Patent Application
20250034726
Power-to-X relates to electricity conversion, energy storage, and reconversion pathways that use surplus electric power, typically during periods where fluctuating renewable energy generation exceeds load.
Electrolyzers are devices that use electricity to drive an electrochemical reaction to break, e.g., water into hydrogen and oxygen. The construction of an electrolyzer is very similar to a battery or fuel cell; it consists of an anode, a cathode, and an electrolyte.
The hydrogen produced from an electrolyzer is perfect for use with hydrogen fuel cells. The reactions that take place in an electrolyzer are very similar to the reactions in fuel cells, except the reactions that occur in the anode and cathode are reversed. In a fuel cell, the anode is where hydrogen gas is consumed, and in an electrolyzer, the hydrogen gas is produced at the cathode. A very sustainable system can be formed when the electrical energy needed for the electrolysis reaction comes from renewal energy sources, such as wind or solar energy systems.
Direct current electrolysis (efficiency 80-85% at best) can be used to produce hydrogen which can, in turn, be converted to, e.g., methane (CH4) via methanation, or converting the hydrogen, along with CO2, to methanol, or to other substances.
The energy, such as hydrogen, generated in this manner, e.g. by means of wind turbines, then can be stored for later usage.
Electrolyzers can be configured in a variety of different ways, and are generally divided into two main designs: unipolar and bipolar. The unipolar design typically uses liquid electrolyte (alkaline liquids), and the bipolar design uses a solid polymer electrolyte (proton exchange membranes).
Alkaline water electrolysis has two electrodes operating in a liquid alkaline electrolyte solution of potassium hydroxide (KOH) or sodium hydroxide (NaOH). These electrodes are separated by a diaphragm, separating the product gases, oxygen, O2, and hydrogen, H2, and transporting the hydroxide ions (OH−) from one electrode to the other.
Other fuels and fuel cells include phosphoric acid fuel cells, molten carbonate fuel cells, solid oxide fuel cells, and all their subcategories as well. Such fuel cells are adaptable for use as an electrolyzer as well.
It is an advantage if the fluid solutions operating in the plant are within given temperatures to optimize the efficiency. It is also an advantage if the plant could be compact and scalable.
It is an object of embodiments of the invention to provide a cassette for an electrolyzer, the electrolyzer being easily producible, efficient and scalable.
The invention provides a cassette for an electrolyzer, the cassette comprising a cooling plate and an electrolyte plate defining an electrolyte flow path between them, and where the electrolyte plate is formed with at least one electrolyte fluid inlet at a first end section and at least one gas outlet at a second, opposite end section and defines an active area between the first end section and the second end section, where at least one of the at least one gas outlet is partly surrounded by an outlet blockade with an opening formed therein, allowing gas only to leave the second end section towards the at least one gas outlet via the opening in the outlet blockade.
Thus, the invention provides a cassette for an electrolyzer. The cassette comprises a cooling plate and an electrolyte plate arranged relative to each other in such a manner that an electrolyte flow path is defined between the cooling plate and the electrolyte plate. The electrolyte plate may, e.g., be in the form of an anodic electrolyte plate or in the form of a cathodic electrolyte plate.
The electrolyzer cassette may be stacked with several other electrolyzer cassettes to form an electrolyzer.
A cooling flow path may be formed on the side of the cooling plate which is arranged opposite to the side facing the electrolyte plate and the electrolyte flow path. This allows a cooling fluid flowing in the cooling path to provide cooling to an electrolytic fluid flowing in the electrolyte flow path. Accordingly, a suitable temperature of the electrolytic fluid can thereby be obtained, and this ensures that the electrolyzer is able to operate in an efficient manner.
The electrolyte plate is formed with at least one electrolyte fluid inlet and at least one gas outlet. Accordingly, electrolytic fluid (mainly in liquid form) being supplied to the electrolyte flow path as well as electrolytic fluid (mainly in gaseous form) leaving the electrolyte flow path, can pass through the electrolyte plate. This will allow electrolyte fluid to be supplied to and retrieved from the respective electrolyte flow paths when the electrolyte plate forms part of an electrolyzer cassette, and also when such an electrolyzer cassette is stacked with other electrolyzer cassettes to form an electrolyzer.
