The field of the present invention is that of the heat exchangers equipping air conditioning installations for vehicles, notably motor vehicles. The invention more specifically concerns the distribution of the refrigerant fluid inside a header that a heat exchanger of this kind includes and consists in a refrigerant fluid distribution device, the associated header and the associated heat exchanger.
A vehicle is routinely equipped with an air conditioning installation for heat treatment of the passenger compartment of the vehicle. An installation of this kind then cooperates with a closed loop refrigerant fluid circuit. That refrigerant fluid circuit comprises in succession, in the direction of circulation of the refrigerant fluid, a compressor, a condenser, a thermostatic expansion valve and at least one heat exchanger.
The heat exchanger can notably be a tube exchanger in which a bundle of tubes extends between a header and a return box for the refrigerant fluid. The refrigerant fluid is admitted via an inlet opening to the interior of the header, circulates in successive paths in the tubes of the bundle between the header and a return box, and is then evacuated from the heat exchanger via an outlet opening. The outlet opening can be formed in the header or the return box.
The heat exchanger is for example a condenser, an evaporator or a liquid cooler. This heat exchanger is intended to perform an exchange of heat between the refrigerant fluid and a flow of fluid, such as respectively outside air, a flow of air circulating in the air conditioning installation or a heat-exchange fluid. To this end, the refrigerant fluid circulates inside the tubes of the bundle and the flow of fluid circulates between the tubes of the bundle to cool it, the exchange of heat being effected by conduction.
However, a disadvantage linked to a heat exchanger of this kind resides in heterogeneous feeding of the tubes of the bundle. In particular, the refrigerant fluid is admitted to the interior of the heat exchanger in a diphase liquid/gas state, and the difference between the physical properties of a liquid and a gas means that the liquid phase and the gas phase of the refrigerant fluid tend to separate. As a result, the tubes of the bundle closest to the inlet opening can then be fed mainly with liquid whereas the tubes of the bundle at the greatest distance from the inlet opening may be fed mainly with gas, or vice versa depending on the arrangement of the heat exchanger.
The heterogeneous feeding of the tubes of the bundle then generates a disparity in the exchange of heat between the refrigerating fluid and the flow of fluid through the heat exchanger and a disparity in the temperature of the flow of fluid that has passed through the heat exchanger in use. This heterogeneity complicates the thermal management of the installation that receives the heat exchanger and in the case of an evaporator implies temperature differences between two zones of the passenger compartment, although the same air flow temperature is requested.
In order to remedy a disadvantage of this kind, the document EP 2 392 886 proposes to accommodate a conduit provided with a plurality of orifices inside a header. The liquid phase refrigerant fluid is therefore sprayed through the orifices in the form of droplets over the whole of the length of the conduit. Although it enables improvement of the distribution of the fluid inside the header, an arrangement of this kind can generate high head losses, notably because of the small size of each of the orifices allowing the passage of fluid, which can lead to revising the whole of the refrigerant fluid circuit in order to feed the heat exchanger correctly.
In this context, the present invention consists in a device for distribution of a refrigerant fluid in a header of a heat exchanger comprising at least two conduits, including an external conduit and an internal conduit, with the internal conduit accommodated in the external conduit in such a manner as to form a volume for communication between the internal conduit and the external conduit, the external conduit comprising spraying orifices each having an axis intersecting a principal lengthwise axis of the external conduit, the internal conduit comprising at least one communication orifice having an axis intersecting a principal lengthwise axis of the internal conduit. According to the invention, the internal conduit comprises a portion of reduced thickness formed by removal of material from an external face of the internal conduit, the external face facing toward the external conduit.
The presence of a portion of reduced thickness of this kind enables an increase in the size of the communication volume between the internal conduit and the external conduit, which allows the refrigerant fluid passing through the communication orifice or orifices to be distributed better along the communication volume, whether in terms of fluid circulation or of mixing a liquid phase and a gas phase of the refrigerant fluid.
Clearly the so-called communication orifice or orifices is or are so called because they allow the refrigerant fluid to circulate from the interior of the internal conduit to the communication volume between the two conduits, prior to being evacuated via the spraying orifices.
According to one or more features that can be considered separately or in combination:
According to a series of features of the invention, the internal conduit may have a single communication orifice. The presence of a single orifice on the internal conduit enables introduction of the fluid into a single part of the external conduit, which enables better management of the feeding of the external conduit with refrigerant fluid. Moreover, the presence of a single orifice on the internal conduit enables reduction of the head losses relative to the situation where it would comprise a plurality of holes.
