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    • 专利摘要:
    The invention relates to a large-scale hydrogen refueling station comprising a plurality of supply storage, compressor modules comprising a local controller, dispenser modules comprising a dispenser controller, and a hydrogen production system comprising a hydrogen production system controller mutually connected by one or more flow paths. Wherein one of the controllers facilitates control of valves and thereby flow of hydrogen gas in the flow paths between one or more of the plurality of supply storages, compressor modules, dispenser modules and hydrogen production system. Wherein the control of the valves enables flow of hydrogen gas in at least three of the flow paths simultaneously.
    公开号:DK201970036A1
    申请号:DKP201970036
    申请日:2019-01-18
    公开日:2020-08-21
    发明作者:Due Sinding Claus；Christian Francois Charbonneau Thomas
    申请人:Nel Hydrogen As；
    IPC主号:
    专利说明:

    [0001] [0001] The invention relates to a large-scale hydrogen refueling station comprising a plurality of supply storage, compressor modules comprising a local controller, dispenser modules comprising a dispenser controller, and a hydrogen production system comprising a hydrogen production system controller mutually connected by — one or more flow paths. Wherein one of the controllers facilitates control of valves and thereby flow of hydrogen gas in the flow paths between one or more of the plurality of supply storages, compressor modules, dispenser modules and hydrogen production system. Wherein the control of the valves enables flow of hydrogen gas in at least three of the flow paths simultaneously.
    [0002] [0002] According to an embodiment of the invention the large-scale hydrogen refueling station comprises at least three supply storages, at least three compressor modules and at least three dispenser modules.
    [0052] [0052] This is advantages in that it has the effect, that it is possible to perform a refueling of a vehicle vessel and perform pressure consolidation during the same period of time ie. simultaneously. In fact, several vehicles can be refueled simultaneously with pressure consolidation of several vessels of the supply storages and hydrogen production.
    [0003] [0003] According to an embodiment of the invention, the compressor of the compressor module is a variable speed compressor.
    [0053] [0053] This is advantages in that it has the effect, that it is possible to reduce the capacity of the compressor and thereby the power consumption leading to a reduced — cost of operation of the compressor.
    [0004] [0004] According to an embodiment of the invention, the valves are controlled to establish: an inlet flow path between at least one supply storage and at least one compressor module, an outlet flow path between at least one compressor module and at least one dispenser module, a consolidation flow path between at least one compressor module and at least one supply storage, a dispense flow path between at least one supply storage and at least one dispenser module. Wherein the dispenser controller is controlling the valves so as to facilitate flow of gas in at least three of inlet flow path, outlet flow path, consolidation flow path or dispense flow path simultaneously.
    [0005] [0005] According to an embodiment of the invention, the valves are controlled to establish a first supply flow path between the hydrogen production system and at least one supply storage, and / or a second supply flow path between the hydrogen production system and at least on compressor module. Wherein the hydrogen production system controller is controlling the valves so as to facilitate flow of gas in — the first supply flow path or second supply flow path simultaneously with flow of gas in at least one of the inlet flow path, outlet flow path, consolidation flow path or dispense flow path.
    [0006] [0006] According to an embodiment of the invention, at least one of the supply storages is predefined as low-pressure storage and at least two of the supply storages — are predefined as medium-pressure storages,
    [0054] [0054] This is advantageous in that it has the effect, that it is possible to consolidate pressure in one vessel of a supply storage at the same time as another vessel of the same supply storage is used as gas source for a refueling.
    [0055] [0055] This is further advantageous in that it has the effect, that the hydrogen production system may supply low pressure hydrogen to a “buffer storage” which when a compressor has time and / or need for medium or high-pressure gas is present and / or energy price is as desired can consolidate this low-pressure gas into medium — pressure gas storage.
    [0007] [0007] According to an embodiment of the invention, the low pressure is defined as being in the range of 0 bar — 250 bar and the medium pressure is defined as being in the range of 150 bar — 200 bar, wherein the predefined medium pressure is always equal to or higher than the predefined low pressure.
    [0008] [0008] According to an embodiment of the invention, the central controller is controlling the valves so that a first inlet flow path is connecting a first supply storage to a first compressor module, a first outlet flow path is connecting the first compressor module to a first dispenser module, a second inlet flow path is connecting a second supply storage and a compressor module and a first consolidation flow path is connecting the second compressor module to a third supply storage.
    [0056] [0056] This is advantageous in that it has the effect, that flow of gas is established in four flow paths at the same time. The second supply storage is preferably the low- pressure storage. One vessel of the third supply storage may be used as gas source for a refueling at the same time as a second vessel of the third supply storage may be used — as gas receiver in a consolidation process.
    [0009] [0009] According to an embodiment of the invention, one of the plurality of supply storages is defined as a low-pressure supply storage and wherein the first supply flow path is only connecting the hydrogen production system and the low-pressure supply storage.
