Microfluidic fan
11078894 · 2021-08-03
Assignee
Inventors
Cpc classification
F04B19/006
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F04B39/06
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F21V29/63
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F04B19/00
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
International classification
F04B37/10
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F04B19/00
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
H05K7/20
ELECTRICITY
F04B39/06
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
Abstract
A device (1, 100) for controlling a flow of a gaseous fluid is disclosed. The device comprises a first electrode (10, 110) and a second electrode (20, 120) offset from the first electrode in a downstream direction of the flow. The electrodes are connectable to a voltage source. A thermally conducting flange (30) is arranged to extend in a plane parallel to a direction of the flow and adapted to dissipate heat from the gaseous fluid. At least a portion of the first electrode has a maximum height (h.sub.1) in a direction parallel to a direction of the flow and a maximum width (w.sub.1) in a direction orthogonal to the direction of the flow, wherein said maximum height is larger than said maximum width so as to improve the pumping efficiency of the device. A method for manufacturing the device, and a method for controlling a fluid flow by means of such device, is also disclosed.
Claims
1. A device for controlling a flow of a gaseous fluid, the device comprising: a first electrode, wherein at least a portion of the first electrode has a maximum height in a direction parallel to a direction of the flow and a maximum width in a direction orthogonal to the direction of the flow, wherein said maximum height is larger than said maximum width; a second electrode, wherein at least a portion of the second electrode is offset from at least a portion of the first electrode in a downstream direction of the flow, the first and second electrodes being connectable to a voltage source; and a plurality of thermally conducting flanges extending in a first plane oriented along a direction of the flow, and arranged around at least a portion of the first electrode, whereby the thermally conducting flanges define a volume receiving at least a portion of the first electrode, and the plurality of thermally conducting flanges being adapted to dissipate heat from the gaseous fluid.
2. The device according to claim 1, wherein the first electrode comprises bridges and joints forming a grid structure arranged to allow the gaseous fluid to pass through the first electrode, and wherein said portion of the first electrode forms part of at least one of the bridges.
3. The device according to claim 1, wherein the first electrode is formed as a rod having a height corresponding to the maximum height and a width corresponding to the maximum width.
4. The device according to claim 1, wherein the first electrode is formed as a rod having a circular or polygonal cross section in a plane intersecting the direction of the flow.
5. The device according to claim 3, wherein the rod comprises at least one pointed tip pointing in the direction of the flow.
6. The device according to claim 1, wherein the device comprises a plurality of mutually intersecting thermally conducting flanges.
7. The device according to claim 1, wherein the second electrode is electrically connected to the plurality of thermally conducting flanges.
8. The device according to claim 1, wherein the second electrode is integrally formed with the plurality of thermally conducting flanges.
9. The device according to claim 1, wherein a distance between the second electrode and the first electrode in the direction of the flow is between 0.4-2.0 mm.
10. A method for manufacturing a device for controlling a flow of a gaseous fluid, the method comprising: providing a first electrode, the first electrode comprising at least a portion having a maximum height in a direction parallel to the direction of the flow and a maximum width in a direction orthogonal to the direction of the flow, and wherein said maximum height is larger than said maximum width; providing a second electrode, the second electrode comprising a portion which is formed as a thermally conducting flange extending in a plane parallel to a direction of the flow and being adapted to dissipate heat from the gaseous fluid; providing, on at least one of the first electrode or the second electrode, a suspension structure, wherein the suspension structure is arranged in a plane orthogonal to the direction of the flow for absorbing thermally induced deformations in the first electrode or the second electrode; and arranging the second electrode offset from the first electrode in the direction of the flow.
11. The method according to claim 10, wherein first and/or second electrode(s) is/are provided by selectively depositing a metal.
12. The method according to claim 10, wherein first and/or second electrode(s) is/are provided by selectively removing material from a metal substrate.
13. A method for controlling a flow of a gaseous fluid, the method comprising: providing a first electrode of a device, the first electrode comprising at least a portion having a maximum height in a direction parallel to the direction of the flow and a maximum width in a direction orthogonal to the direction of the flow, and wherein said maximum height is larger than said maximum width; providing a second electrode of the device, the second electrode comprising a portion which is offset from at least a portion of the first electrode in a downstream direction of the flow and being adapted to dissipate heat from the gaseous fluid; providing a plurality of thermally conducting flanges extending in a first plane oriented along a direction of the flow, arranged around at least a portion of the first electrode, whereby the thermally conducting flanges define a volume receiving at least a portion of the first electrode, and the plurality of thermally conducting flanges being adapted to dissipate heat from the gaseous fluid; arranging the second electrode offset from the first electrode in the direction of the flow; providing the gaseous fluid that contacts the first electrode of the device; and applying an electric potential difference between the first electrode and the second electrode.
14. The method according to claim 13, further comprising the step of varying the electric potential difference as a function of time.
15. The method according to claim 13, wherein the applied electric potential difference is comprised in the range of 400-4000 V.