The axis of the single communication orifice may be substantially aligned with the middle of the spraying zone. It is therefore clear that the communication orifice discharges at substantially equal distances from the two spraying orifices at the greatest distances from the external conduit, that is to say at equal distances from the first spraying orifice and the last spraying orifice of the longitudinal series. The term substantially means that an uncertainty of plus or minus 5% is permitted to specify that the axis of the communication orifice is aligned with the middle of the spraying zone. It will be clear that the presence of a single orifice on the internal conduit enables introduction of the fluid into a particular zone of the external conduit, which enables better management of the feeding of the external conduit with refrigerant fluid. Moreover, the presence of a single orifice on the internal conduit facilitates modification of the dimension thereof and, as a function of that dimension, reduction of the head losses on passing through the internal conduit.
The single communication orifice may have a greatest dimension, measured in a section plane perpendicular to the axis of the single communication orifice, less than or equal to a greatest dimension of the internal conduit, measured in a section plane perpendicular to the principal lengthwise axis of the internal conduit. Such a dimension ensures good distribution of the fluid between the two conduits and limits the associated head loss.
According to one particular embodiment, the single communication orifice has a section of at least 4 millimetres diameter.
According to a series of features, considered separately or in combination with each other and with the foregoing features:
The invention also concerns a refrigerant fluid header for a heat exchanger comprising a distribution chamber. The distribution chamber accommodates a distribution device as defined above, and the internal conduit of the distribution device comprises an inlet opening for admission of the refrigerant fluid, the spraying orifices being arranged in such a manner as to allow circulation of the refrigerant fluid between the distribution device and the distribution chamber.
The distribution device may extend along a lengthwise axis of the header, with the internal conduit including at a first of its two longitudinal ends the inlet opening for the admission of the refrigerant fluid into the internal conduit, the internal conduit being closed at a second longitudinal end.
The invention further concerns a heat exchanger including at least one header as defined above, and tubes forming a bundle of tubes extending from the header, characterized in that the internal conduit of the distribution device is oriented in such a manner that the removal of material to form the portion of reduced thickness is effected in a zone of the internal conduit facing the bundle of tubes. For example, if the removal forms a flat, it is clear that the plane surface of the flat is perpendicular to the axes of the tubes of the bundle and that it is formed in the external face of the internal conduit closest to the bundle of tubes.
The spraying zone of the external conduit may have a length equal to a length of the bundle of tubes.
The portion of reduced thickness may be formed over a length of the internal conduit equal to a length of the bundle of tubes.
Other features, details and advantages of the invention will emerge more clearly on reading the detailed description given hereinafter by way of illustrative example with reference to the drawings of the appended sheets, in which:
It is first of all to be noted that although the figures show the invention in detail for its implementation, they can of course serve to define the invention better if necessary. Similarly, it is pointed out that, in all the figures, the same elements are designated by the same references.
In order to connect the various elements constituting the circuit 100, the latter comprises channels and valves to control the flow. It is to be noted that a minimalist circuit 100 of this kind is given as an example and is not restrictive on the scope of the invention given the various architectures that the circuit 100 can have.
The heat exchanger 500, in the form of an evaporator 600, is dedicated to cooling a flow of air A circulating in the air conditioning installation. A flow of air A of this kind is notably used to heat treat the air in the passenger compartment of the vehicle or for example to cool a unit of the vehicle in operation. According to another embodiment, the heat exchanger 500 is a cooler and is dedicated to cooling a liquid enabling cooling of a unit of the vehicle in operation, such as one or more batteries supplying electrical energy to an electrical drive train of the vehicle.
According to a variant embodiment not shown here, the heat exchanger 500 comprises a header 7 at one of the ends of the bundle of tubes and an outlet box 9 disposed at the other end of the bundle of tubes 6.
In the following description, an orientation is referred to as a function of the longitudinal axis L, vertical axis V and transverse axis T, as defined by the trihedron L, V, T represented in
Accordingly, in this frame of reference, the header 7 and the return box 8 are disposed at two opposite vertical ends of the bundle of tubes 6, with the header 7 disposed at a first vertical end and the return box at a second vertical end of the bundle of tubes 6. The outlet box 9 is disposed beside the header 7, along the transverse axis T, at the first vertical end of the bundle of tubes 6. The header 7 and the outlet box 9 are advantageously of unitary construction, that is to say they are made in one piece.