The at least one electrolyte fluid inlet is formed at a first end section of the electrolyte plate, and the at least one gas outlet is formed at second, opposite end section of the electrolyte plate. Accordingly, the at least one fluid inlet and the at least one gas outlet are arranged at opposite ends of the electrolyte plate, e.g. as seen along a length direction of the electrolyte plate. Thus, an electrolytic fluid flowing in the electrolyte flow path from the at least one fluid inlet to the at least one gas outlet will pass along a substantial part of the area of the electrolyte plate.
An active area is defined between the first end section and the second end section, and thereby also between the at least one electrolyte fluid inlet and the at least one gas outlet. Accordingly, the electrolyte flowing in the electrolyte flow path passes the active area. The active area may, e.g., be provided with electrolyte plate openings and/or be covered by a membrane. The electrolyte plate openings form a porous area of the electrolyte plate and may be adapted to pass gas across the electrolyte plate between a membrane to be positioned at the one side of the electrolyte plate and an electrolyte flow path positioned at the other side of the electrolyte plate. When electrolyzer cassettes are stacked into an electrolyzer, an anodic electrolyte plate of one electrolyzer cassette will be arranged adjacent to a cathodic electrolyte plate of a neighbouring electrolyzer cassette, and a membrane will be arranged between the anodic electrolyte plate and the cathodic electrolyte plate. This allows transport of hydronic ions (H−) from the cathodic electrolyte plate to the anodic electrolyte plate, via the membrane, while keeping the product gases resulting from the electrolysis (e.g. O2 and H2, respectively) separated. Accordingly, the active area defines a part of the electrolyzer where electrolysis takes place.
At least one of the at least one gas outlet is partly surrounded by an outlet blockade with an opening formed therein, allowing gas only to leave the second end section towards the at least one gas outlet via the opening in the outlet blockade. Accordingly, the outlet blockade partly separates the at least one gas outlet from the second end section, and the only passage from the second end section to the at least one gas outlet is via the opening formed in the outlet blockade. Electrolytic fluid which leaves the active area and flows towards the at least one gas outlet, via the second end section, may be in the form of a vapour, i.e. a mixture of product gases and liquid electrolyte. It is desirable that only the product gases leave the electrolyzer via the at least one gas outlet, whereas it is desirable to keep the liquid electrolyte in the electrolyzer. This is due to the fact that liquid being passed on in the system may cause short circuits. Furthermore, it is desirable to utilize all of the liquid electrolyte for the electrolysis process.
The outlet blockade prevents that the vapour flowing from the active area towards the at least one gas outlet, via the second end section, enters the at least one gas outlet directly and unhindered. Instead the outlet blockade forms an obstacle which forces the vapour flow to follow a longer flow path, in particular within a region defined by the second end section. This increases the probability that the liquid part of the vapour flow interacts with an obstacle, a side wall or similar, causing a separation of the liquid and the gaseous part of the vapour. Accordingly, mainly product gases will leave the second end section via the at least one gas outlet, and the liquid part of the vapour will mainly remain in the system. The liquid may be drained back into the active area, and may therefore be applied in the electrolysis process taking place there.
The opening in the outlet blockade may be arranged at a side of the at least one gas outlet which is opposite to a side which faces the active area. According to this embodiment, the opening in the outlet blockade is positioned in such a manner that vapour entering the second end section from the active area needs to pass a region defined by the at least one gas outlet before reaching the opening in the outlet blockade, via which it can reach the gas outlet and leave the electrolyzer. This even further increases the probability that the liquid part of the vapour flow interacts with an obstacle, a side wall or similar, causing a separation of the liquid and the gaseous part of the vapour, and therefore even further decreases the risk that liquid enters the gas outlet.
The outlet blockade may further be formed with an outlet blockade drain arranged substantially opposite to the opening. According to this embodiment, liquid which passes through the opening in the outlet blockade, from the second end section, can be drained back towards the second end section, via the blockade drain, rather than entering the gas outlet, further decreasing the risk of liquid entering the gas outlet.
