HYDROGEN STORAGE DEVICE
20220349527 · 2022-11-03
Inventors
- Luke SPERRIN (London, GB)
- Enass ABO HAMED (London, GB)
- Peter ITALIANO (London, GB)
- Kieran O'DONNELL (London, GB)
Cpc classification
F17C2203/03
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F17C2205/0142
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F17C11/005
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F17C2250/0439
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F17C2201/0109
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F17C2221/012
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F17C2227/0337
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F17C2227/0304
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F17C2250/043
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
Y02E60/32
GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
International classification
F17C11/00
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
Abstract
A hydrogen storage device (100A) comprises: a pressure vessel (230A), having a first fluid inlet (210A) and/or a first fluid outlet (220A), having therein a thermally conducting network (240A) optionally thermally coupled to a first heater and/or a first cooler; wherein the pressure vessel (230A) is arranged to receive therein a hydrogen storage material in thermal contact, at least in part, with the thermally conducting network (240A); wherein the thermally conducting network (240A) preferably has a lattice geometry, a gyroidal geometry and/or a fractal geometry in two and/or three dimensions, comprising a plurality of nodes, having thermally conducting arms therebetween, with voids between the arms; and wherein the thermally conducting network (240A) comprises fluidically interconnected passageways therein, for example within the arms and/or the nodes thereof, for flow therethough of a fluid.
Claims
1. A hydrogen storage device comprising: a pressure vessel, having a first fluid inlet and/or a first fluid outlet, having therein a thermally conducting network optionally thermally coupled to a first heater and/or a first cooler; wherein the pressure vessel is arranged to receive therein a hydrogen storage material in thermal contact, at least in part, with the thermally conducting network; wherein the thermally conducting network has a lattice geometry, a gyroidal geometry and/or a fractal geometry in two and/or three dimensions, comprising a plurality of nodes, having thermally conducting arms therebetween, with voids between the arms; and wherein the thermally conducting network comprises fluidically interconnected passageways therein for flow therethough of a fluid.
2. The hydrogen storage device according to claim 1, wherein the hydrogen storage device is arrangeable in: a first arrangement wherein the thermally conducting network is within the pressure vessel; and a second arrangement wherein the thermally conducting network is outside the pressure vessel.
3. The hydrogen storage device according to claim 1, wherein the hydrogen storage material comprises one or more selected from: a metal a hydride salt of a metal a borohydride salt of a metal borohydride salt of ammonium and/or alkyl ammonium; and mixtures thereof.
4. The hydrogen storage device according to claim 1, wherein the hydrogen storage material comprises and/or is an AB.sub.x alloy, wherein A is at least one selected from a group consisting of La, Ce, Pr, Nd, Ca, Y, Zr, and Mischmetal, wherein B is at least one selected from a group consisting of Ni, Co, Mn, Al, Cu, Fe, B, Sn, Si, Ti, and xis in a range from 4.5 to 5.5.
5. The hydrogen storage device according to claim 1, wherein the hydrogen storage material comprises and/or is an AB/A.sub.2B alloy, wherein A is at least one selected from a group consisting of Ti and Mg, and B is at least one selected from a group consisting of Ni, V, Cr, Zr, Mn, Co, Cu, and Fe.
6. The hydrogen storage device according to claim 1, wherein the hydrogen storage material comprises and/or is an AB.sub.2 alloy, wherein A is at least one selected from a group consisting of Ti, Zr, Hf, Th, Ce and rare earth metals, and B is at least one selected from a group consisting of Ni, Cr, Mn, V, Fe, Mn and Co.
7. The hydrogen storage device according to claim 1, wherein the hydrogen storage material comprises and/or is a metal hydride.
8. The hydrogen storage device according to claim 7, wherein the hydrogen storage material comprises one or more metal hydrides selected from a group consisting of: lithium hydride (LiH), sodium hydride (NaH), potassium hydride (KH), beryllium hydride (BeH.sub.2), magnesium hydride (MgH.sub.2), calcium hydride (CaH.sub.2), strontium hydride(SrH.sub.2), titanium hydride (TiH.sub.2), aluminum hydride (AlH.sub.3), boron hydride(BH.sub.3), lithium borohydride (LiBH.sub.4), sodium borohydride (NaBH.sub.4), magnesium borohydride (Mg(BH.sub.4).sub.2), calcium borohydride (Ca(BH.sub.4).sub.2), lithium alanate (LiAlH.sub.4), sodium alanate (NaAlH.sub.4), magnesium alanate (Mg(AlH.sub.4).sub.2), calcium alanate (Ca(AlH.sub.4).sub.2), and mixtures thereof.