The header 7 delimits a distribution chamber 2 that is fed with refrigerant fluid 700 with the aid of a distribution device 10 accommodated in the header 7 and into which a plurality of tubes of the bundle of tubes 6 discharge.
The distribution device 10, which will be described in more detail later, includes an inlet opening 11 for admission of the refrigerant fluid 700 into the heat exchanger 500 and notably into the distribution device 10 that is configured to distribute the refrigerant fluid 700 along the header 7.
Once the refrigerant fluid 700 is inside the heat exchanger 500, it circulates along the tubes of the bundle of tubes 6 in such a manner as to cool them in one or more passes with the aid of the return box 8. The refrigerant fluid 700 is then evacuated from the heat exchanger 500 via an outlet opening 12 provided on the outlet box 9.
According to the arrangement of the heat exchanger 500 shown, the circulation of the refrigerant fluid 700 is in the shape of a āUā. According to a variant embodiment, the heat exchanger 500 is of the multiple pass type, that is to say the return box 8 is compartmented so that the refrigerant fluid 700 effects a plurality of passes through one layer of tubes before reaching the second layer and the outlet box. If the heat exchanger 500 does not include a return box 8 and comprises instead the outlet box 9, the circulation of the refrigerant fluid in the shape of an āIā.
Moreover, in the context of its application to an air conditioning installation, the heat exchanger 500 is intended to cool a flow of air A passing through the bundle of tubes 6 in a direction transverse to their lengthwise direction. In other words, the flow of air A passes through the bundle 6 transversely to a longitudinal plane P1 of the heat exchanger 500. To improve the exchange of heat, the tubes of the bundle 6 include, for example, fins encouraging the exchange of heat between the flow of air A and the tubes of the bundle 6.
The refrigerant fluid 700 circulates from the header 7 to a first layer of tubes of the bundle 6 dedicated to feeding the return box 8 with refrigerant fluid 700. The refrigerant fluid 700 then circulates from the return box 8 to the outlet box 9 through a second layer of tubes of the bundle 6. The first layer and the second layer are superposed one on the other on each side of the longitudinal plane P1.
The distribution chamber 2 of the header 7 accommodates the distribution device 10 extending along a lengthwise axis parallel to the direction in which the header 7 extends. The distribution device 10 comprises at least two conduits 12, 13, an internal conduit 13 configured to receive the refrigerant fluid via one of its longitudinal ends forming the inlet opening 11 and to transfer that fluid to an external conduit 12, which for its part is configured to enable the passage of refrigerant fluid toward each of the tubes of the bundle of tubes 6. To be more precise, the internal conduit 13 is accommodated in the external conduit 12. Each of the conduits 12, 13 of the distribution device 10 extends along a respective lengthwise axis 12A and 13A.
Each conduit 12, 13 of the distribution device 10 more particularly extends parallel to the lengthwise direction of the header 7, parallel to the longitudinal axis L. In other words, the lengthwise axis of each of the conduits 12, 13 is parallel to the lengthwise direction of the header 7. According to a variant embodiment, not shown here, at least one of the conduits 12, 13 of the distribution device 10 extends obliquely to the direction in which the header 7 extends.
According to the example shown, the conduits 12, 13 are coaxial, with the result that the lengthwise axes 12A, 13A coincide. In order to retain the conduits in this position, the two conduits 12, 13 are separated from one another with the aid of a spacer also enabling the fixing of the distribution device 10 to the header 7. Alternatively a distribution device 10 could be provided comprising more than two conduits 12, 13, it being understood that the additional conduits would be disposed between the internal conduit 13 and the external conduit 12.
The external conduit 12 and the internal conduit 13 are hollow and each of them delimits an internal volume. There are then defined an internal volume 15 extending in the internal conduit 13 and into which the refrigerant fluid 700 is admitted from the inlet opening 11 and a communication volume 14 extending in the external conduit 12 and to be more precise between the internal conduit 13 and the external conduit 12.
According to the example shown, the external conduit 12 and the internal conduit 13 both have an end of circular section, the section of the conduit being taken in a plane transverse to the principal lengthwise axis 12A, 13A of the conduit 12, 13. Accordingly, the communication volume 14 and the internal volume 15 are each delimited by at least one of the conduits 12, 13 of which at least a part of the walls is rounded. Of course, other section shapes of the conduits 12, 13 are allowed and could for example be a square or rectangular shape.
