore different number of
lanes 25". - In other words, the ridges 25' allow to divide the
second mixing chamber 30 in such a way as to constrain the fluid F', outflowing from said one ormore openings 23, in a plurality of delimited regions. - Each region of said plurality preferably developing along a main developing direction that is substantially parallel to the direction x, as above defined and also with reference to
figure 2 and10 . - Whereas a uniform mixture of the fluid is achieved after the expansion through the
lamination unit 20 and, for example, under those particular operating conditions wherein the fluid does not reach quickly the throughholes 101a of thetube plate 100, the presence of ridges 25' advantageously allows to avoid the fluid to move towards and stagnate into an area 15' of thesecond mixing chamber 30 which is far located from theopenings 23 oftube plate 100. - At the same time, a configuration of the ridges 25' as above described allows the fluid to reach every point of the
second mixing chamber 30 as well. Accordingly, each of the ridges 25' preferably projects from theoutlet surface 22 in such a way as to maintain the latter and thetube plate 100 spaced therebetween. - Said spacing, advantageously, allows the fluid to reach every tubular member of the tube bundle even in case of a bad distribution upstream of said one or
more openings 23. - As well as described for a particular embodiment of
ridges 25, also ridges 25' can be configured as spacer between thetube plate 100 and theoutlet surface 22. Said spacing can be obtained, for example, by providing a battlement shape along the length of ridges 25' properly dimensioned to contact in selected points thetube plate 100. - The present invention has hereto been described with reference to preferred embodiments thereof. It is understood that other embodiments might exist, all falling within the concept of the same invention, as defined by the protective scope of the claims hereinafter.
Claims (18)
- A fluid distributor assembly (1), in particular for a refrigerant fluid, for use in a heat exchanger, which fluid distributor (1) comprises:- a head unit (10), comprising a head inlet (11) configured to receive the fluid fed into the exchanger;- a tube plate (100) coupled to said head unit (10) at a coupling surface (A) thereof and provided with apertures (101) configured to put in fluid communication said head inlet (11) and tubes of the exchanger;characterised in that the fluid distributor assembly (1) further comprises- a plate-shaped lamination unit (20) having an inlet surface (21) and an outlet surface (22) and further comprising one or more openings (23) to allow the inlet fluid to pass therethrough,wherein the head unit (10) is provided with a seat (13) which fixedly receives said lamination unit (20), the overall configuration of the distributor assembly (1) being such that the fluid sequentially crosses a first collecting chamber (14) defined between said inlet surface (21) and said head inlet (11), said one or more openings (23) and a second mixing chamber (30) defined between said coupling surface (A) and said outlet surface (22), and it is so administered into the tubes of said tube plate (100),
wherein the lamination unit (20) allows an expansion of the fluid in the second mixing chamber (30) with respect to the first collecting chamber (14),
and wherein the fluid distributor assembly (1) further comprises direction means provided with an impact surface (241, 26) arranged downstream of said openings (23), which impact surface (241, 26) is configured so as to direct the fluid outflowed from said openings (23) along a substantially orthogonal direction with respect to a fluid inlet direction into said apertures (101). - The fluid distributor assembly (1) according to claim 1, wherein said apertures (101) are arranged laterally with respect to a positioning of said one or more openings (23), and wherein said impact surface (26) is a surface of the tube plate (100) facing toward said second mixing chamber (30).
- The fluid distributor assembly (1) according to claim 2, wherein said impact surface (26) is arranged along a substantially orthogonal direction with respect to a fluid inlet direction into said apertures (101).
- The fluid distributor assembly (1) according to claim 2 or 3, wherein said impact surface (26) lies on a plane comprising said coupling surface (A).
- The fluid distributor assembly (1) according any one of the preceding claims, wherein said direction means comprises flow deviation members (24, 25, 25') arranged onto the outlet surface (22) of said lamination unit (20).
- The fluid distributor assembly (1) according to claim 5, wherein said flow deviation members comprise a wall (24) arranged laterally to said one or more openings (23) and configured in such a way as to confer to the fluid a motion having a direction substantially parallel to said outlet surface (22).