16. The method according to claim 13, wherein the applied electric potential difference is comprised in the range of 100-400 V.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
(1) The above, as well as additional objects, features and advantages of the present invention, will be better understood through the following illustrative and non-limiting detailed description of embodiments of the present invention. Reference will be made to the appended drawings, on which:
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(9) All the figures are schematic, generally not to scale, and generally only show parts which are necessary in order to elucidate the invention, whereas other parts may be omitted or merely suggested.
DETAILED DESCRIPTION OF EMBODIMENTS
(10)
(11) The emitter may be formed as a rod 10 having a vertical extension, or maximum height h1, in the direction of the flow and a lateral extension, or maximum width w1, in a direction perpendicular to, or at least intersecting, the direction of the flow. As shown in the present figure, the maximum height h1 is larger than the maximum width w2, hence providing the rod 10 with an elongated shape in the direction of the flow. The rod 10 may also be provided with one or several pointed tips 16 pointing in the direction of the flow, thereby increasing the number of possible emitting points of the emitter.
(12) During operation, the emitter 10 and the collector 20 may be connected to a voltage source (not shown) so as to induce an electric field between the emitter 10 and the collector 20 at least in a direction of the intended flow direction, thereby inducing a motion of the gaseous fluid along said direction. As the fluid passes through the device 1, heat energy carried by the fluid may, upon thermal contact with the flange 30, be transferred to the flange 30 and eventually dissipated to the surroundings of the device 1.
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(17) The emitter 10 and the collector 20 may be attached to a heat transferring element 50 which may be arranged to transfer or dissipate heat from at least one of the emitter 10 and the collector 20. As shown in
(18) According to some embodiments, the device may comprise a suspension structure adapted to absorb, or prevent, thermally induced deformations of the first electrode and/or the second electrode. The suspension structure, which also may be referred to as a deformation structure, may e.g. be adapted to apply a tensile stress to a length direction of any one of the electrodes, at least a portion of the electrode(s), or a structure formed by the electrode(s).
(19) As the material of the grid may expand with an increasing temperature, the bridges 111 of the deformation structure 126 may be compressed by compressive forces acting in the length direction of the bridges 111. By length direction should be understood the direction of extension between a first joint and a second joint. Thereby the lateral expansion of the grid may be absorbed by the deformation structure 115 and thermally induced stresses reduced so that the emitter 110 other than the deformation structure 115 may keep its original shape despite thermal expansion. It should however be understood that the forces acting on the bridges 111 of the deformation structure 115 also, or alternatively, may be caused by e.g. a torsional moment, or torque, acting on the structure.
(20)
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(22) The grid spacer 130 may e.g. be formed as a grid supporting the emitter 110 and the collector 120. As illustrated in
(23) The spacing d of the emitter and collector may be determined by the height of the bridges of the grid spacer 130, which may hence determine the magnitude of the electric field induced between the emitter 110 and the collector 120. The distanced between the emitter 110 and the collector 120 may e.g. be within the range of 0.4 mm and 2 mm.
(24) Further, the grid spacer 130 may comprise an alignment structure for facilitating alignment of the emitter 110 and the collector 120, and/or alignment of the devices 100 of the stack.
(25) The fan assembly 200 may also comprise a stacked structure with stage spacers 140 arranged to maintain a distance between the emitter 110 of a first device and the collector 120 of a second device. The stacking structure 140 may also comprise an alignment structure 142 (not shown in
(26) The grid spacer 130 and/or the stacking structure 140 may e.g. comprise a ceramic material, such as Al.sub.2O.sub.3 or Macor™, a plastic material or any suitable electrically insulating material.
(27) As shown in
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(29) To further improve relaxation, a pulse-reverse current may be introduced between the pulses described with reference to
(30) The applied electrical potential difference may e.g. depend on the mode of operation of the device. In case of e.g. an injection type mode, the applied electrical potential difference may be comprised in the range of 250-5000 V, depending on the actual distance between the emitter and the collector. In case of e.g. a conduction type mode, the applied potential difference may, for the same actual distance between emitter and the collector, be in the range of 10-500 V.
(31) The injection type mode, or ion drag mode, may be understood as an operational mode of the device wherein a relatively high electric field at the emitter causes electrons to be injected into the gaseous fluid at the interface of the emitter and the gaseous fluid, thus creating a corona of free ions in the gaseous fluid. The conduction mode, on the other hand, can be understood as a mode wherein the electric field is too low to create a substantial corona. Instead, the gaseous flow is caused by impurities or particles in the gaseous fluid, entraining a flow of the fluid.
(32) In one example, the external voltage supply may be controlled in a manner reducing formation of ozone. This may e.g. be achieved by limiting a maximum electric potential difference or electrical charge, and thereby reducing the risk for electrical break-through or sparks. Additionally, or alternatively, a housing, the collector and/or the flange may be adapted to decompose ozone, e.g. by means of a catalytic surface.
(33) As outlined above, the method for controlling the flow of a fluid as illustrated by