A spraying zone Z is defined on the external conduit 12 in which all of the spraying orifices 120 are situated. The spraying orifices 120 are arranged in a longitudinal series comprising a first spraying orifice 120i and a last spraying orifice 120n+i, the first spraying orifice 120i and the last spraying orifice 120n+i being disposed at opposite longitudinal ends of the series. It is then clear that the first spraying orifice 120i and the last spraying orifice 120n+i are the spraying orifices 120 at the greatest distance from one another in the series. The first spraying orifice 120i and the last spraying orifice 120n+i can also be defined as being the first and the last of the orifices to be reached by the refrigerant fluid 700 in the direction of circulation of that fluid along the internal conduit 13, as indicated by the arrow S.
The spraying zone Z extends over a length LZ, measured along the principal lengthwise axis 12A of the external conduit 12. The middle M of this length LZ enables definition of a central part C of the spraying zone Z, the central part covering an interval of plus or minus 5% of the length LZ around the middle M.
It is to be stated that according to the embodiment shown, the spraying orifices 120 are regularly spaced in the spraying zone Z of the external conduit 12. To be more precise, the spraying orifices 120 are disposed in a rectilinear manner along the principal lengthwise axis 12A of the external conduit 12, at regular intervals. In other words, the spraying orifices 120 are positioned in a straight line, the straight line being parallel to the principal lengthwise axis 12A of the external conduit 12, with a constant pitch between two successive spraying orifices. According to a variant embodiment, the spraying orifices 120 are arranged in the form of a helix around the principal lengthwise axis 12A of the external conduit 12.
Is it is to be noted that in the example shown the external conduit 12 comprises a single row of spraying orifices 120. According to a variant embodiment, the external conduit 12 comprises a plurality of parallel rows of spraying orifices 120. It is then clear that, in this variant not shown here, the spraying zone Z comprises two first spraying orifices 120i and two last spraying orifices 120n+i.
According to the invention, the internal conduit 13 comprises a portion 16 of reduced thickness, that is to say that at least a part of the internal conduit 13 has been subjected to a removal of material. This removal of material is effected on the external face of the internal conduit 13, that is to say on the face of the internal conduit 13 on the communication volume 14 side. This portion 16 of reduced thickness enables the communication volume 14 to be increased compared to an internal conduit 13 comprising no portion 16 of reduced thickness. The increased communication volume 14 enables improvement of the homogenization of the liquid phase and the gas phase of the refrigerant fluid 700 when that fluid, having left the internal conduit 13, circulates along the external conduit 12 before reaching the spraying orifices 120, as described later.
The portion 16 of reduced thickness of the internal conduit 13 is for example formed by machining the tube forming the internal conduit. According to the example illustrated, the portion 16 of reduced thickness takes the form of a flat 17. By flat is meant a plane surface formed on a circular section. It is to be noted that the flat 17 extends in the example shown over at least 50% of a length of the internal conduit 13. The flat 17 preferably extends in a rectilinear manner and parallel to the principal lengthwise axis 13A of the internal conduit 13. Moreover, the communication orifice 130 is formed in such a manner as to pass through the flat 17. In other words, the flat 17 extends over at least a part of the internal conduit 13 in which the communication orifice 130 is formed.
The presence of a single communication orifice 130 on the internal conduit 13, that is to say a single orifice enabling the passage from the internal conduit to the external conduit, enables the refrigerant fluid 700 to access a precise point on the external conduit 12, which enables total control of the distribution of this refrigerant fluid along the external conduit, notably preventing the fluid circulating from one longitudinal end to the other. The single communication orifice moreover enables modification of its dimension, and notably making it large enough to minimize head losses. It is clear that these two points make it possible to facilitate the development of the distribution device 10 in its application to a heat exchanger 500 regardless of the dimension of the heat exchanger 500 on which the distribution device 10 is mounted.