- The fluid distributor assembly (1) according to claim 6, wherein said wall (24) is substantially "L" shaped and comprises said impact surface (241).
- The fluid distributor assembly (1) according to claim 5, wherein said flow deviation members comprise two opposite end walls configured to connect said impact surface to said outlet surface (22), said two opposite connecting walls developing along a direction parallel to each other and/or orthogonal with respect to a distribution of said one or more openings (23).
- The fluid distributor assembly (1) according to any claim from 5 to 8, wherein said flow deviation members comprises one or more ridges (25) arranged along an orthogonal transverse direction relative to a direction of fluid outflowing as defined by said one or more openings (23).
- The fluid distributor assembly (1) according to any claim from 5 to 8, wherein said flow deviation members comprises ridges (25') arranged along a longitudinal transverse direction relative to a direction of fluid outflowing as defined by said one or more openings (23), wherein said ridges (25') are spaced from and parallel to each other in such a way as to define a plurality of lanes (25") therebetween.
- The fluid distributor assembly (1) according to any one of the preceding claims, wherein said one or more openings (23) are distributed along a peripheral edge of said lamination unit (20).
- The fluid distributor assembly (1) according to any one of the preceding claims, wherein said one or more openings (23) are arranged laterally with respect to an input fluid flow as directed by said head inlet (11).
- The fluid distributor assembly (1) according to any one of the preceding claims, wherein said one or more openings (23) comprise holes with a circular geometry.
- The fluid distributor assembly (1) according to any one of the preceding claims, wherein at least one of said one or more openings (23) comprise an elongated shape, in particular a single slot.
- The fluid distributor assembly (1) according to any one of the preceding claims, wherein said lamination unit (20) is a plate-shaped element made in a single piece with said head unit (10).
- The fluid distributor assembly (1) according to any one of the preceding claims, wherein the plate-shaped lamination unit (20) lies on a plane substantially parallel to a plane comprising the coupling surface (A).
- The fluid distributor assembly (1) according to any one of the preceding claims, wherein said first collecting chamber (14) and said second mixing chamber (30) are arranged in sequence with respect to a fluid flow direction as defined by the head inlet (11).
- A heat exchanger (100) comprising a fluid distributor assembly (1) according to any one of the preceding claims.
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP17184287.5A EP3438596B1 (en) | 2017-08-01 | 2017-08-01 | Improved fluid distributor |
PCT/IB2018/055719 WO2019025963A1 (en) | 2017-08-01 | 2018-07-31 | Improved fluid distributor |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP17184287.5A EP3438596B1 (en) | 2017-08-01 | 2017-08-01 | Improved fluid distributor |
Publications (2)
Publication Number | Publication Date |
---|---|
EP3438596A1 EP3438596A1 (en) | 2019-02-06 |
EP3438596B1 true EP3438596B1 (en) | 2020-04-08 |
Family
ID=59506184
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP17184287.5A Active EP3438596B1 (en) | 2017-08-01 | 2017-08-01 | Improved fluid distributor |
Country Status (2)
Country | Link |
---|---|
EP (1) | EP3438596B1 (en) |
WO (1) | WO2019025963A1 (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112033048B (en) * | 2020-08-31 | 2022-09-16 | 青岛海尔空调电子有限公司 | Dry evaporator |
Family Cites Families (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DD137276A1 (en) * | 1978-06-30 | 1979-08-22 | Johannes Grund | FLUID COOLER FOR WAFER TRANSFER AND METHOD FOR FIXING IT |
US5465783A (en) * | 1994-03-04 | 1995-11-14 | Fedco Automotive Components Company, Inc. | Sacrificial erosion bridge for a heat exchanger |
JPH1089885A (en) * | 1996-09-11 | 1998-04-10 | Calsonic Corp | Connecting section between metallic tank and metallic inlet pipe for heat exchanger |
JP2003065696A (en) * | 2001-08-24 | 2003-03-05 | Honda Motor Co Ltd | Radiator |
JP5114771B2 (en) * | 2007-05-29 | 2013-01-09 | 株式会社ケーヒン・サーマル・テクノロジー | Heat exchanger |
US9174192B2 (en) * | 2009-01-21 | 2015-11-03 | Basf Se | Tube bundle reactor for uncatalyzed or homogeneously catalyzed reactions |
AT507552B1 (en) * | 2009-05-22 | 2010-06-15 | Siemens Vai Metals Tech Gmbh | METHOD AND DEVICE FOR INFLUENCING FLOW CHARACTERISTICS IN A FLUID CURRENT |
