The present application claims priority from European Patent Application No. EP 21305239.2, filed on Feb. 26, 2021, the entirety of which is incorporated by reference herein.
The present technology relates to heat exchanger systems, such as dry coolers, using mesh panels for adiabatic cooling.
Dry coolers and similar heat exchanger systems reject thermal energy from a heat transfer fluid (e.g., water) circulating therethrough to the atmosphere. For example, in a data center, a dry cooler can be used to cool heated water extracted from within the data center (e.g., water circulated through water blocks to collect heat from heat-generating components). In order to improve the efficiency of dry coolers, in some cases, adiabatic cooling can be implemented in order to lower the temperature of (i.e., pre-cool) ambient air that flows through the dry cooler. For example, in some cases, a water spraying system (i.e., an atomizer) is placed at the air inlet of the dry cooler to spray water and thereby increase humidity of the ambient air and thereby reduce its temperature. Other adiabatic cooling solutions are also available, including for instance evaporative cooling pads, or mesh panels on which water is applied and through which ambient air flows prior to entering the dry cooler.
However, these solutions may also have various disadvantages. For instance, spraying water under high pressure which advantageously promotes water evaporation (due to the small size droplets released) can require a complex and expensive pumping system. Moreover, in some cases, high pressure water spraying can be hazardous since, if the water is contaminated, it may promote dispersion of pathogenic bacteria such as Legionella. As a result, this practice is forbidden in some countries. Conversely, spraying water under low pressure (e.g., below 5 bars) does not require a complex pumping system, but it can be wasteful in terms of its usage of water and not very efficient as evaporation of the sprayed water is not achieved as easily. For their part, evaporative cooling pads can obstruct flow of ambient air therethrough which can result in greater power consumption and noise emission by the dry cooler. Mesh panels, which allow using low pressure water spraying, improve homogenization of the evaporation of water but can still be wasteful in water usage and limited in terms of the ratio of water evaporation achieved.
There is therefore a desire for a heat exchanger system which can alleviate at least some of these drawbacks.
It is an object of the present technology to ameliorate at least some of the inconveniences present in the prior art.
According to one aspect of the present technology, there is provided a mesh panel for a heat exchanger system, the mesh panel comprising: a mesh body extending from an upper end to a lower end, the mesh body having an inlet side and an outlet side opposite the inlet side, the mesh body comprising a plurality of mesh wires arranged to form a mesh pattern defining a plurality of mesh openings between the mesh wires, the mesh body comprising: at least one penetrating mesh portion extending at least partly along a depth direction of the mesh body, the depth direction being normal to a plane extending between the upper and lower ends of the mesh body, the at least one penetrating mesh portion at least partly defining an air flow opening, the air flow opening having greater dimensions than each of the mesh openings.
In some embodiments, the at least one penetrating mesh portion comprises: an inlet end; an outlet end distanced from the inlet end along the depth direction, the outlet end defining the air flow opening; and a peripheral side wall extending between the inlet end and the outlet end.
In some embodiments, the peripheral side wall of the at least one penetrating mesh portion converges toward the outlet end.
In some embodiments, the at least one penetrating mesh portion has a generally truncated conical shape.
In some embodiments, the air flow opening defined by each of the at least one penetrating mesh portion is circular.
In some embodiments, the air flow opening defined by each of the at least one penetrating mesh portion is polygonal.
In some embodiments, the at least one penetrating mesh portion defines a first perimeter at the inlet end and a second perimeter at the outlet end; and the first perimeter is greater than the second perimeter.
In some embodiments, the at least one penetrating mesh portion comprises a plurality of penetrating mesh portions; and at least some of the penetrating mesh portions are spaced apart from one another along a height direction of the mesh body, the height direction being normal to the depth direction.
In some embodiments, the at least one penetrating mesh portion deflects air flowing through the air flow opening to cause turbulence thereof.