    [0057] [0057] Having one supply storage defined as a low-pressure storage connected to the hydrogen production system is advantages in that it can be used as buffer for the production. Further, it is advantageous in that the requirements to e.g. compressor of the hydrogen production system can be reduced. The low-pressure supply is used as supply for the medium pressure storage or compressor modules.
    [0010] [0010] According to an embodiment of the invention a first supply storage vessel of a supply storage serves as gas input to one inlet flow path to a first compressor module simultaneously with a second vessel of the supply storage serving as gas receiver of a consolidation flow path from a second compressor module.
    [0058] [0058] This is advantageous in that it has the effect, that it adds flexibility to the system to be able to refuel from one vessel and consolidate pressure in another vessel of the same supply storage.
    [0011] [0011] According to an embodiment of the invention, the hydrogen production system is producing hydrogen when the pressure in the at least one supply storage vessel is below a plant pressure threshold.
    [0059] [0059] This is advantageous in that it has the effect of ensuring sufficient pressure to comply with expected refueling demands. It is an aim of the present invention to always be able to initiate a refueling with maximum pressure in the supply storage.
    [0012] [0012] According to an embodiment of the invention, the hydrogen production system is production hydrogen when the energy price is below an energy price threshold value if the pressure in all supply storage vessels is above a plant pressure threshold.
    [0060] [0060] This is advantageous in that it has the effect, that when there is sufficient pressure / hydrogen in the supply storages, then operation costs are reduced. In this — situation hydrogen is only produced when cost of energy available on the utility grid supplying the hydrogen production system is below a predefined energy price threshold.
    [0061] [0061] The energy price threshold is determined based on local energy price level and can be adjusted over time as the energy prices changes. The plant pressure threshold is a measure of how full the supply storages are i.e. if the total capacity in the supply storages are empty, the plant pressure is 50% hence if the plant pressure threshold is 50%, then production of hydrogen will be initiated disregarding energy prices if the plant pressure drops to 49%.
    [0013] [0013] According to an embodiment of the invention, a first part of a refueling is made directly from one of the supply storages and a second part of the refueling is made via a compressor module. Wherein the shift between the first and the second part is made when the flow in the dispense flow path is estimated to be lower than the flow 5 generated by the compressor module in the output flow path.
    [0062] [0062] This is advantageous in that it has the effect that the refueling is made as fast as possible. The flow generated in the dispense flow path due to the pressure difference between the pressure in the vehicle vessel and the pressure in the supply storage is higher than the flow generated by the compressor.
    [0014] [0014] According to an embodiment of the invention, a main controller facilitating broadcasting a control reference of the list comprising: related to energy consumption, related to maintenance, related to pressure consolidation to the dispenser controller and / or local controller.
    [0015] [0015] Moreover, the invention relates to a method of refueling a vehicle vessel from a large-scale refueling station comprising a plurality of supply storage, compressor modules comprising a local controller, dispenser modules comprising a dispenser controller and a hydrogen production system comprising a hydrogen production system controller mutually connected by one or more flow paths. The method comprising the following steps: connecting the vehicle vessel to a dispenser module, starting the refueling from a user interface, preferably on a dispenser module, initiating flow of hydrogen gas from a supply storage via a dispense flow path during a first part of the refueling, continuing the flow of hydrogen via a compressor module during second part of the refueling, and disconnecting the dispenser module from the vehicle vessel when a target pressure is reached. Wherein the refueling is initiated by a user — who activates a dispenser controller, the dispenser controller change status of one or more valves to facilitate flow of gas via a dispense flow path during a first part of the refueling and activates the local controller of the compressor module and change status of one or more valves to facilitate flow of gas via an outlet flow path during a second part of the refueling.
    [0016] [0016] According to an embodiment of the invention, a first compressor module is used and simultaneously a second compressor is used for pressure consolidation between vessels of one or two of the supply storages.
    [0017] [0017] According to an embodiment of the invention, simultaneously a third compressor module is used for moving pressure from a low-pressure storage connected to the hydrogen production system to a medium or high pressure supply storage or to a vehicle vessel.
    [0063] [0063] Vehicle should preferably be understood as a heavy-duty vehicle but could be any type of vehicle. Further, vehicle is a fuel cell vehicle.
    [0064] [0064] The user interface could be a simple device communicating with e.g. a portable device such as a smartphone. in this way most of the user interface is on the smartphone which is communicating with the dispenser or compressor module or main controller to initiate the refueling.
    [0065] [0065] The continuing of the refueling via the compressor module may be at — reduced speed of the compressor and from the same or another supply storage.
    [0066] [0066] The target pressure may alternatively be a target state of charge.
    [0067] [0067] The first, second and third compressor modules are able to be used in any of the mentioned refueling, consolidation and moving of gas processes. This is advantageous in that it has the effect, that the large scale refueling station is able to be — operated in a flexible manner and thereby always be ready for a high frequency of refuelings at a low operation cost.