Whatever the dimension of the heat exchanger 500 and therefore of the internal conduit 13, the communication orifice 130 is positioned in such a manner as to open onto the central part C of the external conduit 12, that is to say a part situated at equal distances from the first spraying orifice 120i and the last spraying orifice 120n+i. As stated above, the spraying zone Z comprises a central part C extending from the middle M to plus or minus 5% of the length LZ of this spraying zone, the middle M being situated at equal distances from the first spraying orifice 120i and the last spraying orifice 120n+i. Accordingly, the refrigerant fluid 700 circulating in the internal conduit 13 is sure to discharge substantially at the middle of the spraying zone Z, which enables homogeneous feeding of the spraying orifices 120 of the external conduit 12, the term substantially signifying that the communication orifice 130 discharges at the middle M, or at least in the central part C bracketing that middle M in the proportions previously referred to.
According to a variant embodiment shown in
According to these embodiments, the communication orifices 130 have a contour of circular or oblong shape. Of course, other orifice shapes are possible, such as a communication orifice having a contour of polygonal, for example decagonal shape. In all cases of these shapes, it is to be noted that the communication orifice 130 has a greater dimension, such as diameter or a diagonal, measured in a section plane perpendicular to its axis 130A, that is less than or equal to a section of the internal conduit 13. By section of the internal conduit 13 is meant the greatest internal dimension of the internal conduit 13 measured in a section plane perpendicular to the principal lengthwise axis 13A of the internal conduit 13, such as a diameter or a diagonal.
In the example shown, the internal conduit 13 has an outer diameter of 6 millimetres and an inside diameter of 4 millimetres, and the communication orifice 130 has a diameter, or a greatest dimension, equal to 4 millimetres. The fact the communication orifice 130 has a diameter substantially equal to the diameter of the internal conduit 13 enables control of the head losses on passage of the fluid between the inlet opening, consisting in a single orifice of given diameter arranged at one end of the device, and the external conduit, along which the refrigerant fluid 700 comes to be distributed to pass in a homogeneous fashion through each of the spraying orifices 120. In the case of a single communication orifice, its central position enables homogeneous feeding in that the refrigerant fluid 700 penetrating into the external conduit 12 is equally distributed to one or the other of the longitudinal ends of the distribution device.
It should be noted from the foregoing description that in the case of a single communication orifice, the optimum position of that communication orifice 130 is theoretical and such that it is located strictly in vertical alignment with the middle M of the spraying zone Z. However, it may be wished to offset the longitudinal position of this communication orifice, advantageously in corresponding relationship with the central portion C around this middle M, if a pressure imbalance is noted between the inlet and the outlet for the refrigerant fluid in the heat exchanger.
For example, if the refrigerant fluid circuit 100 of the air conditioning installation is configured so that the pressure of the refrigerant fluid at the inlet is higher than the pressure at the outlet, it is then appropriate to move the communication orifice toward the end corresponding to the inlet opening/opposite the inlet opening?
Question for Valeo: Please check which proposition is correct, and if possible explain the technical reason in a few words.
Moreover,
This vertical overlapping is accompanied in the example shown by a particular arrangement of the flat 17, and of the communication orifice 130, the internal conduit 13 and the spraying orifices 120 of the external conduit 12. The internal conduit 13 is therefore disposed in the external conduit 12 in such a manner that the portion 16 of reduced thickness faces toward a portion of the external conduit 12 with no spraying orifices 120. In
To encourage this separation of phases by gravity, each communication orifice 130 advantageously has an axis 130A parallel to the direction of terrestrial gravity and the flat 17 has a plane surface extending perpendicularly to the direction of terrestrial gravity.
In order for the volume in which the liquid phase accumulates to be as large as possible, the spraying orifices 120 have axes 120A perpendicular to the plane face formed by the removal of material. In other words, the spraying orifices 120 have axes 120A perpendicular to the plane of the flat 17.
Each communication orifice 130 advantageously opens onto a portion of the external conduit 12 with no spraying orifices 120. Accordingly, the communication orifices 130 are disposed facing a solid part of the external conduit 12. By solid part is meant a part of the external conduit 12 with no spraying orifices 120. Accordingly, the communication orifices 130 are not disposed facing the spraying zone Z.
The communication orifices 130 are preferably arranged in such a manner that the refrigerant fluid 700 passing through them circulates in the opposite direction to the direction of circulation of the refrigerant fluid 700 passing through the spraying orifices 120. In other words, each communication orifice 130 has an axis 130A parallel to the axes 120A of the spraying orifices 120, whilst opening in the opposite direction. When the conduits 12, 13 are coaxial and circular, it can be said that each communication orifice 130 is situated facing a part of the external conduit 12 that is diametrically opposite the spraying orifices 120. When the conduits have a shape other than circular, it can be said that each communication orifice 130 is situated facing a part of the external conduit 12 that is symmetrically opposite the spraying orifices 120. A position of this kind of the communication orifice 130 relative to the spraying orifices 120 enables the gas phase to be forced to drive the liquid phase in the direction of the spraying orifices 120.