The opening in the outlet blockade and the blockade drain may be arranged in such a manner that the blockade drain is closer to the active area than the opening in the outlet blockade. This ensures that the vapour needs to travel a longer distance in order to reach the opening in the outlet blockade, as described above. Furthermore, the liquid drained via the blockade drain is guided towards the active area.
The cassette may be oriented in such a manner that the opening formed in the outlet blockade is arranged above the at least one gas outlet. For instance, during operation, the cassette may be oriented in such a manner that the second end section is arranged above the first end section and above the active area, e.g. directly above the first end section and the active area along a substantially vertical direction. In this case the gaseous part of the vapour will tend to move upwards, and thereby towards the opening formed in the outlet blockade above the gas outlet, whereas the liquid part of the vapour will tend to move downwards, towards the active area, assisted by gravity. This even further reduces the risk that liquid enters the gas outlet.
The outlet blockade may be formed by one or more projections on the electrolyte plate and/or on the cooling plate. According to this embodiment, the outlet blockade may form an integral part of either the electrolyte plate or the cooling plate. As an alternative, the outlet blockade may comprise a part or portion forming part of the electrolyte plate as well as a part or portion forming part of the cooling plate, the two parts or portions cooperating in forming the outlet blockade. In any event, the outlet blockade may be adapted to contact a neighbouring plate, i.e. the outlet blockade may form a contact between the electrolyte plate and the cooling plate forming the electrolyte flow path therebetween. Forming the outlet blockade as one or more projections on the electrolyte plate and/or on the cooling plate is an easy manner of forming the outlet blockade as an integral part of the electrolyte plate and/or the cooling plate. For instance, the projections may be formed by stamping or a similar process when the electrolyte plate and/or the cooling plate is formed.
The at least one gas outlet may be provided with an outer gasket, and the outer gasket may be formed with beads reaching into the gas outlet, where the beads extend into the gas outlet of the cassette as well as into the gas outlet of a neighbouring cassette.
The outer gasket may, e.g., be positioned at an outer circumference of the at least one gas outlet and may be arranged to seal to the externals when another cassette is positioned adjacent to the cassette.
According to this embodiment, liquid is prevented from flowing into the gas outlet. Furthermore, fluid is prevented from leaking into the section between connected cassettes.
The electrolyte plate and/or the cooling plate may be symmetric with respect to a centre line of the plate, extending along a length direction of the plate. For instance, a right half of the plate may mirror a left half of the plate.
The electrolyte plate may further be formed with a cooling inlet opening and a cooling outlet opening for a cooling fluid to pass the electrolyte plate. This will allow cooling fluid to be supplied to and retrieved from a cooling flow path defined between two cooling plates when the electrolyte plate forms part of an electrolyzer cassette, and also when such an electrolyzer cassette is stacked with other electrolyzer cassettes to form an electrolyzer.
The at least one gas outlet may be positioned between the cooling inlet opening and the cooling outlet opening. According to this embodiment, an extended cooling path for the gaseous products is provided, thereby ensuring efficient cooling thereof.
The electrolyte plate may define a centre line passing in a length direction of the cassette, the at least one gas outlet may include an anodic gas outlet and a cathodic gas outlet, and the anodic gas outlet may be positioned at a first side of the centre line and the cathodic gas outlet may be positioned at a second, opposite side of the centre line. According to this embodiment, it is prevented that the gaseous products of the anodic electrolyte flow path and the cathodic electrolyte flow path, respectively, mix.
For instance, the plates may be symmetrical with respect to the centre line, e.g. a right half of the plate mirroring a left half of the plate. In this case, the symmetric property of the plates results in an identical front and back side of the plates. This enables to use the plates on both sides, without having to consider for correct side orientation. Additionally, the same plate can be used as an anodic electrolyte plate or as a cathodic electrolyte plate. This is also correlated with the manufacturing process. For instance, only one process and identical tools can be used to produce the anodic electrolyte plate and the cathodic electrolyte plate. Similar advantages are obtained with regards to the two cooling plates.
For instance, the anodic gas outlet may be positioned at the first side of the centre line substantially halfway between a first side edge of the electrolyte plate and the centre line, and/or the cathodic gas outlet may be positioned at the second side of the centre line substantially halfway between a second side edge of the electrolyte plate and the centre line.