In some embodiments, the mesh body comprises a plurality of mesh layers stacked with one another in the depth direction to form the mesh body; and the air flow opening defined at least in part by the at least one penetrating mesh portion is defined in part by each of the mesh layers.
In some embodiments, the mesh body has a first angled portion extending from the upper end and a second angled portion extending from the lower end to the first angled portion, the first and second angled portions being angled relative to one another; each of the at least one penetrating mesh portion is formed in one of the first angled portion and the second angled portion.
In some embodiments, the mesh body has an undulating configuration such that the mesh body forms a plurality of undulations offset from another in a height direction of the mesh body, the height direction being normal to the depth direction.
According to another aspect of the present technology, there is provided a heat exchanger system comprising: a frame; at least one heat exchanger panel connected to the frame and configured to exchange heat with air flowing therethrough, the at least one heat exchanger panel having an inlet side and an outlet side, the at least one heat exchanger panel comprising: a cooling coil for circulating fluid therein; and a plurality of fins in thermal contact with the cooling coil, the fins being spaced from one another for air to flow therebetween and into an interior space of the heat exchanger system; a fan assembly connected to the frame and comprising at least one fan, the at least one fan being rotatable about a fan rotation axis to pull air into the interior space through the at least one heat exchanger panel and evacuate heated air from the interior space through the fan assembly; the mesh panel of any one of claims 1 to 9, the mesh panel being disposed on the inlet side of the at least one heat exchanger panel such that rotation of the at least one fan causes ambient air to flow subsequently through the mesh panel, through the heat exchanger panel and into the interior space; and a water distribution system operable to spray water on the mesh panel to pre-cool ambient air flowing through the mesh panel.
In some embodiments, the water distribution system comprises a conduit disposed between the at least one heat exchanger panel and the mesh panel, the water distribution system being operable to spray water from the conduit onto the mesh panel.
In some embodiments, the heat exchanger system is a dry cooler.
Embodiments of the present technology each have at least one of the above-mentioned object and/or aspects, but do not necessarily have all of them. It should be understood that some aspects of the present technology that have resulted from attempting to attain the above-mentioned object may not satisfy this object and/or may satisfy other objects not specifically recited herein.
Additional and/or alternative features, aspects and advantages of embodiments of the present technology will become apparent from the following description, the accompanying drawings and the appended claims.
For a better understanding of the present technology, as well as other aspects and further features thereof, reference is made to the following description which is to be used in conjunction with the accompanying drawings, where:
The drawings are not to scale unless otherwise specified.
As shown in
The dry cooler 10 comprises two heat exchanger panels 130 connected to the frame 14 and configured to exchange heat with air flowing therethrough. In particular, the heat exchanger panels 130 are liquid-to-air heat exchanger panels 130 that transfer heat from the fluid (e.g., water) circulating therein to the air flowing therethrough. As shown in
In this embodiment, the heat exchanger panels 130 are in an inclined position defining a V-shaped configuration of the heat exchanger panels 130. Notably, an axis of each heat exchanger panel 130, extending from the upper end to the lower end of the heat exchanger panel 130, is angled relative to a vertical axis. The heat exchanger panels 130 could be oriented differently in other embodiments. For instance, the heat exchanger panels 130 may be disposed to extend vertically and thereby have an I-shaped configuration.
As shown in
The dry cooler 10 comprises a fan assembly 140 connected to the frame 14 and configured to cause air flow through the dry cooler 10. In particular, the fan assembly 140 comprises a plurality of fans 142 (one of which is shown in
The dry cooler 10 thus functions by pumping heated water (e.g., extracted from a data center in this example) through the cooling coils 60 of the heat exchange panels 130, while simultaneously pulling ambient air between the fins 33 of the heat exchange panels 130. The ambient air absorbs heat from the heated water circulating through the cooling coils 60. As ambient air is pulled in through the heat exchange panels 130 into the interior space 12 of the dry cooler 10, thermal energy is transferred from the water circulating in the heat exchanger panels 130 to the ambient air. The now-heated air is then discharged from the interior space 12 of the dry cooler 10 through the fan assembly 140. The water circulating in the heat exchanger panels 130 is thus cooled and is recirculated back into the data center.
