EP4001463A1 - Agencement et procédé d'électrolyse - Google Patents

Agencement et procédé d'électrolyse Download PDF

Info

Publication number
EP4001463A1
EP4001463A1 EP20207789.7A EP20207789A EP4001463A1 EP 4001463 A1 EP4001463 A1 EP 4001463A1 EP 20207789 A EP20207789 A EP 20207789A EP 4001463 A1 EP4001463 A1 EP 4001463A1
Authority
EP
European Patent Office
Prior art keywords
anode
cathode
separator
medium
stack
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
EP20207789.7A
Other languages
German (de)
English (en)
Inventor
Alexander BEHR
Gary Combes
Tibor SVITNIC
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
LAir Liquide SA pour lEtude et lExploitation des Procedes Georges Claude
Original Assignee
Air Liquide SA
LAir Liquide SA pour lEtude et lExploitation des Procedes Georges Claude
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Air Liquide SA, LAir Liquide SA pour lEtude et lExploitation des Procedes Georges Claude filed Critical Air Liquide SA
Priority to EP20207789.7A priority Critical patent/EP4001463A1/fr
Priority to AU2021258014A priority patent/AU2021258014A1/en
Priority to CN202111329878.6A priority patent/CN114507871A/zh
Publication of EP4001463A1 publication Critical patent/EP4001463A1/fr
Pending legal-status Critical Current

Links

Images

Classifications

    • C—CHEMISTRY; METALLURGY
    • C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B9/00—Cells or assemblies of cells; Constructional parts of cells; Assemblies of constructional parts, e.g. electrode-diaphragm assemblies; Process-related cell features
    • C25B9/70—Assemblies comprising two or more cells
    • C—CHEMISTRY; METALLURGY
    • C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B1/00—Electrolytic production of inorganic compounds or non-metals
    • C25B1/01—Products
    • C25B1/02—Hydrogen or oxygen
    • C—CHEMISTRY; METALLURGY
    • C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B1/00—Electrolytic production of inorganic compounds or non-metals
    • C25B1/01—Products
    • C25B1/02—Hydrogen or oxygen
    • C25B1/04—Hydrogen or oxygen by electrolysis of water
    • C—CHEMISTRY; METALLURGY
    • C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B15/00—Operating or servicing cells
    • C25B15/02—Process control or regulation
    • C—CHEMISTRY; METALLURGY
    • C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B15/00—Operating or servicing cells
    • C25B15/02—Process control or regulation
    • C25B15/023—Measuring, analysing or testing during electrolytic production
    • C—CHEMISTRY; METALLURGY
    • C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B15/00—Operating or servicing cells
    • C25B15/08—Supplying or removing reactants or electrolytes; Regeneration of electrolytes
    • C25B15/083—Separating products
    • C—CHEMISTRY; METALLURGY
    • C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B15/00—Operating or servicing cells
    • C25B15/08—Supplying or removing reactants or electrolytes; Regeneration of electrolytes
    • C25B15/087—Recycling of electrolyte to electrochemical cell
    • C—CHEMISTRY; METALLURGY
    • C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B9/00—Cells or assemblies of cells; Constructional parts of cells; Assemblies of constructional parts, e.g. electrode-diaphragm assemblies; Process-related cell features
    • C—CHEMISTRY; METALLURGY
    • C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B9/00—Cells or assemblies of cells; Constructional parts of cells; Assemblies of constructional parts, e.g. electrode-diaphragm assemblies; Process-related cell features
    • C25B9/60—Constructional parts of cells
    • C—CHEMISTRY; METALLURGY
    • C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B9/00—Cells or assemblies of cells; Constructional parts of cells; Assemblies of constructional parts, e.g. electrode-diaphragm assemblies; Process-related cell features
    • C25B9/60—Constructional parts of cells
    • C25B9/65—Means for supplying current; Electrode connections; Electric inter-cell connections