    [0018] [0018] Moreover, the invention relates to the use of a large-scale refueling station according to any of the claims 1-14 and controlled according to the method of any of the claims 15-17.
    [0019] [0019] For a more complete understanding of this disclosure, reference is now made to the following brief description, taken in connection with the accompanying drawings and detailed description, wherein like reference numerals represent like parts: Figure 1 illustrates an overall view of the large-scale refueling station, and Figure 2-4 illustrates configuration of gas flow paths according to first, second and third main control strategy. Detailed description
    [0020] [0020] Figure 1 illustrates an embodiment of the invention, a large-scale hydrogen refueling station mainly for refueling of heavy duty vehicle, with four hydrogen supply storages la-1n, four compressor modules 2a-2n and four dispensers 3a-3n. It should be noted, that there do not have to be a 1:1:1 relationship between the number of supply storages 1, compressors 2 and dispensers 3 as illustrated in figure 1. In addition, figure 1 illustrates a hydrogen production system 15. Note that more valves than illustrated may be included to obtain the total number of combination of connections (flow paths) between the modules.
    [0021] [0021] A supply storage 1 typically comprises a plurality of vessels 13 but may be implemented as one single vessel. The vessels 13 are typically Type 1 vessels designed to holding a gas at a pressure of at least 200bar. Typically, the supply storages are stationary. In a preferred embodiment, at least one supply storage is defined as a low- pressure storage and the rest as medium pressure storage. In an embodiment, the low- pressure region is defined as a range between 0 and 200bar whereas the medium pressure region is defined as a range between 200 and 500bar. These ranges can be — change from site to site and should therefore only serve as examples and not limitations in the present invention. Further, high pressure storages may also be used where hydrogen gas is stored at pressures above 500bar.
    [0022] [0022] According to a specific embodiment, the hydrogen production system 15 is designed to deliver hydrogen at a pressure of 200 bar. If compressor capacity is available this 200bar hydrogen could be delivered to any of the supply storages 1. However, this cannot be guaranteed and therefore in this embodiment a low-pressure — supply storage is defined for sole or at least main storage of hydrogen gas from the production system 15. Here the hydrogen is stored until compressor capacity is available for consolidating it in other storages 1 or supply directly to a vehicle.
    [0023] [0023] It should be mentioned that in addition to the hydrogen production system 15, a movable supply preferably in the form of a truck trailer may be connected to one or more of the supply storages 1. This is especially relevant in situations where the hydrogen production system 15 is not producing in its full capacity or being maintained.
    [0024] [0024] The consolidation is made to what in this specific embodiment is defined as medium pressure storage at a pressure of 500bar. The 500bar limit is defined based on a calculation of the price of storing an amount of hydrogen at a given pressure. It may be even factor three more expensive to store gas at 1000bar (example of high pressure) compared to storage at 500bar (example of medium pressure). With this said the pressure in the vessels 13 of the supply storages 1 may be increased up to maybe 1000bar if this is required to comply with refueling demands which has the highest priority in the operation of the large-scale refuelings station.
    [0025] [0025] A compressor module 2 typically comprises elements including compressor, cooling system, etc. all locally controlled by a local controller 4. The local controller 4 is an autonomous controller controlling the compressor module elements to ensure a desired pressure, temperature, flow, etc. of the gas leaving the compressor module 2 via the outlet flow path 8 or consolidation flow path 9. The local controller 4 may control the compressor module in response to setpoint or operation values received from / determined from a central controller 5.
    [0026] [0026] Preferably the compressor 17 is a variable speed compressor meaning that the speed of the diaphragm / piston of the compressor can vary. This is leading to a more
    [0027] [0027] On the output (outlet flow path 8) from the compressor 2 the pressure of hydrogen may vary from O bar to desired pressure in vehicle vessel 14 at the end of — the refueling, which typically is between 350 and 900 bar. Typically, the pressure in the outlet flow path 8 is higher than the minimum pressure in the supply storage 1 defined as medium pressure storages i.e. above 150 — 200 bar, but preferably (with reference to the example above) above the 500bar. Accordingly, the pressure in the outlet flow path 8 is defined as high pressure during a refueling.
    [0028] [0028] A dispenser 3 typically comprises a user interface via which a user can communicate with one or more of the local controllers 4 either directly or via the central controller 5. As a result of the communication, the user is allowed to refuel a vehicle tank with a gaseous fuel, preferably hydrogen. Further, the dispenser 3 also comprise a dispenser controller 18, hose 20 and nozzle for connecting to the vehicle tank 14 and thereby allowing flow of hydrogen gas into the vehicle vessel 14. The dispenser controller 18 is preferably controlling a dispenser cooling system 19.