The cassette may comprise two cooling plates and two electrolyte plates, in the form of an anodic electrolyte plate and a cathodic electrolyte plate, and the two cooling plates may be positioned between the anodic electrolyte plate and the cathodic electrolyte plate. According to this embodiment, a cooling flow path is formed between the two cooling plates, an anodic electrolyte flow path is formed between one of the cooling plates and the anodic electrolyte plate, and a cathodic electrolyte flow path is formed between the other cooling plate and the cathodic electrolyte plate. Thus, a cooling fluid flowing in the cooling flow path provides cooling to an anodic electrolytic fluid flowing in the anodic electrolyte flow path as well as to a cathodic electrolytic fluid flowing in the cathodic electrolyte flow path. This allows for efficient cooling of these fluids, and a suitable temperature of the anodic electrolytic fluid as well as of the cathodic electrolytic fluid can thereby be obtained. This ensures that the electrolyzer is able to operate in an efficient manner.
The electrolyte plates and cooling plates may each be formed with cooling openings for a cooling fluid to pass the plate, at least one anodic electrolyte fluid inlet for an anodic electrolyte fluid to pass the plate, at least one cathodic electrolyte fluid inlet for a cathodic electrolyte fluid to pass the plate, at least one anodic gas outlet for an anodic gas to pass the plate, and at least one cathodic gas outlet for a cathodic gas to pass the plate, and each of the respective openings may reach through all four plates and combine with the similar respective openings of neighbouring connected cassettes.
According to this embodiment, when the cassette is stacked with several other cassettes to form an electrolyzer, the respective openings formed in the cooling plates and the electrolyte plates are aligned, and allow relevant fluids to be easily supplied to and retrieved from the relevant flow paths in the electrolyzer. For instance, cooling fluid can be supplied to and retrieved from the cooling flow paths via the cooling openings. Furthermore, anodic electrolytic fluid can be supplied to the anodic electrolyte flow paths via the anodic electrolyte fluid inlets and anodic gas product can be retrieved from the anodic electrolyte flow path via the anodic gas outlets. Finally, cathodic electrolytic fluid can be supplied to the cathodic electrolyte flow paths via the cathodic electrolyte inlets and cathodic gas product can be retrieved from the cathodic electrolyte flow paths via the cathodic gas outlets. This allows for a compact and scalable design of the electrolyzer.
The cooling plates and the electrolyte plates in the cassette may be connected such that the cooling openings are sealed from an anodic electrolyte flow path formed between one of the cooling plates and the anodic electrolyte plate, and from a cathodic electrolyte flow path formed between the other cooling plate and the cathodic electrolyte plate, and the cooling openings may be in fluid connection to a cooling flow path formed between the cooling plates. According to this embodiment, it is ensured that the cooling fluid is neither mixed with the anodic electrolytic fluid nor with the cathodic electrolytic fluid, while ensuring that cooling fluid can be supplied to and retrieved from the cooling flow path.
Similarly, the cooling plates and the electrolyte plates in the cassette may be connected such that the anodic electrolyte fluid inlets and the anodic gas outlets are sealed from respectively the cooling flow path and the cathodic electrolyte fluid inlets and the cathodic gas outlets. According to this embodiment, it is ensured that the anodic electrolytic fluid is neither mixed with the cooling fluid, nor with the cathodic electrolytic fluid.
Similarly, the cooling plates and the electrolyte plates in the cassette may be connected such that the cathodic electrolyte fluid inlets and the cathodic gas outlets are sealed from respectively the cooling flow path and the anodic electrolyte fluid inlets and the anodic gas outlets. According to this embodiment, it is ensured that the cathodic electrolytic fluid is neither mixed with the cooling fluid, nor with the anodic electrolytic fluid.
In the embodiments described above, it is efficiently ensured that the various flow paths are separated from each other, and accordingly that various fluids flowing in the cassette are kept separated and prevented from mixing.
The detailed description and specific examples, while indicating embodiments of the invention, are given by way of illustration only.