Definitions

  • the invention is directed to an electrolysis arrangement and a method for performing an electrolysis.
  • electrolysis is usually performed using stacks of electrolysis cells.
  • Each of the electrolysis cells has an anode and a cathode, between which a voltage is applied.
  • the medium that is the subject of the electrolysis is supplied to the electrolysis cells via a cathode inlet into a cathode space and via an anode inlet into an anode space.
  • the anode space and the cathode space are separated from each other by a membrane.
  • the electrolysis products can be extracted from the electrolysis cells.
  • the electrolysis products are mixed with the unreacted medium.
  • separators are used to separate the electrolysis products from the medium.
  • the pressure differential across the membrane has a significant influence on the electrolysis. In particular, this is due to the fact that a pressure difference between the cathode space and the anode space drives the medium through the membrane. Hence, accurate pressure control is desired.
  • the overall pressure is usually controlled by a pump that drives the medium.
  • the pressure differential between the anode and cathode inlets of an electrolysis stack usually depends on a back pressure generated by the anode and cathode separators, respectively.
  • each stack is provided with a respective anode separator and with a respective cathode separator. Having a respective anode separator and a respective cathode separator for each electrolysis stack is considered necessary in terms of reliability. However, such an arrangement is expensive.
  • each of the electrolysis stacks is usually equipped with a respective cooler and filter, together with appropriate safety and control instrumentation. This is not only relevant in terms of an initial investment, but also in terms of maintenance costs dues to the large number of pieces of equipment.
  • the object of the invention is to improve the prior art such that electrolysis can be performed with simplified equipment.
  • an electrolysis arrangement that comprises:
  • the electrolysis arrangement can be used for electrolysis of a medium.
  • the medium is water.
  • hydrogen and oxygen can be obtained as electrolysis products.
  • the electrolysis arrangement is intended to be used for an industrial scale electrolysis. For example, it is preferred that at least one of the electrolysis products is obtained at a rate of 250 to 1500 Nm 3 per hour per stack. This applies, in particular, to the production of hydrogen in the case of water electrolysis.
  • the electrolysis is preferably performed in an automated way.
  • the electrolysis arrangement comprises multiple stacks.
  • the electrolysis arrangement comprises 2 to 16 stacks, in particular 2, 4 or 8 stacks.
  • the stacks can also be referred to as electrolysis stacks.
  • Each of the stacks comprises several electrolysis cells.
  • Each stack has at least one stack inlet, an anode outlet and a cathode outlet.
  • the medium can be provided to the stack via the stack inlet(s).
  • the electrolysis of the medium can be performed using the electrolysis cells.
  • an anode product and a cathode product are obtained.
  • the anode product is oxygen and the cathode product is hydrogen.
  • the anode product can be extracted from the stack via the anode outlet.
  • the anode product will be mixed with the medium.
  • a mixture of the cathode product and the medium can be extracted from the stack via the cathode outlet.
  • Each of the electrolysis cells preferably comprises an anode, an anode space adjacent to the anode, a cathode and a cathode space adjacent to the cathode.
  • the cathode space is preferably separated from the anode space by a membrane and, optionally also by the anode and the cathode.
  • the anode outlet is preferably connected to the anode space.
  • the cathode outlet is preferably connected to the cathode space.
  • the membrane is preferably permeable for certain ions.
  • the membrane is preferably permeable for hydrogen ions (H + ). In that case the anode and the cathode are permeable and arranged adjacent to the membrane.
  • each stack has only one stack inlet, which is connected to the cathode space.
  • the membrane is preferably permeable for hydroxide ions (OH).
  • each of the stacks has preferably two stack inlets: a respective anode stack inlet and a respective cathode stack inlet.
  • the anode stack inlet is preferably connected to the anode space.
  • the cathode stack inlet is preferably connected to the cathode space.
  • the electrolysis arrangement further comprises an anode separator and a cathode separator.
  • the separators are configured for separating the electrolysis products from the medium.
  • the separators have a respective separator inlet, a respective separator product outlet and a respective separator medium outlet. If a mixture of the product and the medium is provided at the separator inlet, the mixture is separated within the separator such that only the majority of the medium (that is >99%) is provided at the separator medium outlet and only the majority of the product (that is >99%) is provided at the separator product outlet.
  • the medium is preferably liquid, while the products are preferably gaseous.