    [0029] [0029] The dispenser cooling system 19 may be located inside or outside the physical dispenser and main purpose hereof is to ensure correct temperature of the hydrogen gas prior to entering the vehicle vessel. Such temperature adjustment may be necessary — duetoa increase caused e.g. by valves including pressure at pressure regulating valves, pipes reaching ambient temperature, etc.
    [0030] [0030] The dispenser controller 18 is preferably controlling the refueling according to a cascade like refueling strategy where the vessel 13 with the lowest pressure of the supply storages 1 (preferably of the medium pressure storages) are used as first gas
    [0031] [0031] In one embodiment of the invention, the refueling is controlled by the dispenser controller 18, but it may also be controlled by the local controller 4 of the compressor module 2 or the main controller 5.
    [0032] [0032] A hydrogen production system 15 is preferably implemented as an electrolyser in the form of an Alkaline or a PEM electrolyser or a combination hereof. — In addition to the electrolyser part, the hydrogen production system 15 also comprise compressors, storage vessels, etc. This enables the hydrogen production system to output hydrogen gas with a pressure defined in the so-called low-pressure region which in this application is defined as a pressure between 0 and 200 bar. It should be mentioned that this definition may vary from site to site and between station / — electrolyser OEMs and should thus not be limiting to the scope of the invention. The hydrogen may also be produced by other systems e.g. from natural gas. The hydrogen production is controlled by a hydrogen production system controller 16 in response to setpoint or operation values received from / determined by the central controller 5. Alternative, predefined threshold values are used by the controller 16 to control when — the production should be initiated or stopped. Such threshold values may be pressure in the low-pressure storage, energy price, or the like.
    [0033] [0033] Hence in a preferred embodiment of the present invention, the hydrogen production system 15 delivers 200bar hydrogen gas to the supply storages 1 defined as low pressure storage when the pressure in vessels hereof is below a threshold value. Alternatively, the produced hydrogen gas is delivered directly to the compressor modules 2 or dispenser module 3.
    [0034] [0034] With reference to figure 1 the compressor modules 2 and the dispensers 3 are located downstream the supply storages 1. The dispenser module 3 is located downstream the compressor module 2. Hence, there is a fluid communication channel
    [0035] [0035] The hydrogen production system 15 is via a first supply flow path 11 supplying hydrogen to at least one supply storages defined as a low-pressure supply storage (on figure 1 denoted In). When the pressure threshold is reached (or before) pressure equalisation is obtained between the hydrogen production system 15 and the low-pressure supply storage In, the valve 6-15.1 is closed and the production is stopped. The production of hydrogen may be continued when the first supply flow path 11 1s closed, if the gas can be transferred to one of the compressor modules 2 via the second supply flow path 12. The receiving compressor module 2 is then increasing the pressure of the gas received and via a consolidation flow path 9 delivering the pressurised gas to one of the medium pressure storages 1.
    [0036] [0036] The flow of gas in the in the flow paths 7, 8, 9, 10, 11, 12 is controlled by valves 6. Valves of the inlet flow path are denoted 6-7, valves of the outlet flow path are denoted 6-8, valves of the consolidation flow path are denoted 6-9, valves of the dispense flow path are denoted 6-10, valves in the first supply flow path are denoted 6-11 and valves in the second supply flow path are denoted 6-12. The position of the valves is controlled by the central controller 5, local controller 4 or dispenser controller
    [0037] [0037] It should be mentioned, that valves (denoted 6-1) controlling flow from — vessels 13 inside the supply storages 1 may also be controlled by the central controller
    [0038] [0038] Preferably the valves 6 are pneumatic valves and therefore as far as possible located as close to the compressor modules 2 as possible in that here compressed air is available. Therefore, the compressor modules 2 preferably comprises valve panels at least with valves 6-1 controlling flow between vessels 13 of the supply storages 1.
    [0039] [0039] The embodiment illustrated in figure 1 illustrates the highest degree of — flexibility that can be added to the large-scale refueling station of the present invention, namely that all supply storages 1 is connected to all compressor modules 2 and all dispenser modules 3. Hence, the embodiment illustrated in figure 1 facilitates flow of gas in the large-scale refueling station between any combination of these modules. However, less flexible configurations are still within the scope of the invention. An — example could be an individual supply storage 1 may be dedicated as supply storage to one dispenser 3 via one dedicated compressor module 2. Another example is the lower pressure storage In which in an embodiment is the only supply storage having a flow path to the hydrogen production system 15. Hence, any configuration of flow paths 7-12 between supply storage 1, compressor module 2, dispenser 3 and hydrogen — production system 15 is in theory possible to implement within the scope of the present invention.
    [0040] [0040] The choice of configuration (i.e. which supply storage is supplying which dispenser module) may be decided by a control strategy which can be based on a predetermined priority given to each of the modules (“modules” may be used as common reference to supply storage 1, compressor module 2, dispenser module 3 and hydrogen production system 15). Based here on a preferred configuration is automatically chosen according to the priority and if the preferred configuration is not possible e.g. because the first priority compressor is busy, the second priority compressor is used instead.