To be more precise, with the presence of the flat 17 on the internal conduit 13, there are distinguished a smallest radial distance W1 and a largest radial distance W2, it being understood that the radial distances are measured in a given section, perpendicular to the principal lengthwise axis 13A of the internal conduit 13, on a straight line segment passing through the common centre of the internal conduit and the external conduit. The smallest radial distance W1 correspond to the distance between the external face of the internal conduit 13 in a portion different from the flat 17 and the internal face of the external conduit 12. Conversely, the greatest radial distance W2 corresponds to the distance between the centre of the flat 17 and the internal face of the external conduit 12.
Depending on the dimensions of the distribution device 10, the shortest distance W1 can reach a maximum value of 0.25 millimetre to 2 millimetres, while the greatest distance W2 can reach a maximum value of 1 to 5 millimetres. Of course, the greatest distance W2 is always greater than the smallest distance W1. Accordingly, it is clear that from one distribution device 10 to another, the communication volume 14 can be larger or smaller as a function of these distances W1, W2.
Note that the external conduit 12 is arranged in the header 7 in such a manner that the spraying orifices 120 discharge opposite the zone of the external conduit into which open the tubes of the bundle of tubes 6. In an arrangement as shown in
The spraying orifices 120 are preferably arranged so that the refrigerant fluid 700 circulates in an opposite direction relative to the direction of circulation of the refrigerant fluid 700 flowing along the bundle of tubes 6. In other words, each spraying orifice 120 has an axis 120A parallel to the axes 6A of the tubes, whilst discharging opposite those tubes, the header participating in guiding the fluid in the tube on leaving the spraying orifice. When the external conduit 12 is circular, it can be said that the spraying orifices 120 are situated facing a part of the header 7 that is diametrically opposite the bundle of tubes 6. This kind of position of the spraying orifices 120 relative to the bundle of tubes 6 enables improvement of the evaporation of the refrigerant fluid 700 before it flows along the tubes.
It is to be noted that the spraying orifices 120 are all distributed along the bundle of tubes 6. In other words, the spraying zone Z has a length LZ equal to the length of the bundle of tubes 6, the length of the bundle of tubes 6 being measured along the longitudinal axis L, parallel to the principal lengthwise axis 12A of the external conduit 12. Accordingly, it can equally be stated that the flat 17 has a length L17 equal to the length of the bundle of tubes 6. It can also be said that when the internal conduit 13 comprises a single communication orifice 130, the latter is aligned with the middle of the bundle of tubes 6.
Whatever the variant embodiment retained, the invention enables provision of a device for distribution of the refrigerant fluid offering low head losses for a homogeneous distribution of the refrigerant fluid in a header of a heat exchanger. Providing a single communication orifice in the distribution device enables an efficient heat exchanger to be obtained in which the fluid distribution device addresses these two criteria.
The invention should nevertheless not be deemed to be limited to the means and configurations described and shown, and applies equally to any means, or any configurations, that are equivalent and to all combinations of such means and/or configurations. In fact, although the invention has been described and shown in different variant embodiments each separately employing a particular arrangement, it goes without saying that these arrangements described can be combined without this compromising the invention.
Number | Date | Country | Kind |
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1762509 | Dec 2017 | FR | national |
Filing Document | Filing Date | Country | Kind |
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PCT/EP2018/085522 | 12/18/2018 | WO |
Publishing Document | Publishing Date | Country | Kind |
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WO2019/121699 | 6/27/2019 | WO | A |
Number | Name | Date | Kind |
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20130020061 | Bergh | Jan 2013 | A1 |
20170219298 | Tsutsui | Aug 2017 | A1 |
20180156512 | Mislak | Jun 2018 | A1 |
Number | Date | Country |
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2392886 | Dec 2011 | EP |
2784428 | Oct 2014 | EP |
2009002256 | Dec 2008 | WO |
WO-2009002256 | Dec 2008 | WO |
Entry |
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International Search Report and Written Opinion in corresponding International Application No. PCT/EP2018/085522, dated Mar. 29, 2019 (7 pages). |
Number | Date | Country | |
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20210088295 A1 | Mar 2021 | US |