  • the separators are hence preferably configured as gas/liquid separators.
  • the anode separator and the cathode separator are preferably not connected to each other except for indirect connections via the separator outlets and/or via the separator inlets.
  • the anode outlets of the stacks are connected to the anode separator inlets. That is, the anode outlets of all stacks are connected to the anode separator inlets of the same anode separator.
  • there is only one cathode separator there is only one cathode separator.
  • the cathode outlets of the stacks are connected to the cathode separator inlets. That is, the cathode outlets of all stacks are connected to the cathode separator inlets of the same cathode separator.
  • the medium is driven by at least one pump unit.
  • the at least one pump unit preferably has a variable flow. That is, the flow of the medium generated by the pump unit can be controlled, for example, by controlling the rotation speed of at least one pump of the at least one pump unit. In case there are multiple pump units, it is preferred that the flows of the medium generated by the pump units can be controlled independently of each other.
  • the at least one pump unit can comprise one or more pumps. In the case of more than one pump, the pumps of a pump unit are configured such that one, some or all of the pumps of this pump unit can contribute to the flow generated by this pump unit. For example, a pump unit can have two pumps, of which one pump can be active, while the other pump is used as a backup.
  • both pumps of the pump unit can be used simultaneously to avoid that one of the pumps has to be operated at its maximum power.
  • the electrolysis arrangement can comprise multiple pump units, each comprising multiple pumps. To that end, the electrolysis arrangement can have, for example, four pumps, of which two form a first pump unit and the other two form a second pump unit.
  • a pump unit outlet is connected to all stack inlets. This does not mean that the pump unit has to be connected directly to the stack inlets.
  • a means for returning excess flow to the separators to balance the feed medium flow can be arranged in between the pump unit and the stack inlets.
  • a header is provided for separating a flow of the medium provided by the pump unit into a respective flow of for each of the stacks. That is, by means of the header the flow of the medium is distributed to the stack inlets.
  • the anode separator medium outlet and the cathode separator medium outlet are connected to a pump unit inlet. This may be via an intermediate common vessel.
  • the first embodiment can be referred to as a single feed or as a common feed because the medium is fed to the stacks via only one feed line that is distributed to the stacks.
  • each of the stacks has only one stack inlet. This is particularly preferred in the case of PEM electrolysis cells.
  • each of the stacks can have a respective anode stack inlet and a respective cathode stack inlet. This is particularly preferred in the case of alkaline electrolysis cells.
  • the anode stack inlet and the cathode stack inlet of a certain stack can be jointly connected to the header.
  • a respective header outlet assigned to the respective stack can be connected to both the anode stack inlet and the cathode stack inlet of this stack.
  • the single feed does not only fan out to the individual stacks by means of the header, but further to the anode stack inlet and the cathode stack inlet.
  • the respective control valve is arranged upstream of where a common flow assigned to this stack is divided into respective flows for the stack inlets.
  • each of the stacks has a respective anode stack inlet and a respective cathode stack inlet.
  • a pump unit outlet of a first of the pump units is connected to all anode stack inlets via a first header and a pump unit outlet of a second of the pump units is connected to all cathode stack inlets via a second header.
  • This does not mean that the pump units have to be connected directly to the stack inlets.
  • a respective means for returning excess flow to the separators to balance the feed medium flow can be arranged in between the pump unit and the respective stack inlets.
  • the first header is provided for separating a flow of the medium provided by the first pump unit into a respective flow for each of the anode stack inlets.
  • the second header is provided for separating a flow of the medium provided by the second pump unit into a respective flow for each of the cathode stack inlets. That is, by means of the first header a flow of the medium is distributed to the anode stack inlets and by means of the second header a flow of the medium is distributed to the cathode stack inlets. In this instance, and in particular for alkaline systems, a portion of the feed flows can be mixed in the separators to ensure a balance of electrolyte concentration is maintained.
  • This embodiment can also be referred to as a separate feed because the medium is fed separately to the anode stack inlets and to the cathode stack inlets.
  • the anode separator is connected to an inlet of the first pump unit, but not to the second pump unit and the cathode separator is connected to an inlet of the second pump unit, but not to the first pump unit. That is, the medium can be circulated separately in an anode circulation and a cathode circulation.