    [0041] [0041] The choice of configuration may also be determined from a random control strategy or based on a strategy takin into account previous use to ensure that each individual supply storage is filled / emptied the same number of times, each individual compressor is running the same number of hours, etc. e.g. leading to an equal wear of e.g compressor modules, energy price, etc.
    [0042] [0042] The fact, that the large-scale refueling station comprises a plurality of identical (at least functional) modules make it possible to load the modules so that e.g. the compressors need maintenance at the same time or at different times depending on maintenance strategy.
    [0043] [0043] The large-scale refueling station and thereby the compressor modules are controlled according to at least three main control strategies. The first control strategy is a refueling strategy aiming at filling a vessel 14 of a vehicle as fast as possible which is described with reference to figure 2, the second is to consolidate the pressure in one or more of the vessels 13 of the supply storage 1 which is disclosed with reference to — figure 3 and the third is to consolidate pressure of / move gas from the low pressure storages produced by the hydrogen production system 15 to medium pressure supply storages 1 which is disclosed with reference to figure 4. The control strategies are described with reference to figure 2, 3 and 4 only with the valves 6 illustrated on figure I needed to explain the control strategies.
    [0044] [0044] A refueling of a vehicle vessel 14a initiated by a user of dispenser module 3a is according to figure 2, established during a first period of time, from the dispense flow path 10a between supply storage la and dispenser 3a. The dispense flow path 10a is opened for gas flow by opening one or more of the valves 6-1a1, 6-1a2, 6-1a3 and open valve 6-10a while keeping valve 6-7a closed.
    [0045] [0045] The duration of the first period of time is determined by the difference in pressure in the vessels 13 of supply storage 1a and the vehicle vessel 14a. If there is a huge pressure difference the period of time is longer than if there is a minor pressure difference. The first period may end when pressure equalisation is obtained, there is a predefined pressure difference or preferably just before the flow in the dispense flow
    [0046] [0046] More specific the refueling made during the first part / time follows the following principle. The vessel 13 of any of the supply storages 1 having a pressure above the pressure of the vehicle vessel 14a is first pressure equalised with the vehicle vessel 14a. The pressure equalisation is made between the vehicle vessel 14a and the vessel 13 of any of the supply storages 1 having the lowest pressure above this new vehicle vessel pressure. This principle is followed until pressure equalisation is has been made between the vessel 13 of any of the supply storages 1 having the highest pressure and the vehicle vessel 14a. It should be noted, that this principle can include vessels 13 which is not in used for other refuelings or consolidation. Further, if the refueling has to be made faster, cheaper, more efficient or the like, some of the bank / vessel shifts may not be made i.e. if higher jump between pressures may be desired.
    [0047] [0047] After this, no refueling is made solely based on pressure differentiation in vessels 13, 14a. Therefore, during a second period of time of the refueling, the valve 6-10a is closed while valves 6-7a and 6-8a are opened. Thereby gas flow is allowed in the inlet flow path 7a to the compressor module 2a from the supply storage la and the outlet flow path 8a from the compressor module 2a to the dispenser 3a. During this second part of the refueling, the compressor in module 2a is increasing the inlet pressure (gas pressure in the supply storage la / inlet flow path) to a desired outlet pressure ending at a target pressure in the vehicle vessel 14a. When this target pressure
    [0048] [0048] It should be noted, that additional not described steps / elements of a refueling such as determining start pressure in the vehicle vessel 14a prior to initiate refueling, cooling of gas in the compressor or dispenser module 2, 3, venting hose / nozzle after end refueling, leakage check, etc. may also be part of a refueling.
    [0049] [0049] At the same time as the vehicle vessel 14a is refueled as described above, from dispenser module 3a, dispenser module 3c is used for a refueling of vehicle vessel 14b. Since a refueling is ongoing from a vessel in supply storage la, compressor module 2a and dispenser module 3a, the dispenser controller 18b is determining if the pressure of any of the vessels of the remaining supply storages 1b-1n is sufficiently high above the pressure of gas in vehicle vessel 14b. If not, the refueling is initiated via one of the compressor modules 2b-2n. However, in this example the pressure of gas in vessel 13 of supply storage 1c is high enough to facilitate a first part refueling — via the dispense flow path 10c bypassing the compressor modules 2. Therefore, the dispenser controller is opening the valve 6-10c to facilitate pressure equalisation between the vessel 13 of supply storage 1c and vehicle vessel 14b. Following the above principle, when the pressure in the vessel 13 of supply storage 1c and in the vehicle vessel 14b is within a determined range, pressure equalisation between another vessel — 13 of another (not in use) vessel 13 of the same 1c or another supply storage and the vehicle vessel 14b is initiated. As above, after refueling by pressure consolidation, the refueling switch to filling via a compressor module 2. In this example, the compressor module 2c is used with inlet flow path 7b from supply storage 1b and outlet flow path 8c to dispenser 3c. This configuration is determined e.g. based on availability, — pressure, temperature, price, hours of operation, etc.