ITMI20100249U1 (en) * | 2010-07-16 | 2012-01-17 | Alfa Laval Corp Ab | HEAT EXCHANGE DEVICE WITH REFRIGERANT FLUID DISTRIBUTION SYSTEM |
JP5795994B2 (en) * | 2012-07-09 | 2015-10-14 | 住友精密工業株式会社 | Heat exchanger |
US10072900B2 (en) * | 2014-09-16 | 2018-09-11 | Mahle International Gmbh | Heat exchanger distributor with intersecting streams |
US10553322B2 (en) * | 2015-09-28 | 2020-02-04 | Ge-Hitachi Nuclear Energy Americas Llc | Modular fluid flow distribution system in which differently shaped plates can be rearranged to different positions |
-
2017
- 2017-08-01 EP EP17184287.5A patent/EP3438596B1/en active Active
-
2018
- 2018-07-31 WO PCT/IB2018/055719 patent/WO2019025963A1/en active Application Filing
Non-Patent Citations (1)
Title |
---|
None * |
Also Published As
Publication number | Publication date |
---|---|
EP3438596A1 (en) | 2019-02-06 |
WO2019025963A1 (en) | 2019-02-07 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
EP2079973B1 (en) | Multi-pass heat exchangers having return manifolds with distributing inserts | |
US10571205B2 (en) | Stacking-type header, heat exchanger, and air-conditioning apparatus | |
EP2998679B1 (en) | Laminated header, heat exchanger, and air conditioner | |
EP2889570B1 (en) | Heat exchanger | |
US7967060B2 (en) | Evaporating heat exchanger | |
US8485248B2 (en) | Flow distributor for a heat exchanger assembly | |
US10801783B2 (en) | Heat exchanger and heat exchange module | |
WO2012176336A1 (en) | Plate heater and refrigeration cycle device | |
EP1435502B1 (en) | Laminated heat exchanger | |
US20210041120A1 (en) | Steam dispersion system | |
EP3438596B1 (en) | Improved fluid distributor | |
EP3971508A1 (en) | Heat exchanger | |
CN110940204B (en) | Heat exchanger and air conditioner provided with same | |
US20110139421A1 (en) | Flow distributor for a heat exchanger assembly | |
CN102563980A (en) | Heat exchanger | |
CN107223198B (en) | Fin for fin group of heat exchanger and heat exchanger | |
EP3619492B1 (en) | Heat exchanger for heat pump applications | |
EP3572743B1 (en) | Heat exchanger assembly | |
CN214666186U (en) | Heat exchanger | |
CN216347194U (en) | Liquid separation device and air conditioner | |
JP7142806B1 (en) | Distributors, heat exchangers and heat pump devices | |
EP4067800A1 (en) | Heat exchanger | |
JP2018096559A (en) | Heat exchanger | |
CN115993000A (en) | Heat exchanger and heat exchange system | |
CN113203307A (en) | Plate heat exchanger and heat exchange system with same |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PUAI | Public reference made under article 153(3) epc to a published international application that has entered the european phase |
Free format text: ORIGINAL CODE: 0009012 |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: THE APPLICATION HAS BEEN PUBLISHED |
|
AK | Designated contracting states |
Kind code of ref document: A1 Designated state(s): AL AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO PL PT RO RS SE SI SK SM TR |
|
AX | Request for extension of the european patent |
Extension state: BA ME |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: REQUEST FOR EXAMINATION WAS MADE |
|
17P | Request for examination filed |
Effective date: 20190710 |
|
RBV | Designated contracting states (corrected) |
Designated state(s): AL AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO PL PT RO RS SE SI SK SM TR |
|
GRAP | Despatch of communication of intention to grant a patent |
Free format text: ORIGINAL CODE: EPIDOSNIGR1 |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: GRANT OF PATENT IS INTENDED |
|
INTG | Intention to grant announced |
Effective date: 20191119 |
|
GRAS | Grant fee paid |
Free format text: ORIGINAL CODE: EPIDOSNIGR3 |
|
GRAA | (expected) grant |
Free format text: ORIGINAL CODE: 0009210 |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: THE PATENT HAS BEEN GRANTED |
|
AK | Designated contracting states |
Kind code of ref document: B1 Designated state(s): AL AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO PL PT RO RS SE SI SK SM TR |
|
REG | Reference to a national code |
Ref country code: AT Ref legal event code: REF Ref document number: 1254959 Country of ref document: AT Kind code of ref document: T Effective date: 20200415 Ref country code: CH Ref legal event code: EP |
|
REG | Reference to a national code |
Ref country code: DE Ref legal event code: R096 Ref document number: 602017014256 Country of ref document: DE |
|
REG | Reference to a national code |
Ref country code: IE Ref legal event code: FG4D |
|
REG | Reference to a national code |
Ref country code: NL Ref legal event code: MP Effective date: 20200408 |
|
REG | Reference to a national code |