9. The hydrogen storage device according to claim 7, wherein hydrogen storage material comprises and/or is one or more metal hydrides selected from MgH.sub.2, NaAlH.sub.4, LiAlH.sub.4, LiH, LaNi.sub.5H.sub.6, TiFeH.sub.2, palladium hydride PdH.sub.x, LiNH.sub.2, LiBH.sub.4 and NaBH.sub.4.
10. The hydrogen storage device according to claim 3, wherein the hydrogen storage material comprises an AB.sub.x alloy, an AB/A.sub.2B alloy, an AB.sub.2 alloy, a hydride and/or a mixture thereof.
11. The hydrogen storage device according to claim 1, wherein the hydrogen storage material comprises a dopant.
12. The hydrogen storage device according to claim 1, having a hydrogen storage density of at least 0.01 wt. % of the hydrogen storage vessel.
13. The hydrogen storage device according to claim 1, wherein the fractal geometry is selected from a group consistant of: Quadratic Koch Island, a Quadratic Koch surface, a Von Koch surface, a Koch Snowflake, a Sierpinski carpet, a Sierpinski tetrahedron, a Mandelbox, a Mandelbulb, a Dodecahedron fractal, a Icosahedron fractal, a Octahedron fractal, a Menger sponge, a Jerusalem cube, and a 3D H-fractal.
14. The hydrogen storage device according to claim 1, wherein an effective density of the lattice geometry is uniform in a first dimention and non-uniform in mutually orthogonal second and third dimensionsl.
15. The hydrogen storage device according to claim 1, wherein the lattice geometry is Bravais lattice a monoclinic; an orthorhombic; a tetragonal; a hexagonal; or a cubic lattic.
16. The hydrogen storage device according to claim 1, wherein the thermally conducting arms have a cross sectional dimension in a range from 0.1 mm to 10 mm and/or a length in range from 0.5 mm to 50 mm.
17. The hydrogen storage device according to claim 1, wherein the thermally conducting network is formed, at least in part, by additive manufacturing and/or by casting.
18. The hydrogen storage device according to claim 1, comprising a thermally-conducting foam.
19. The hydrogen storage device according to claim 1, wherein the thermally conducting network partially fills an internal volume of the pressure vessel, of at least 50% by volume of the pressure vessel, thereby defining an unfilled volume.
20. The hydrogen storage device according to claim 1, wherein the first heater comprises a Joule heater and/or a recirculating heater. cm 21-26. (canceled)
Description
BRIEF DESCRIPTION OF THE DRAWINGS
[0077] For a better understanding of the invention, and to show how exemplary embodiments of the same may be brought into effect, reference will be made, by way of example only, to the accompanying diagrammatic Figures, in which:
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DETAILED DESCRIPTION OF THE DRAWINGS
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[0111] In this example, the first hydrogen storage device 100A comprises a passageway 250A, wherein the first hydrogen storage device 200A is arrangeable in: a first configuration to receive a Joule heater in the passageway 250A; and a second configuration to receive a flow of a liquid through the passageway 250A. In the first configuration, a cartridge heater (not shown) is insertable into the passageway 250A through an end thereof and the opposed end of the passageway 250A is closed, with an insulating plug 260A. In the second configuration, the cartridge heater and the plug 260A are removed and fluid couplings 270A, 280A instead fitted to the ends, such that a recirculating liquid, such as coolant from a fuel cell, may be pumped therethrough.