Each cooling plate 2 is patterned, and one side of one of the cooling plates 2 connects to an anodic plate 3a, and the other of the two cooling plates 2, at one side, connects to a cathodic plate 3c. The two cooling plates 2, at their respective other sides, are connected to each other. Thus, the two cooling plates 2 face each other, at one side, and at the other, opposite side, they each face an electrolyte plate 3a, 3c in the form of an anodic plate 3a and a cathodic plate 3c, respectively.
A cooling path 5 is formed between the two connected cooling plates 2, adapted for a cooling fluid to pass from a cooling fluid inlet 7in to a cooling fluid outlet 7out.
Similarly, an anodic electrolyte path 6a is formed between the anodic plate 3a and the connected one of the cooling plates 2, and a cathodic electrolyte path 6c is formed between the cathodic plate 3c and the connected one of the cooling plates 2.
Electrolyte is fed via an anodic electrolyte fluid inlet 8in into the anodic electrolyte path 6a to replace the electrolyte being transferred into gas (e.g. O2), leaving the anodic electrolyte path 6a via an anodic electrolyte gas outlet 8out. Similarly, electrolyte is fed via a cathodic electrolyte fluid inlet 9in into the cathodic electrolyte path 6c to replace the electrolyte within the cathodic electrolyte path 6c being transferred into gas (e.g. H2), leaving the cathodic electrolyte path 6c via a cathodic electrolyte gas outlet 9out.
The cassette 1 is adapted for a thin, porous foil, also referred to as a diaphragm or membrane 4, to be positioned between respectively an anodic plate 3a and a cathodic plate 3c of two connected cassettes 1 (see also
The membrane 4 is electrically insulating, or nonconductive, in order to avoid electrical shorts between the electrolyte plates 3a, 3c.
The membranes 4 may be connected at the outside surfaces of the electrolyte plates 3a, 3c relative to respectively the anodic electrolyte path 6a and cathodic electrolyte path 6c, and may be fixed by a clip-on gasket to be described in more detail later.
An electrolyte solution, e.g. potassium hydroxide (KOH) or sodium hydroxide (NaOH), is fed to the anodic electrolyte path 6a via the anodic electrolyte fluid inlet 8in, and to the cathodic electrolyte path 6c via the cathodic electrolyte fluid inlet 9in.
The electrolyte plates 3a, 3c are porous, at least in the area adapted to match with the membrane 4, allowing the diffusion of the product gases and the transportation of hydroxide ions (OH−) across the membranes 4, and hence the porous areas of the electrolytic plates 3a, 3c.
The flaps 11a reach towards the cooling plate 2 arranged adjacent to the electrolyte plate 3a, 3c, possibly without contacting it, and thus into the respective electrolyte path 6a, 6c. The flaps 11a may be positioned such that they ‘point’ in the direction of the respective electrolyte gas outlet 8out, 9out, thereby ensuring a smooth flow of the entering gasses, such as hydrogen or oxygen gasses.
The recess 12 is formed at the otherwise flat surface adapted to face the membrane 4, and is formed in order to ease and direct the flow of gasses, such as hydrogen and oxygen, from the membrane 4 towards the openings 11.
The pushed outwards section 11b could be positioned such that at least one of the two openings 11 formed below the pushed outwards section 11b points in the direction of the respective electrolyte gas outlet 8out, 9out. This ensures a smooth flow of the entering gasses, such as hydrogen or oxygen gasses.
The opposite surface of the electrolyte plate 3a, 3c to the one in the bending direction of the pushed outwards sections 11b is essentially flat. The electrolyte plate 3a, 3c is positioned with the flat surface facing outwards relative to the connected cooling plate 2, to form a contact surface to the membrane 4.
The pushed outwards sections 11b will then face the respective cooling plate 2, preferably without contacting it, and thus extend into the respective electrolyte path 6a, 6c.
The flanges 11c could be positioned such that free ends of the flanges 11c point in the direction of the respective electrolyte gas outlet 8out, 9out. This ensures a smooth flow of the entering gasses, such as hydrogen or oxygen gasses.