  • control valve per stack.
  • electrolysis arrangement a high degree of pressure control is possible. This is advantageous because it is desired to operate the electrolysis cells at precisely controlled pressures.
  • the membrane of the electrolysis cells is preferably largely impermeable to the medium. However, a larger pressure difference between the anode space and the cathode space can drive greater amounts of the medium through the membrane. If too much of the medium is driven through the membrane, a hydrostatic imbalance between the anode separator and the cathode separator can be the result.
  • a respective pressure difference between the anode space and the cathode space is smaller than 0.05 bar, in particular smaller than 0.02 bar.
  • the electrolysis arrangement comprises a respective control valve for each of the stacks.
  • the control valve is arranged between the header and the stack inlet of the respective stack.
  • the control valve is arranged between the stack inlet and the one header.
  • the respective control valve is arranged between the header and a point where a flow from the header is divided into separate flows for the individual stack inlets.
  • control valves are arranged between the respective stack inlet and the header to which this stack inlet is connected. It is preferred that for each stack a respective first control valve is provided between the first header and the anode stack inlet and a respective second control valve is provided between the second header and the cathode stack inlet.
  • the pump units provide a pressure that is at least 1 bar higher than the desired pressure at the stack inlets.
  • the control valves can be used to reduce the pressure.
  • the electrolysis arrangement is configured such that for all of the stacks a respective pressure drop from a first point between the header and the respective control valve to a second point within the anode separator downstream of the respective anode separator inlet has the same value within a tolerance of 0.3 bar, more preferably within 0.1 bar and/or such that for all of the stacks a respective pressure drop from a third point between the header and the respective control valve to a fourth point within the cathode separator downstream of the respective cathode separator inlet has the same value within a tolerance of 0.3 bar, more preferably within 0.1 bar.
  • the "and" case is preferred.
  • This embodiment is directed to the pressure drop across the stack with respect to the anodes and/or to the pressure drop across the stack with respect to the cathodes. This means that a comparison among the pressure drops with respect to the anodes is performed and/or that a comparison among the pressure drops with respect to the anodes is performed.
  • the pressure drop is defined between a first point and a second point.
  • a respective first point and a respective second point are defined.
  • the second point can be the same for all stacks.
  • the pressure at the respective first point is compared with the pressure at the respective second point.
  • a respective pressure difference is obtained.
  • the pressure differences of the stacks are, within a tolerance of 0.3 bar, the same for all stacks. That is, the obtained pressure difference for a certain stack differs by not more than 0.3 bar from the respective pressure difference obtained for any of the other stacks. Thereby, only the pressure drop with respect to the anodes are taken into account.
  • the first point is located between the header and the control valve.
  • headers and separate anode and cathode stack inlets this refers to the header that is connected to the anode stack inlet and to the control valve upstream of the anode stack inlet.
  • the second point is located within the anode separator downstream of the respective anode separator inlet. That means that a pressure drop caused by the anode separator inlet is taken into account in the described pressure drop the present embodiment is directed to.
  • the pressure drop is defined between a third point and a fourth point.
  • a respective third point is defined, whereas the fourth point is the same for all stacks.
  • a respective third point and a respective fourth point are defined.
  • the fourth point can be the same for all stacks.
  • the pressure at the respective third point is compared with the pressure at the respective fourth point. The comparison of the obtained pressure differences is analogous to what has been described with respect to the anodes.
  • the stacks each have a maximum rated DC power consumption in the range of 1 to 20 MW, in particular in the range of 3 to 10 MW.
  • the described electrolysis arrangement is preferably used for industrial scale electrolysis. In particular, this is to be understood in contrast to experimental setups on a laboratory scale.
  • the industrial scale is quantified in terms of the maximum rated DC power consumption of the stacks.
  • the maximum rated DC power consumption is what is commonly used to describe the electrolysis stacks. For example, a "5 MW stack" has a maximum rated DC power consumption of 5 MW.