[0112] In this example, the hydrogen storage device 100A is arranged to be oriented horizontally, in use. In this example, the pressure vessel 230A is generally cylindrical, having dished ends. In this example, the passageway, provided by a tube having a circular cross-section, extends between the dished ends longitudinally, offset from an axis of the pressure vessel 230A. In this example, the thermally conducting network 240A partially fills an internal volume of the pressure vessel 230A, particularly a region of the internal volume extending across about 75% of a diameter the pressure vessel, thereby completely surrounding the tube, such that an unfilled volume UV above the thermally conducting network 240A is defined. In this example, the thermally conducting network 240A is thermally coupled to at least a part of an internal surface of the pressure vessel 230A and an external surface of the tube. In this example, the unfilled volume UV acts as a buffer, providing a reservoir of hydrogen during charging and similarly during release, for example to account for kinetics thereof.
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[0116] In this example, the hydrogen storage device 200 comprises: a pressure vessel 1, having a first fluid inlet 8 and/or a first fluid outlet 9, having therein a thermally conducting network 4 optionally thermally coupled to a first heater and/or a first cooler; wherein the pressure vessel 1 is arranged to receive therein a hydrogen storage material in thermal contact, at least in part, with the thermally conducting network 4; wherein the thermally conducting network 340 has a fractal geometry in two dimensions, comprising a plurality of nodes, having thermally conducting arms therebetween, with voids between the arms; and wherein the thermally conducting network 4 comprises fluidically interconnected passageways therein, within the arms and the nodes thereof, for flow therethough of a fluid.
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[0125] In this example, the hydrogen storage device 200″ comprises: a pressure vessel 201″, having a first fluid inlet 208″ and/or a first fluid outlet 209″, having therein a thermally conducting network 204″ optionally thermally coupled to a first heater and/or a first cooler;
[0126] wherein the pressure vessel 201″ is arranged to receive therein a hydrogen storage material in thermal contact, at least in part, with the thermally conducting network 204″; wherein the thermally conducting network 203″ has a fractal geometry in two dimensions, comprising a plurality of nodes, having thermally conducting arms therebetween, with voids between the arms; and wherein the thermally conducting network 204″ comprises fluidically interconnected passageways therein, within the arms and the nodes thereof, for flow therethough of a fluid.
[0127] In this example, the pressure vessel 201″ is generally cylindrical, having a generally dished first end and a necked second end opposed thereto, and having a single aperture providing both the first fluid inlet 208″ and the first fluid outlet 209″. In other words, the pressure vessel 201″ is bottle-shaped. An inner wall portion 2011″ of the pressure vessel 201″ provides an axial cylindrical, elongate blind passageway 210″, arranged to receive a first heater 206″ (not shown), that extends from the first end towards the second end and that is coaxial with an outer wall portion 2010″ of the pressure vessel 201″. A second blind passageway in the first end is arranged to receive a thermocouple (not shown).
[0128] In this example, the pressure vessel has an internal volume of about 500 cm.sup.3, thereby providing a hydrogen storage capacity of about 25 g Hz. In this example, .
[0129] In this example, the thermally conducting network 204″ has a lattice geometry in three dimensions. In this example, an effective density of the lattice geometry is uniform in a first dimension, particularly axially, and non-uniform in mutually orthogonal second and third dimensions, particularly radially. Particularly, the effective density decreases radially outwards, such that there is faster heat transfer proximal the passageway 210″ and hence the first heater. In this example, the thermally conducting network 204″ is formed from an aluminium alloy. Alternatively, the thermally conducting network 204″ may be formed from copper, respective alloys thereof such as brass or bronze alloys, and/or stainless steel, as described previously.
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[0138] In this example, the hydrogen storage device 300 comprises: a pressure vessel 330, having a first fluid inlet 310 and/or a first fluid outlet 320, having therein a thermally conducting network 340 optionally thermally coupled to a first heater and/or a first cooler; wherein the pressure vessel 330 is arranged to receive therein a hydrogen storage material in thermal contact, at least in part, with the thermally conducting network 340; wherein the thermally conducting network 340 has a fractal geometry in two dimensions, comprising a plurality of nodes 341, having thermally conducting arms 342 therebetween, with voids V between the arms 342; and wherein the thermally conducting network 340 comprises fluidically interconnected passageways 343 therein, within the arms 342 and the nodes 341 thereof, for flow therethough of a fluid.
[0139] The hydrogen storage device 300 is generally as described with respect to the hydrogen storage device 100A of
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[0141] and wherein the thermally conducting network 240 has a lattice geometry in three dimensions.