    [0050] [0050] As mentioned with respect to figure 2, only two of multiple different configurations between the modules are illustrated. The two illustrated configurations can easily be operated simultaneously. Further refuelings / consolidations may also be made simultaneous to the two above described refuelings.
    [0051] [0051] The second main control strategy is pressure consolidation, which means ensuring a desired pressure in the individual vessels 13 of the supply storage 1 and thereby in the supply storages 1 as such. A non-limiting example of configuration of flow paths necessary for pressure consolidation is illustrated on figure 3 and in this embodiment, the supply storages 1 are defined as medium pressure storages which in this embodiment defines a maximum pressure of 500bar of the vessels 13. As mentioned, the purpose of pressure consolidation is firstly to increase the pressure in one or more vessels 13 of a supply storage 1 and secondly to decrease / emptying one or more vessels 13 of a supply storage 1. One advantage of the first is to increase the first-time period of a refueling where the compressor is bypassed and one advantage of the second is to increase efficiency of dump off or having as much gas pressurized to a determined pressure as possible in the large-scale refueling station as such.
    [0052] [0052] On figure 3 the vessels 13b1-13bn of the second supply storage 1b is emptied into the vessels 13c1-13cn of the third supply storage 1c. Hence by opening valve 6- 7b and valve 6-9b the inlet and outlet flow paths 7b, 9b are opened so that the compressor of module 2b can pressurise the gas from the inlet pressure in the second supply storage 1b to the desired pressure in the third supply storage 1c. One vessel 13 at the time is emptied / filled during the pressure consolidation and which vessel 13 that is source and target vessel 13 inside the individual supply storages 1 is determined by valves 61b1 — 11bn of the second supply storage 1b and valves 61c1 — 11cn of the third supply storage 1c.
    [0053] [0053] This pressure consolidation can be made simultaneously with the refuelings described above with reference to figure 2. In particular, when the first part of the refuelling of vehicle vessel 14b is ended, the supply storage 1b is available and since compressor module 2b, and supply storage 1c is also available the consolidation can be made at the same time as vehicle vessels 14a, 14b are refueled. It should be noted, that even if the vehicle vessel 14b is refueled e.g. from vessel 13b1, vessel 13b2 can be consolidated as described with reference to figure 3 due to the flexible design including the control of the many valves 6. As mentioned, the valves 6 can be controlled by the any of the mentioned controllers 4, 5, 16, 18 e.g. based on reference
    [0054] [0054] The third main control strategy is illustrated with reference to figure 4. On figure 4, the supply storage In is a low-pressure storage supplied with gas from the hydrogen production system 15 via the first supply flow path 11. If / when the pressure of all vessels 13n1 — 13nn has reached 200bar, the produced hydrogen may be conducted to vessels 13 of other supply storages having a pressure below 200bar. Alternatively, the produced gas may be supplied to an available compressor module in this case module 2n via the second supply flow path 12. From the compressor module 2n, via the outlet flow path 8n, the pressurised gas from the production system 15 is delivered to vessels 13 of supply storages 1 having a pressure below the (in this example defined) medium pressure threshold value of 500bar (if they are not in use for refueling).
    [0055] [0055] The main purpose of the third of the main control strategies are to distribute the hydrogen gas produced by the hydrogen production system 15 or delivered by e.g. a truck trailer and stored in the low-pressure supply storage In of figure 4 from the low pressure supply storage to the medium / high pressure storages.
    [0056] [0056] The invention is particularly advantages in that one or more of each of the individual main control strategies can be executed simultaneously in that by the control of the valves 6 flow of hydrogen gas is allowed in at least two but preferably three, four, five, six, seven, eight, nine ten or even more of the flow paths 7, 8, 9, 10, 11, 12 simultaneously depending number of modules 1, 2, 3 of the large-scale refueling stations. When all compressor modules 2 are in used, at least the inlet flow path 7 and one of the outlet flow path 8 or consolidation flow path 9 may be in used per compressor. In addition, hereto a number of dispense flow paths 10 may be in use plus the first supply flow path 11, hence between 30% and 50% of the flow paths may be in uses simultaneously.
    [0057] [0057] All the above required control of valves 6, compressors 2, dispensers 3, etc may at least indirectly controlled by the central controller 5 sending a reference value
    [0058] [0058] As mentioned above, the control of the large-scale refueling station can be controlled according to as least three main control strategies. The first focus on servicing users 1.e. facilitating refueling of vehicle vessels 14, the second focus on preparing for future refuelings i.e. consolidating pressure in the vessels 13 of the supply storages 1 and the third focus on distributing produced hydrogen from the low- pressure storage to the other storages. The large-scale refueling station may be controlled based on a merge of both the first and the second control strategy based on current situation and predicted future situation. In addition, the following can be taking into account when controlling the large-scale refueling station.