  • the total maximum rated DC power consumption of the electrolysis arrangement is the sum of the respective maximum rated DC power consumptions of the stacks.
  • the total maximum rated DC power consumption of the electrolysis arrangement is preferably in the range of 10 to 80 MW. In particular with such a total maximum rated DC power consumption it would be inefficient to have a respective anode separator and a respective cathode separator for each of the stacks, as is the case in the prior art.
  • the at least one pump unit comprises a centrifugal pump configured to provide an adjustable flow of the medium.
  • Centrifugal pumps are particularly suitable for industrial scale electrolysis.
  • the present embodiment points out that the described electrolysis arrangement is directed to industrial scale electrolysis, and not to laboratory scale electrolysis.
  • all pump units comprise a respective centrifugal pump configured to provide a respective adjustable flow of the medium.
  • a pump unit comprises more than one pump, it is preferred that all these pumps are the pumps are centrifugal pumps.
  • all pumps of the electrolysis arrangement are centrifugal pumps.
  • one or more of the pumps can be a mechanical gear pump could be used.
  • a cooler and/or a filter are arranged between the at least one pump unit and the respective header.
  • the "and" case is preferred.
  • the cathode separator and the at least one pump unit can be shared by the multiple stacks, but also the cooler and/or the filter. This further simplifies the electrolysis arrangement and reduces costs.
  • each of the pump units a respective cooler and/or a respective filter are arranged between the pump unit and the respective header.
  • the electrolysis cells are configured as PEM electrolysis cells, anion exchange membrane electrolysis cells or alkaline electrolysis cells.
  • PEM electrolysis cells are particularly preferred.
  • the medium is water, in particular de-ionised water.
  • the medium is an aqueous solution of potassium hydroxide (KOH).
  • each of the anode separator inlets is configured as a nozzle and/or wherein each of the cathode separator inlets is configured as a nozzle.
  • the "and" case is preferred.
  • the anode separator inlets are arranged between the first points and the second point(s). That is, the anode separator inlets configured as a nozzle contribute to the pressure drops across the stack as defined between the first points and the second point(s).
  • This pressure drop can be adjusted, in particular, by adjusting the nozzles.
  • This can mean that an adjustable nozzle is used and/or that the nozzle design is adjusted. That is, the nozzle design can be used to achieve pressure drops within the above described tolerance.
  • the dominant pressure drop is delivered by the control valve and the nozzle.
  • a respective pipe length between the anode outlets and the anode separator inlets differ by less than 50 %, preferably by less than 30 % and more preferably by less than 10 %, and/or for the stacks a respective pipe length between the cathode outlets and the cathode separator inlets differ by less than 50 %, preferably by less than 30 % and more preferably by less than 10 %.
  • the "and" case is preferred.
  • the pipe length between an anode outlet and an anode separator inlet is the distance between the anode outlet and the anode separator inlet measured along a pipe that connects the anode outlet and the anode separator inlet.
  • the anode separator is arranged horizontally and/or the cathode separator is arranged horizontally.
  • the "and" case is preferred.
  • the electrolysis arrangement further comprises a bypass from a point between the at least one pump unit and the respective header to the anode separator and/or to the cathode separator.
  • the "and" case is preferred.
  • the bypass preferably extends from a point between the pump unit and the header and, via a first outlet branch, to the anode separator and, via a second outlet branch, to the cathode separator.
  • the bypass preferably has a respective inlet branch for each of the pump units, wherein each of the inlet branches begins between the pump unit and the respective header. Also in this case the bypass preferably terminates at the anode separator via a first outlet branch and at the cathode separator via a second outlet branch.
  • the medium can flow from the pump unit outlet to the pump unit inlet without passing the stacks.
  • the pump unit(s) can generate a flow that is higher than required.
  • the bypass comprises a bypass valve.
  • the flow through the bypass and, in consequence, through the stacks can be adjusted particularly quickly, in particular compared to adjusting the rotation speed of one or more pumps of the pump unit.
  • the flow control is particularly fast.
  • the anode separator and the cathode separator are preferably connected to each other only via the separator outlets, the separator inlets and/or via the bypass.
  • the bypass can be used to balance the medium level in the anode separator and the cathode separator.
  • a method for performing an electrolysis of a medium in order to obtain an anode product and a cathode product using an electrolysis arrangement as described comprises driving the medium by means of the at least one pump unit and applying a voltage to the electrolysis cells, wherein the speed of at least one pump of the at least one pump unit and the settings of the control valves are controlled.