[0142] In this example, the pressure vessel 230 is generally cylindrical, having a generally internally dished first end and a flanged second end opposed thereto, and having a single aperture providing both the first fluid inlet 210 and the first fluid outlet 220. In other words, the pressure vessel 230 is can-shaped. An inner wall portion 2301 of the pressure vessel 230 provides an axial cylindrical, elongate blind passageway P, arranged to optionally receive a second heater 300B (not shown) of the set of heaters 300, particularly a cartridge heater (not shown), that extends from the first end towards the second end and that is coaxial with an outer wall portion 2300 of the pressure vessel 230. Blind passageways in the second end are arranged to receive thermocouples TC. In this example, the first heater 300A is provided by a recirculating heater, for example heated using waste heat from a fuel cell coupled thereto, and includes a double helix heating tube 350, having an inlet 310 and an outlet 320, in thermal contact with the thermally conducting network 240, which is arranged between the inner 3501 and outer 3500 helices of the heating tube 350. The double helix heating tube 350 extends from the second end towards the first end is coaxial with an outer wall portion 2300 of the pressure vessel 230. The inner 3501 and outer 3500 helices of the double helix heating tube 350 are directly in thermal contact with the inner wall portion 2301 and the outer wall portion 2300 of the pressure vessel 230, respectively. A pressure gauge PG is provided in the second end. The second end is mechanically releasably coupled to the pressure vessel 230, using mechanical fasteners.
[0143] In this example, the thermally conducting network 240 has a lattice geometry in three dimensions, in which generally each node is connected by four arms to four other nodes, respectively, in an axially adjacent preceding layer, such that generally each node is thus connected by eight arms to eight other nodes, four nodes in the axially adjacent preceding layer and four nodes in an axially adjacent proceeding layer. Nodes proximal the inner 3501 and outer 3500 helices of the heating tube 350 are in mutual thermal contact therewith. In this example, an effective density of the lattice geometry is uniform in a first dimension, particularly axially, and non-uniform in mutually orthogonal second and third dimensions, particularly radially. In this example, the thermally conducting network 240 has a porosity of at least 90%. In this example, the thermally conducting network 240 is formed from an aluminium alloy. In this example, the thermally conducting network 240 comprises inner 2401 and outer 2400 portions, having annular shapes. The outer portion 2400 is received in thermal contact with and between the inner 3501 and outer 3500 helices of the double helix heating tube 350 while the inner portion 2401 is received in thermal contact with and within the inner helix 3501.
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[0146] In contrast with the hydrogen storage device 200 of
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[0148] The hydrogen storage device 200 comprises a pressure vessel 230, having a first fluid inlet 210 and a first fluid outlet 220, comprising therein a thermally conducting network 240 thermally coupled to a first heater 300A, wherein the pressure vessel 230 is arranged to receive therein a hydrogen storage material (not shown) in thermal contact, at least in part, with the thermally conducting network 240, wherein the first fluid inlet 210 and/or the first fluid outlet 220 are in fluid communication with the first releasable fluid inlet coupling (not shown) and/or the first releasable fluid outlet coupling (not shown), respectively; and wherein the thermally conducting network 240 has a lattice geometry in three dimensions. In this example, the hydrogen storage material comprises and/or is a liquid organic hydrogen carrier, LOHC. In this example, the hydrogen storage device 200 is a dynamic hydrogen storage device 200. In this example, the first fluid inlet 210 and the first fluid outlet 220 are mutually spaced apart at opposed ends of the first vessel 230, thereby defining, at least in part, a path for flow of the hydrogen storage material and/or hydrogen therebetween, for example via the voids of the thermally conducting network 240. In this example, the first fluid inlet 210 and the first fluid outlet 220 comprise releasable couplings, thereby providing coupling thereto and uncoupling therefrom, for example repeatedly, of corresponding couplings. In this example, the lattice geometry is Bravais lattice particularly a cubic lattice specifically a primitive cubic lattice. In this example, the thermally conducting arms have a cross sectional dimension (for example a diameter or a width) of about 0.5 mm. In this example, the thermally conducting network 240 partially fills an internal volume of the first vessel 230, of at least 90%, by volume of the first vessel 230. In this example, the thermally conducting network 240 comprises a LOHC hydrogenation and/or dehydrogenation catalyst, for example provided on and/or in a surface thereof. In this example, the thermally conducting network 240 has a porosity in a range from 75% to 95%, by volume of the thermally conducting network 240. In this example, the thermally conducting network 240 has a specific surface area in a range from 1 m.sup.−1 to 10 m.sup.−1, particularly about 7 m.sup.−1. In this example, the thermally conducting network 240 comprises a LOHC hydrogenation and/or dehydrogenation catalyst, for example provided on and/or in a surface thereof. In this example, the first heater is arranged heat the hydrogen storage material to temperature in a range from 150° C. to 300° C. In this example, the hydrogen storage device 200 comprises a pump (not shown) arranged to flow the hydrogen storage material through the first vessel 230. In this example, the hydrogen storage device 200 is a reactor.