The opposite surface of the electrolyte plate 3a, 3c to the one in the bending direction of the flanges 11c is essentially flat. The electrolyte plate 3a, 3c is positioned with the flat surface to form a contact surface to the membrane 4.
The flanges 11c will then reach towards the respective cooling plate 2, preferably without contacting it, and thus into the respective electrolyte path 6a, 6c.
In the illustrated embodiment, the opening 11 has a curving shape, similar to a meat bone, and may therefore be referred to as being ‘meat bone’-shaped. This means that the opening 11 has concave sections as well as convex sections. In the illustrated embodiment, the two ends arranged opposite each other along a direction defined by the length of the opening 11 are concave seen from the inside of the opening 11d, 11e, and convex sections are present at the centre part, seen from the inside of the opening 11d, 11e. The ends, thus, may form part of a circular or elliptic shape. The convex sections are having a width X which is smaller than the width Y of the concave section. The angle between the line (D) defined by two points (A and B) and the horizontal axis (H) is between 5° and 20°.
The opening 11d, 11e, 11f may be symmetric with two halves mirroring each other.
The centre line L also corresponds to a line parallel to the length direction of the plates 2, 3a, 3c.
According to one embodiment, the openings 11 may, at the centre portions, have a smaller width than the upper width or diameter of a contact column 19. This ensures that only a part of the opening 11 is obstructed by the contact column 19, while maintaining a contact to the electrolyte plate 3a, 3c.
The embodiment with contact areas for contact columns 19 or the smaller width diameter could also apply to any of the embodiments of
An active area of the electrolyte plate 3a, 3c is formed between the electrolyte fluid inlets 8in, 9in and gas outlets 8out, 9out and is formed with the openings 11, i.e. the active area is porous. This active area is adapted to be aligned with the membrane 4.
In the illustrated embodiment, cooling fluid openings 7in, 7out, being cooling fluid inlets 7in and/or cooling fluid outlets 7out, are positioned at the corners of the plates 3a, 3c, 2, but they could be positioned elsewhere, such as at the centre of the plates 3a, 3c, 2.
The cooling fluid flow direction in the cooling path 5 could be counter to the electrolyte fluid flow direction in the respective electrolyte paths 6a, 6c. As an alternative, the cooling fluid flow and the electrolyte fluid flow may be in the same direction. The cooling fluid inlet 7in and/or the cooling fluid outlet 7out, respectively, may consist of one or a plural of openings 7in, 7out, such as two openings 7in, 7out as illustrated.
The embodiment further shows an anodic electrolyte inlet 8in and a cathodic electrolyte inlet 9in, respectively, positioned between the two cooling openings 7in, 7out, such as in each their half of the plates 3a, 3c, 2, seen in relation to a centre line L passing in a length direction of the cassette 1, and thereby in a length direction of the plates 3a, 3c, 2. The electrolyte inlets 8in, 9in could, for example, be positioned at or near the centre of each their half.
The electrolyte plates 3a, 3c, and possibly also the cooling plates 2, may be symmetric relative to the centre line L, the left half of a respective plate 3a, 3b, 2 mirroring the right half thereof.
The four plates 3a, 3c, 2 in the cassette 1 are connected such that the cooling openings 7in, 7out are in fluid connection to the cooling path 5, but are sealed from the electrolyte paths 6a, 6c. The anodic electrolyte openings 8in, 8out are sealed from respectively the cooling fluid path 5 and from the cathodic electrolyte openings 9in, 9out. In the same manner, the cathodic electrolyte openings 9in, 9out are sealed from respectively the cooling fluid path 5 and the anodic electrolyte openings 8in, 8out. This is illustrated in more details in
Projections 55 may be formed in the plates 3a, 3c, 2 at the circumference of the respective openings 7in, 7out, 8in, 8out, 9in, 9out to contact the neighbouring plates 3a, 3c, 2, possibly contacting similar projections 55 formed in the neighbouring plates 3a, 3c, 2. This stabilizes the areas of the respective openings 7in, 7out, 8in, 8out, 9in, 9out.
Openings 56, see also
In
In
In
In
The electrolyte paths 6a, 6c may comprise a section stretching from the edges 60 of the plates 2, 3a, 3c towards the centre line L and the respective electrolyte gas outlet 8out, 9out.