  • the advantages and features of the electrolysis arrangement are transferrable to the method, and vice versa.
  • the electrolysis arrangement is preferably configured to be used according to the method.
  • the voltage is applied such that the anode product and the cathode product are obtained from the medium by electrolysis.
  • the at least one pump unit and/or the control valves are controlled such that the at least one pump unit provides the medium with a pressure that is at least 0.4 bar higher than the pressure at each of the stack inlets.
  • the "and" case is preferred.
  • the at least one pump unit is controlled based on a total flow demand.
  • the load of the at least one pump unit is preferably not controlled based on an amount of the anode product or of the cathode product that are supposed to be produced.
  • the load of the at least one pump unit is preferably not controlled based on an amount of hydrogen that is supposed to be produced.
  • the load of the at least one pump unit is controlled based on the total flow demand.
  • the total flow demand is the sum of the respective flow demands of the stacks and, optionally, of a bypass flow.
  • the flow demand of a stack can be determined based on an inherent age of the stack, a power factor of the stack and/or a harmonic distortion limit of the stack.
  • the inherent age of a stack is a measure that can be seen, for example in the case of hydrogen production, from the power demand for a given amount of hydrogen that is supposed to be obtained. In determining the total flow demand it is preferably taken into account which of the stacks are in operation.
  • control valves are controlled based on at least three of these eight parameters. More preferably, all parameters are used.
  • the amount of the anode product that is supposed to be obtained and the amount of the cathode product that is supposed to be obtained describe a production request that may be issued by a control system.
  • the difference of the temperature of the medium at the anode outlet and the cathode outlet is preferably in the range of 10 and 15 °C.
  • the maximum temperature of the medium at the anode outlet can also be considered the maximum outlet temperature of the stack. This parameter is an operating constraint. Providing a predetermined minimum flow can ensure efficient stack operation for a given production rate. A predetermined maximum flow can be provided to ensure that the stacks are not damaged.
  • a pressure of the medium at the stack inlets is within the range of 5 to 50 bar.
  • the electrolysis is preferably a high pressure electrolysis. In the present embodiment this is quantified in terms of the pressure at the stack inlets.
  • Fig. 1 shows an electrolysis arrangement 1 that comprises multiple stacks 3 of electrolysis cells.
  • the electrolysis cells may be configured as PEM electrolysis cells, anion exchange membrane electrolysis cells or alkaline electrolysis cells.
  • the stacks 3 each have a maximum rated DC power consumption in the range of 1 to 20 MW.
  • the electrolysis arrangement 1 comprises a pump unit 2 for driving a medium.
  • the pump unit 2 comprises a single pump only.
  • the pump unit 2 comprises a centrifugal pump configured to provide an adjustable flow of the medium.
  • Each stack 3 comprises two stack inlets 4a,4b that are connected to the pump unit 2 via a header 5 for separating a flow of the medium provided by the pump unit 2 into a respective flow for each of the stacks 3.
  • a cooler 21 and a filter 22 are arranged between the pump unit 2 and the header 5 .
  • each stack 3 comprises a respective anode outlet 6 and a respective cathode outlet 7.
  • the stacks 3 are configured to obtain by electrolysis of the medium introduced into the respective stack inlets 4a,4b an anode product provided together with the medium at the respective anode outlet 6 and a cathode product provided together with the medium at the respective cathode outlet 7.
  • the electrolysis arrangement 1 comprises a respective control valve 8 for each of the stacks 3 arranged between the header 5 and the respective stack inlets 4a,4b, wherein the control valves 8 are configured to individually control a flow of the medium into the respective stack 3.
  • the control valves 8 are configured to individually control a flow of the medium into the respective stack 3.
  • the electrolysis arrangement 1 further comprises an anode separator 9 having an anode separator medium outlet 12 that is connected to the pump unit 2.
  • Each of the anode outlets 6 of the stacks 3 is connected to a respective anode separator inlet 10 of the anode separator 9.
  • the anode separator 9 is configured to separate the anode product from the medium introduced into the anode separator inlets 10 such that the anode product is provided at an anode separator product outlet 11 and the medium is provided at the anode separator medium outlet 12.
  • the pressure of the anode separator 9 is controlled by a control valve 25.
  • the electrolysis arrangement 1 further comprises a cathode separator 13 having a cathode separator medium outlet 16 that is connected to the pump unit 2.