    [0059] [0059] If a vessel 13, supply storage 1, compressor module 2, dispenser 3, valve 6, flow paths, electrolyser 15 or other components of the large-scale refueling station needs maintenance, such module can be disregard in the operation and thereby the operation of the remaining parts / modules can be continued during such maintenance.
    [0060] [0060] To reduce the cost of the production of hydrogen, preferably by the — electrolyser 15, the production of hydrogen gas is preferably done while the prices of energy available on the utility grid is as low as possible. Of course, the main object is to ensure enough hydrogen in the supply storages 1 to facilitate the needed number of refuelings no matter energy price. However, when the amount of hydrogen is above a defined level (referred to as plant pressure threshold) of usage of the total capacity of the supply storage vessels 13 such as above 25%, preferably above 50%, most preferably above 75%, the production can be made with respect to energy price to reduce the overall operation cost of the large-scale refueling station. In practise, as much of the hydrogen as possible is therefore produced during night time where energy price typically is lower.
    [0061] [0061] As mentioned, the compressors 17 are preferably variable speed compressors. This means that they can be operated between standstill and nominal speed in dependent of the electric voltage / frequency applied. Accordingly, at low speed the energy consumption (and thereby cost of operation of the compressor) is lower than — when the compressor 17 is operated at full speed / nominal speed.
    [0062] [0062] The flexibility added by the variable speed compressors 17 leads to a reduction of the overall operation costs of the large-scale refueling station. This is at least partly because, when the pressure in the vessels 13 of the supply storages 1 (preferably the medium pressure storages) are sufficient, then pressure consolidation — can be facilitated at reduced speed of the compressor leading to reduced noise and cost. A further example of operation of the compressor 17 with variable speed is if pressure in the medium pressure supply storages are sufficient with respect to the expected refuelings during the next couple of hours.
    [0063] [0063] The main controller 5 or hydrogen production system controller 16 may initiate production of hydrogen from the hydrogen production system 15 if the system 15 is ready and the produced hydrogen can be delivered to the low-pressure storage or via a compressor 17 to a medium / high pressure storage or in a vehicle vessel 14.
    [0064] [0064] The main controller 5 preferably receives information of energy price e.g. from grid energy marked place to be able to determine when to consolidation and / or — produce hydrogen if capacity is available in that refuelings are always highest priority. Further, the main controller may determine when maintenance of a module has to be made and in this way bypass such module. Control signals to valves 6 and local controllers 4, 16, 18 may include open / close valve signal and information of purpose of operation of compressor 17. If high pressure hydrogen is needed to a refueling, the local controller 4, 18 may also control the cooling system / dispenser cooling system so that the hydrogen is entering the vehicle vessel 14 with a desired temperature. Other relevant and necessary control to conduct a refueling is also controlled by the local controller 4, 18.
    [0065] [0065] From the above, it is now clear that the present invention relates to a large- scale hydrogen refueling station comprising a plurality of storages 1, compressor modules 2 including compressors 17, dispensers 3 (maybe including dispenser cooling system) and at least one hydrogen production system 15. A main controller 5 may partially control / provide control reference values related to price, maintenance, when the production of hydrogen should be initiated e.g. with respect to energy price, storage capacity or the like. The controller 16 of the hydrogen production system 15 then produces hydrogen according to the received reference or e.g. pressure / temperature of the low-pressure storage. The dispenser controller 18 may control valve 6 relevant of a refueling as well as dispenser cooling system 19. The local controller 4 may control the compressor module 2.
    [0066] [0066] All control is made based on input from external sensors or data processors such as pressure sensor, temperature sensors, central servers, external data providers, etc. these external data contributors are not illustrated on the figures.
    [0067] [0067] In an aspect, the main controller 5 is controlling valves 6 and sends control references to the compressor modules 2 / dispenser module 3 to facilitate either a pressure consolidation, a refueling of a vehicle vessel 14 or moving of gas from low to medium / high pressure storage.
    [0068] [0068] As mentioned above, the main controller 5, local controllers 4, dispenser — controllers 18, hydrogen production system controller 16 is together or individually able to facilitate several consolidations and several refuelings at the same time and even also at the same time facilitate production of hydrogen. To ensure as low operation costs as possible, the compressors 17 are variable speed compressors which can reduce energy consumption (and noise) when reducing speed.
    — Further, the operation of compressors 17 and the hydrogen producing system 15 may be controlled with respect to energy prise of power received from the utility grid.