[0149] Generally, the first vessel 230 is an elongated cylinder formed from a Ti alloy (to withstand an operating pressure of about 2 bar at a temperature of about 260° C. for dehydrogenation), having a bore extending therethrough for the first heater, particularly a Joule cartridge heater. The first fluid inlet 210 and the first fluid outlet 220 are provided with Swagelok releasable couplings. The first fluid inlet 210 is arranged at an acute angle to the axis of the first vessel and the first fluid outlet is arranged parallel to the axis, to suit the particular application.
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[0154] Like reference signs denote like features. In this example, the thermally conducting network 240 comprises metal foam quadrants or wedges, for example manufactured by rolling a sheet of foam around a tubular core and subsequently, dividing the rolled foam cylinder. Thermal contact with the walls of the pressure vessel 230 arises from compression of the foam thereagainst.
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[0157] Although a preferred embodiment has been shown and described, it will be appreciated by those skilled in the art that various changes and modifications might be made without departing from the scope of the invention, as defined in the appended claims and as described above.
Summary
[0158] In summary, the invention provides a hydrogen storage device comprising: a pressure vessel, having a first fluid inlet and/or a first fluid outlet, having therein a thermally conducting network optionally thermally coupled to a first heater and/or a first cooler; wherein the pressure vessel is arranged to receive therein a hydrogen storage material in thermal contact, at least in part, with the thermally conducting network; wherein the thermally conducting network preferably has a lattice geometry, a gyroidal geometry and/or a fractal geometry in two and/or three dimensions, comprising a plurality of nodes, having thermally conducting arms therebetween, with voids between the arms; and wherein the thermally conducting network comprises fluidically interconnected passageways therein, for example within the arms and/or the nodes thereof, for flow therethough of a fluid.
[0159] In this way, control for charging and/or release of hydrogen from the hydrogen storage device is improved because the flow of the fluid through the interconnected passageways in the thermally conducting network provides for faster, more homogenous, more accurate and/or more precise heating and/or cooling of the thermally conducting network and in turn, the hydrogen storage material in thermal contact therewith. Additionally and/or alternatively, in this way, storing and/or release of the hydrogen may be accelerated since heat generated or required, respectively, may be provided by the flow of the fluid through the interconnected passageways in the thermally conducting network. Disclosure
[0160] Attention is directed to all papers and documents which are filed concurrently with or previous to this specification in connection with this application and which are open to public inspection with this specification, and the contents of all such papers and documents are incorporated herein by reference.
[0161] All of the features disclosed in this specification (including any accompanying claims and drawings), and/or all of the steps of any method or process so disclosed, may be combined in any combination, except combinations where at most some of such features and/or steps are mutually exclusive.
[0162] Each feature disclosed in this specification (including any accompanying claims, and drawings) may be replaced by alternative features serving the same, equivalent or similar purpose, unless expressly stated otherwise. Thus, unless expressly stated otherwise, each feature disclosed is one example only of a generic series of equivalent or similar features.
[0163] The invention is not restricted to the details of the foregoing embodiment(s). The invention extends to any novel one, or any novel combination, of the features disclosed in this specification (including any accompanying claims and drawings), or to any novel one, or any novel combination, of the steps of any method or process so disclosed.