  • Each of the cathode outlets 7 of the stacks 3 is connected to a respective cathode separator inlet 14 of the cathode separator 13.
  • the cathode separator 13 is configured to separate the cathode product from the medium introduced into the cathode separator inlets 14 such that the cathode product is provided at a cathode separator product outlet 15 and the medium is provided at the cathode separator medium outlet 16.
  • the pressure of the cathode separator 13 is controlled by a control valve 26. The operation of the control valves 25 and 26 are such that the pressure difference is minimized between the two separators 9,13.
  • the anode separator 9 and the cathode separator 13 are arranged horizontally. In particular thereby it is possible that a respective pipe length between the anode outlets 6 and the anode separator inlets 10 for the stacks 3 differ by less than 50 % and that a respective pipe length between the cathode outlets 7 and the cathode separator inlets 14 for the stacks 3 differ by less than 50 %.
  • Each of the anode separator inlets 10 is configured as a nozzle and each of the cathode separator inlets 14 is configured as a nozzle.
  • the electrolysis arrangement 1 is configured such that for all of the stacks 3 a respective pressure drop from a first point 17 between the header 5 and the respective control valve 8 to a second point 18 within the anode separator 9 downstream of the respective anode separator inlet 10 has the same value within a tolerance of 0.3 bar and such that for all of the stacks 3 a respective pressure drop from a third point 19 between the header 5 and the respective control valve 8 to a fourth point 20 within the cathode separator 13 downstream of the respective cathode separator inlet 14 has the same value within a tolerance of 0.3 bar.
  • the first point 17 and the third point 19 are the same.
  • the electrolysis arrangement 1 further comprises a bypass 23 from a point between the pump unit 2 and the header 5 to the anode separator 9 and to the cathode separator 13.
  • Fig. 2 shows a further embodiment of an electrolysis arrangement 1.
  • the embodiment of Fig. 2 can be referred to as a separate feed.
  • each of the pump units 2 have a single pump.
  • the pump units 2 each comprise a respective centrifugal pump configured to provide a respective adjustable flow of the medium.
  • Each stack 3 comprises two stack inlets 4a,4b.
  • a respective anode stack inlet 4a is connected to one of the pump units 2 via a header 5, while a respective cathode stack inlet 4b is connected to the other pump unit 2 via a further header 5.
  • a respective cooler 21 and respective filter 22 are arranged between each of the pump units 2 and the respective header 5 .
  • the electrolysis arrangement 1 comprises two respective control valves 8 for each of the stacks 3. For each stack 3, one control valve 8 is arranged between the anode stack inlet 4a and the header 5 connected thereto and one control valve 8 is arranged between the cathode stack inlet 4b and the header 5 connected thereto.
  • the control valves 8 are configured to individually control a flow of the medium into the respective stack inlets 4a,4b.
  • the need to minimize the pressure difference between the inlet 4a and 4b may require a minor additional flow control on one of the two streams downstream of one of the two valve 8.
  • the electrolysis arrangement 1 further comprises an anode separator 9 having an anode separator medium outlet 12 that is connected to each of the pump units 2. Also, the electrolysis arrangement 1 comprises a cathode separator 13 having a cathode separator medium outlet 16 that is connected to each of the pump units 2.
  • the electrolysis arrangement 1 is configured such that for all of the stacks 3 a respective pressure drop from a first point 17 between the header 5 and the respective control valve 8 assigned to the anode stack inlet 4a to a second point 18 within the anode separator 9 downstream of the respective anode separator inlet 10 has the same value within a tolerance of 0.3 bar and such that for all of the stacks 3 a respective pressure drop from a third point 19 between the header 5 and the respective control valve 8 assigned to the cathode stack inlet 4b to a fourth point 20 within the cathode separator 13 downstream of the respective cathode separator inlet 14 has the same value within a tolerance of 0.3 bar.
  • the first points 17 and the third points 19 are not the same.
  • An electrolysis arrangement 1 that comprises:
  • control valves 8 assigned to each of the stacks 3 an independent flow control can be achieved for the stacks 3. This allows safe and reliable operation of the electrolysis arrangement 1 although multiple stacks 3 are connected to the same anode separator 9 and to the same cathode separator 13.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Organic Chemistry (AREA)
  • Electrochemistry (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Inorganic Chemistry (AREA)
  • Automation & Control Theory (AREA)
  • Analytical Chemistry (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Sustainable Development (AREA)
  • Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
EP20207789.7A 2020-11-16 2020-11-16 Agencement et procédé d'électrolyse Pending EP4001463A1 (fr)