One of the respective electrolyte gas outlets 8out, 9out will be open to the respective electrolyte path 6a, 6c, whereas the other will be closed, or sealed, e.g. by a gasket 33, in a manner similar to the cooling fluid openings 7in, 7out, and optionally also the circumference edge of the plates 2, 3a, 3c.
In order to partly separate the upper section electrolyte paths 6a, 6c around the electrolyte gas outlets 8out, 9out from the lower sections where the main gas generation occurs, an inner gas barrier 26 is provided, which obstructs the gas from flowing back to the lower section of the active area.
The inner gas barrier 26 may comprise two halves, each declining or sloping towards the centre line L, corresponding to declining or sloping towards the active area, where a drain 27 in the inner gas barrier 26 is positioned, allowing fluids, in particular in the form of liquid, in the section to drip back to the active area for further processing, due to gravity. This further prevents that liquid enters the gas outlet 8out, 9out and is passed further on in the system. This is an advantage, because liquid being passed on may introduce a risk of short circuiting.
The cassette 1 may be adapted to be positioned in a substantially vertical position with the gas outlets 8out, 9out at the top and electrolyte fluid inlets 8in, 9in at the bottom. Then liquids which are not dissolved will tend to fall downwards, due to gravity, and will be collected by the inner gas barrier 26 since they are heavier than the gas. The declining or sloping gas barrier 26 will guide the liquids towards the gas barrier drain 27.
A lower inner gas barrier 26a may be positioned at the gas barrier drain 27, immediately at the side facing the active area below the inner gas barrier drain 27.
The barrier 26, 26a, 27 may be formed in either of the electrolyte plates 3a, 3c or the connected cooling plate 2, or both, and will be adapted to contact the neighbouring plate 2, 3a, 3c.
The section illustrated in
The respective electrolyte gas outlet 8out, 9out is partly surrounded by an outlet blockade 28 only allowing the gas to leave the section and move towards the electrolyte gas outlet 8out, 9out, via an opening 29 in the outlet blockade 28. Facing the lower sections, the outlet blockade 28 may be provided with an outlet blockade drain 30, allowing possibly remaining fluids, primarily in the form of liquids, to drain back to the section.
Barriers, such as the gas barriers 24, the inner gas barrier 26 and the outlet blockade 28, may be formed by projections on the plates 2, 3a, 3c facing each other and being connected, thus obstructing fluid and gas from passing. Similarly, the dimples 25 may be formed by projections, possibly projecting to both sides and contacting at both the opposing sides of a plate 2, 3a, 3c, in order to form support in the section.
The membrane 4 is clamped between the two electrolyte plates 3a, 3c of the connected cassettes 1 and placed in grooves 13a′ in the electrolyte plates 3a, 3c to hold them in place. For this, the gasket parts 13, 14 may be formed with projections 13′, 14′ adapted to be positioned within the grooves 13a′.
One gasket part, e.g. the second gasket part 14, is formed with a locking part 15 that extends through a hole 4a in the membrane 4 and a gasket hole 16 of the other gasket part, e.g. the first gasket part 13. The outer part of the locking part 15 has a larger diameter than the hole 4a of the membrane 4 and must therefore be pushed through with a force. This ensures that the membrane 4 and the gasket parts 13, 14 are kept firmly together, and that relative movements therebetween are essentially prevented. Accordingly, it is ensured that the various parts of the cassette 1 remain properly aligned with respect to each other, and the risk of leaking is minimised.
Either of the first gasket part 13 and/or the second gasket part 14 could be provided with respectively locking part(s) 15 and gasket opening(s) 16.
The first gasket part 13 or the second gasket part 14, respectively, could be the gasket 33′ encircling the active area.
In an embodiment, the gasket 33′ is formed of respectively the first gasket part 13 and the second gasket part 14, these being adapted to seal at each their side of the membrane 4. The respective first gasket part 13 and second gasket part 14 could be formed of different materials suitable for each their environments at the two sides of the membrane 4, the one possibly being made of a cheap material.
Such fixations 4a, 13a′, 13′, 14′, 15, 16 could be positioned at regular intervals at the circumference of the membrane 4.