While in this embodiment the heat transfer fluid is water, in other embodiments, the heat transfer fluid may be a dielectric fluid, a refrigerant fluid, a phase change material (PCM) or any other fluid suitable for collecting and discharging thermal energy.
It will be appreciated that the configuration of the dry cooler 10 as described above is provided merely as an example to aid in understanding the present technology. The dry cooler 10 may be configured differently in other embodiments. For instance, in other embodiments, a single heat exchanger panel 130 may be provided, and the fan assembly 140 may include a single fan 142. Moreover, the fans 142 may be oriented such that their respective fan rotation axes FA extend horizontally, or at angle between horizontal and vertical.
The adiabatic cooling system of the dry cooler 10 will now be described in greater detail. In this embodiment, as shown in
The water distribution system 110 is configured to spray water in a surrounding environment of the dry cooler 10, notably, in this embodiment, onto the mesh panels 150 such that ambient air flows through the sprayed water retained by the mesh panels 150. In this embodiment, the water distribution system 110 includes, for each heat exchanger panel 130, a conduit 111 for circulating water therein and a plurality of nozzles 112 for spraying water droplets from the conduit 111 onto the corresponding mesh panel 150. In this embodiment, the water distribution system 110 also includes a pump (not shown) for pumping water through the water distribution system 110. In other embodiments, the pump may be omitted (e.g., the water distribution system may be connected to municipal makeup water operating on low pressure—e.g., 3-4 bars). As can be seen in
In this embodiment, the water distribution system 110 operates on low pressure. In the present disclosure, a system operating on low pressure is defined as operating at a pressure below 5 bars. In this embodiment, the water distribution system 110 operates at a pressure of approximately 1.5 bars. Since the water distribution 110 operates on low pressure, the pump thereof is relatively inexpensive. Moreover, spraying water at low pressure reduces the likelihood of causing the dispersion of pathogenic organisms. As such, the water distribution system 110 is compliant with regulations in jurisdictions in which high pressure water spraying is not permitted.
While in some embodiments the water distribution system 110 may continuously spray water onto the mesh panels 150, this may be wasteful and therefore not preferable. Instead, in this embodiment, the water distribution system 110 includes an electronic controller (not shown) which is in communication with the pump of the water distribution system 110 and with one or more valves to control the spray of water from the nozzles 112. The controller may control the spraying of water by the nozzles 112 based on a set timer (e.g., every 5 minutes). In other embodiments, the controller of the water distribution system 110 may be in communication with sensors (not depicted) such as a temperature sensor and/or a humidity sensor, such that the water distribution system 110 is activated and sprays water droplets only under specific environmental parameters. More precisely, the water distribution system 110 may be configured to spray water droplets only when the temperature and/or the humidity in a vicinity of the dry cooler 10 are above or below specific respective thresholds. Other environmental parameters may be contemplated in alternative embodiments. Alternatively or additionally, the controller of the water distribution system 110 may be in communication with sensors (not depicted) configured to sense a temperature of the water in the water distribution system 110 (e.g. before being sprayed on the mesh panels 150), water received in the drain 170, heat transfer fluid flowing in the heat exchanger panels 130 (e.g. at the inlet 30 and/or the outlet 32) such that the water distribution system 110 is activated and sprays water droplets only under specific operational conditions
With reference to
In this embodiment, each of the mesh panels 150 has an identical configuration and therefore only one of the mesh panels 150 will be described in detail herein. It is to be understood that the same description applies to both mesh panels 150. With reference to
The mesh body 155 has an air inlet side 1500A and an air outlet side 1500B opposite the air inlet side 1500A. The mesh panel 150 is positioned such that in use, ambient air flows through the mesh body 155 from the air inlet side 1500A to the air outlet side 1500B. A thickness of the mesh body 155 is measured between the air inlet side 1500A and the air outlet side 1500B. As shown in
In this embodiment, the mesh wires 1505 are made of plastic material but other materials are also contemplated.