Ref country code: LT Ref legal event code: MG4D |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: IS Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20200808 Ref country code: NO Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20200708 Ref country code: FI Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20200408 Ref country code: GR Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20200709 Ref country code: PT Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20200817 Ref country code: NL Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20200408 Ref country code: LT Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20200408 Ref country code: SE Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20200408 |
|
REG | Reference to a national code |
Ref country code: AT Ref legal event code: MK05 Ref document number: 1254959 Country of ref document: AT Kind code of ref document: T Effective date: 20200408 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: LV Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20200408 Ref country code: HR Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20200408 Ref country code: RS Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20200408 Ref country code: BG Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20200708 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: AL Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20200408 |
|
REG | Reference to a national code |
Ref country code: DE Ref legal event code: R097 Ref document number: 602017014256 Country of ref document: DE |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: SM Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20200408 Ref country code: AT Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20200408 Ref country code: EE Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20200408 Ref country code: DK Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20200408 Ref country code: CZ Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20200408 Ref country code: ES Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20200408 Ref country code: RO Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20200408 |
|
PLBE | No opposition filed within time limit |
Free format text: ORIGINAL CODE: 0009261 |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: NO OPPOSITION FILED WITHIN TIME LIMIT |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: PL Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20200408 Ref country code: SK Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20200408 |
|
26N | No opposition filed |
Effective date: 20210112 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: SI Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20200408 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: TR Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20200408 Ref country code: CY Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20200408 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: MK Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20200408 |
|
REG | Reference to a national code |
Ref country code: DE Ref legal event code: R081 Ref document number: 602017014256 Country of ref document: DE Owner name: WIELAND PROVIDES SRL, IT Free format text: FORMER OWNER: PROVIDES METALMECCANICA S.R.L., LATINA, IT |
|
REG | Reference to a national code |
Ref country code: LU Ref legal event code: HC Owner name: WIELAND PROVIDES SRL.; IT Free format text: FORMER OWNER: PROVIDES METALMECCANICA S.R.L. Effective date: 20230224 |
|
REG | Reference to a national code |
Ref country code: BE Ref legal event code: HC Owner name: WIELAND PROVIDES S.R.L.; IT Free format text: DETAILS ASSIGNMENT: CHANGE OF OWNER(S), CHANGE OF OWNER(S) NAME; FORMER OWNER NAME: PROVIDES METALMECCANICA S.R.L. Effective date: 20230306 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: IT Payment date: 20230804 Year of fee payment: 7 Ref country code: CH Payment date: 20230902 Year of fee payment: 7 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: MT Payment date: 20230721 Year of fee payment: 7 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: LU Payment date: 20240821 Year of fee payment: 8 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: DE Payment date: 20240821 Year of fee payment: 8 Ref country code: IE Payment date: 20240827 Year of fee payment: 8 Ref country code: MC Payment date: 20240823 Year of fee payment: 8 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: GB Payment date: 20240826 Year of fee payment: 8 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: BE Payment date: 20240821 Year of fee payment: 8 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: FR Payment date: 20240829 Year of fee payment: 8 |