Priority Applications (3)

Application Number Priority Date Filing Date Title
EP20207789.7A EP4001463A1 (fr) 2020-11-16 2020-11-16 Agencement et procédé d'électrolyse
AU2021258014A AU2021258014A1 (en) 2020-11-16 2021-10-28 Electrolysis arrangement and method
CN202111329878.6A CN114507871A (zh) 2020-11-16 2021-11-10 电解装置及方法

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
EP20207789.7A EP4001463A1 (fr) 2020-11-16 2020-11-16 Agencement et procédé d'électrolyse

Publications (1)

Publication Number Publication Date
EP4001463A1 true EP4001463A1 (fr) 2022-05-25

Family

ID=73452067

Family Applications (1)

Application Number Title Priority Date Filing Date
EP20207789.7A Pending EP4001463A1 (fr) 2020-11-16 2020-11-16 Agencement et procédé d'électrolyse

Country Status (3)

Country Link
EP (1) EP4001463A1 (fr)
CN (1) CN114507871A (fr)
AU (1) AU2021258014A1 (fr)

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20050121315A1 (en) * 2003-12-05 2005-06-09 Baltrucki Justin D. System for generating hydrogen and method thereof

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20050121315A1 (en) * 2003-12-05 2005-06-09 Baltrucki Justin D. System for generating hydrogen and method thereof

Also Published As

Publication number Publication date
AU2021258014A1 (en) 2022-06-02
CN114507871A (zh) 2022-05-17

Similar Documents

Publication Publication Date Title
JP6826699B2 (ja) ガス製造装置及びガス製造方法
EP2108199B1 (fr) Contrôle de la pression de combustible mixte pour une pile à combustible
EP3017089B1 (fr) Système à hydrogène et procédé de fonctionnement
EP4086370A2 (fr) Systèmes d'électrolyseur à oxyde solide contenant une pompe à hydrogène et procédé de fonctionnement associé
US20220397118A1 (en) Process and apparatus for compressing hydrogen gas in a hybrid compression system
JP7363419B2 (ja) 水電解システム
WO2005112177A2 (fr) Mecanisme de recyclage de combustible minimal a rendement maximal pour pile a combustible
AU2014310784A1 (en) Method for operating a fuel cell stack, fuel cell stack and fuel cell system
US4879189A (en) Fuel cell air pressurization system and method
CA3162566C (fr) Methode et appareil pour comprimer un flux de gaz a debit variable
TW202405246A (zh) 用於soec系統之大氣操作的壓縮器整合及安全操作啟動
EP4001463A1 (fr) Agencement et procédé d'électrolyse
JP2019123899A (ja) 水電解システム
EP4001464A1 (fr) Séparateur pour un agencement d'électrolyse
EP4242350A1 (fr) Extensibilité modulaire d'estampillage et de compression de soec
EP4059889A2 (fr) Procédé et appareil de dosage d'hydrogène dans un système de compression centrifuge
AU2022203965B2 (en) Process and apparatus for operating a compression system
CN116732574A (zh) 电解冲头中的独立产生器模块产物管线的隔离和可维护性
EP4001465A1 (fr) Agencement et procédé d'électrolyse
AU2021279136B2 (en) Electrolytic cell, method for operating a cell of this type and electrolyser
CN115513494A (zh) 一种燃料电池氢空压力自动跟随的控制系统
JP2024510000A (ja) Ｍｅｃシステム
JP2006024484A (ja) 燃料電池及びその運転方法
EP4071276A1 (fr) Agencement d'électrolyse pour une électrolyse alcaline
CN117070963A (zh) 一种水电解制氢系统中控制气体纯度的装置及系统和方法

Legal Events

Date Code Title Description
PUAI Public reference made under article 153(3) epc to a published international application that has entered the european phase

Free format text: ORIGINAL CODE: 0009012

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: THE APPLICATION HAS BEEN PUBLISHED

AK Designated contracting states

Kind code of ref document: A1

Designated state(s): AL AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO PL PT RO RS SE SI SK SM TR

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: REQUEST FOR EXAMINATION WAS MADE

17P Request for examination filed

Effective date: 20220810

RBV Designated contracting states (corrected)

Designated state(s): AL AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO PL PT RO RS SE SI SK SM TR

RAP3 Party data changed (applicant data changed or rights of an application transferred)

Owner name: L'AIR LIQUIDE, SOCIETE ANONYME POUR L'ETUDE ET L'EXPLOITATION DES PROCEDES GEORGES CLAUDE