The intention of the cooling cells 17 is to ensure an even distribution of cooling, or the cooling fluid, across the cooling plate 2, and accordingly across the neighbouring electrolyte plate 3a, 3c.
The cooling cells 17 may be formed with a pattern 18 adapted to contact a similar pattern 18 of a connected neighbouring cooling plate 2, forming a cooling path 5 within the cooling cells 17. The pattern 18, however, does not contact the electrolyte plate 3a, 3c positioned at the opposite side, and therefore contact columns 19 are distributed over the cooling plate 2, such as within the cooling cells 17, as illustrated in
The contact columns 19 are situated to contact the respective neighbouring electrolyte plate 3a, 3c in the areas between the electrolyte plate openings 11. This ensures support of the plates 2, 3a, 3c as well as a uniform distance between the cooling plates 2 and the electrolyte plates 3a, 3c, across the entire active area, and essentially regardless of the pressure conditions within the electrolyzer cassette. The contact columns 19 may also form the electrical contact to the electrolyte plates 3a, 3c supplying them with a current/voltage.
The contact columns 19 may be fixedly attached to the respective electrolyte plates 3a, 3c, e.g. by welding or soldering. Alternatively, the contact columns 19 may simply be pushed into contact with the respective electrolyte plates 3a, 3c by pressing the plates 2, 3a, 3c together.
In the embodiment illustrated in
Each cooling cell 17 is provided with cooling fluid from a cooling cell supply channel 20 extending between the cooling cells 17, via respective cooling cell inlets 21. Each cooling cell supply channel 20 may connect to a plural of cooling cells 17.
The cooling fluid (now with an increased temperature) leaves the cooling cells 17 via a cooling cell outlet 23, and is fed to cooling cell return channels 22, where each cooling cell return channel 22 may connect to a plural of cooling cells 17.
According to one embodiment, the area of the cooling plates 2 formed with cooling cells 17 may be adapted to be aligned with the active area of the electrolyte plates 3a, 3c, enabling a control of the temperature in the gas generating processes occurring in the electrolytic fluids in the electrolyte flow paths 6a, 6c.
The cooling cells 17 are enclosed by a cooling cell wall 17a, where the respective cooling cell inlets 21 and cooling cell outlets 23 are formed in the cooling cell wall 17a. The cooling cell wall 17a separates the individual cooling cells 17 from each other and may be formed as a projection in the two cooling plates 2 connecting to form a flow barrier.
The corrugated pattern 18 illustrated in
The cooling cell inlets 21 and the cooling cell outlets 23 of the connected cooling cells 17 of the respective two connected cooling plates 2 are positioned to align. In the illustrated embodiment, the inlets 21 are positioned at an upper part and the outlets 23 at a bottom part of the cooling cell walls 17a, seen relative to the flow direction of cooling fluid flow.
The contact columns 19 are seen pointing towards the electrolyte plates 3a, 3c, contacting these. An electrical contact is created by the contact columns 19 to the electrolyte plates 3a, 3c, the cooling plates 2 themselves thus operating as electrical conductors.
The contact columns 19 may not be fixed to the electrolyte plates 3a, 3c, and in an embodiment contact may be ensured by the pressure of the electrolyte solution in the electrolyte paths 6a, 6c being higher than the pressure of the cooling fluid 2 in the cooling fluid path 5.
While the present disclosure has been illustrated and described with respect to a particular embodiment thereof, it should be appreciated by those of ordinary skill in the art that various modifications to this disclosure may be made without departing from the spirit and scope of the present disclosure.
| Number | Date | Country | Kind |
|---|---|---|---|
| PA202170630 | Dec 2021 | DK | national |
| PA202270125 | Mar 2022 | DK | national |
This application is a National Stage application of International Patent Application No. PCT/EP2022/085914, filed on Dec. 14, 2022, which claims priority to Danish Patent Application No. PA202170630, filed Dec. 17, 2021, and Danish Patent Application No. PA202270125, filed Mar. 22, 2022, each of which is hereby incorporated by reference in its entirety.
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/EP2022/085914 | 12/14/2022 | WO |