As shown in
In this embodiment, the penetrating mesh portions 1560 of the mesh body 155 are all configured identically and therefore only one of the penetrating mesh portions 1560 will be described in detail herein. It is to be understood that the same description applies to the other penetrating mesh portions 1560. As best shown in
With reference to
As best shown in
In this embodiment, the configuration of the penetrating mesh portions 1560 provides a relatively uniform air flow at the outlet side 1500B of the mesh body 155. Notably, as denoted by the air flow arrows in
Moreover, the penetrating mesh portions 1560 can cause turbulent air flow as air exits the air flow openings 1562. The turbulence generated by the penetrating mesh portions 1560 may be adjusted by calibration of the shape of the penetrating mesh portions 1560, namely calibrating a shape of the side wall 1561, and a size of the air flow opening 1562. The turbulent air flow caused by the air flow openings 1562 can force air to follow a path that lingers along the mesh panel 150 (e.g., air vortices formed around the side walls 1561) before flowing through the heat exchanger panel 130, thereby increasing a time during which the air collects water. In doing so, the penetrating mesh portions 1560 enhance a cooling of air flowing therethrough.
The penetrating mesh portions 1560 may be formed in various ways. In this embodiment, the penetrating mesh portions 1560 are made by cutting the air flow openings 1562 into a mesh body and then punching the peripheral side walls 1561 of the penetrating mesh portions 1560 into the mesh body 155 around the air flow openings 1562. The penetrating mesh portions 1560 may be made differently in other embodiments. For instance, the mesh body 155 comprising the penetrating mesh portions 1560 may be fabricated using known plastic molding techniques or 3D-printing techniques.
With reference to
The penetrating mesh portions 1560 may be configured differently in other embodiments. For instance, in some embodiments, rather than the penetrating mesh portions 1560 converging toward the outlet end 1567, in some embodiments, the peripheral side walls 1561 of the penetrating mesh portions 1560 may be cylindrical (i.e., same diameter at the inlet end 1565 and the outlet end 1567). Notably, in such embodiments, the extension of the side wall 1561 in the depth direction increases the surface contact between the incoming air flow and the water retained on the side wall 1561, thereby increasing evaporation of water to cool the ambient air flowing through the mesh panel 150.
In another alternative embodiment of the penetrating mesh portions 1560 depicted in
In some embodiments, one or more of the penetrating mesh portions 1560 may be a mirrored version of the penetrating mesh portion 1560 illustrated on
While the mesh panels 150 have been described above as being generally planar (as depicted in
For instance, with reference to
In other embodiments, with reference to
Furthermore, in the above-described embodiments, the mesh body 155 has a single mesh layer which defines the penetrating mesh portions 1560. However, with reference to
As will be understood from the above description, the mesh panels 150 according to the present technology improve the pre-cooling of air prior to its entry into the interior space 12 of the dry cooler 10. Notably, the penetrating mesh portions 1560 formed in the mesh panels 150 can increase surface contact between air flowing through the mesh panels 150 and water retained by the penetrating mesh portions. Moreover, the shape of the penetrating mesh portions can improve the evaporation ratio of water sprayed onto the mesh panels 150. Therefore, the mesh panels 150 provide a cost-efficient manner to improve the adiabatic cooling of ambient air for heat exchanger systems such as dry coolers.
Modifications and improvements to the above-described embodiments of the present technology may become apparent to those skilled in the art. The foregoing description is intended to be exemplary rather than limiting. The scope of the present technology is therefore intended to be limited solely by the scope of the appended claims.
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21305239 | Feb 2021 | EP | regional |
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Number | Date | Country | |
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20220279680 A1 | Sep 2022 | US |