    DK 2019 70036 A1 21 List
    1. Supply storage
    2. Compressor module
    3. Dispenser module
    4. Local controller
    5. Main controller
    6. Valves
    7. Inlet flow path
    8. Outlet flow path
    9. Consolidation flow path
    10. Dispense flow path
    11. First supply flow path
    12. Second supply flow path
    13. Supply storage vessel
    14. Vehicle vessel
    15. Hydrogen production system
    16. Hydrogen production system controller
    17. Variable speed compressor
    18. Dispenser controller — 19. Dispenser cooling system
    20. Hose
    权利要求:
    Claims (18)
    [1] 1. A large-scale hydrogen refueling station comprising a plurality of supply storage (1), compressor modules (2) comprising a local controller (4), dispenser modules (3) comprising a dispenser controller (18), and a hydrogen production system (15) comprising a hydrogen production system controller (16) mutually connected by one or more flow paths (7, 8, 9, 10, 11, 12), wherein one of the controllers (4, 18, 16) facilitates control of valves (6) and thereby flow of hydrogen gas in the flow paths (7, 8, 9, 10, 11, 12) between one or more of the plurality of supply storages (1), compressor modules (2), dispenser modules (3) and hydrogen production system (15), wherein the control of the valves (6) enable flow of hydrogen gas in at least three of the flow paths (7, 8, 9, 10, 11, 12) simultaneously.
    [2] 2. A large-scale refueling station according to claim 1, comprising at least three supply storages (1), at least three compressor modules (2) and at least three dispenser modules 6).
    [3] 3. A large-scale refueling station according to claim 1 or 2, wherein the compressor (17) of the compressor module (2) is a variable speed compressor. 4, A large-scale refueling station according to any of the preceding claims, wherein the valves (6) are controlled to establish: - an inlet flow path (7) between at least one supply storage (1) and at least one compressor module (2), - an outlet flow path (7) between at least one compressor module (2) and at least one dispenser module (3), - a consolidation flow path (8) between at least one compressor module (2) and at least one supply storage (1), - a dispense flow path (10) between at least one supply storage (1) and at least one dispenser module (3),
    [4] DK 2019 70036 A1 23 wherein the dispenser controller (18) is controlling the valves (6) so as to facilitate flow of gas in at least three of inlet flow path (7), outlet flow path (8), consolidation flow path (9) or dispense flow path (10) simultaneously.
    [5] 5. A large-scale refueling station according to any of the preceding claims, wherein — the valves (6) are controlled to establish - afirst supply flow path (11) between the hydrogen production system (15) and at least one supply storage (1), and / or - 2asecond supply flow path (12) between the hydrogen production system (15) and at least on compressor module (2), wherein the hydrogen production system controller (16) is controlling the valves (6) so as to facilitate flow of gas in the first supply flow path (11) or second supply flow path (12) simultaneously with flow of gas in at least one of the inlet flow path (7), outlet flow path (8), consolidation flow path (9) or dispense flow path (10).
    [6] 6. A large-scale refueling station according to any of the preceding claims, wherein the supply storages (1) comprise a plurality of vessels (13), wherein at least one of the supply storages (1) is predefined as low-pressure storage and at least two of the supply storages (1) are predefined as medium-pressure storages,
    [7] 7. A large-scale refueling station according to claim 6, wherein the low pressure is defined as being in the range of 0 bar — 250 bar and the medium pressure is defined as — being in the range of 150 bar — 200 bar, wherein the predefined medium pressure is always equal to or higher than the predefined low pressure.
    [8] 8. A large-scale refueling station according to any of the preceding claims, wherein the central controller (5) is controlling the valves (6) so that a first inlet flow path (7a) is connecting a first supply storage (1a) to a first compressor module (2a), a first outlet — flow path (8) is connecting the first compressor module (2a) to a first dispenser module (3), a second inlet flow path (7b) is connecting a second supply storage (1b) and a compressor module (2b) and a first consolidation flow path (9) is connecting the second compressor module (2b) to a third supply storage (1c).
    DK 2019 70036 A1 24
    [9] 9. A large-scale refueling station according to any of the preceding claims, wherein one of the plurality of supply storages (1) is defined as a low-pressure supply storage and wherein the first supply flow path (11) is only connecting the hydrogen production system (15) and the low pressure supply storage.
    [10] 10. A large-scale refueling station according to any of the preceding claims, wherein a first supply storage vessel (13a) of a supply storage (1) serves as gas input to one inlet flow path (7) to a first compressor module (2) simultaneously with a second vessel (13b) of the supply storage (1) serving as gas receiver of a consolidation flow path (9) from a second compressor module (2).
    [11] 11. A large-scale refueling station according to any of the preceding claims, wherein the hydrogen production system (15) is producing hydrogen when the pressure in the at least one supply storage vessel (13) is below a plant pressure threshold.
    [12] 12. A large-scale refueling station according to any of the preceding claims, wherein the hydrogen production system (15) is production hydrogen when the energy price is — below an energy price threshold value if the pressure in all supply storage vessels (13) is above a plant pressure threshold.
    [13] 13. A large-scale refueling station according to any of the preceding claims, wherein a first part of a refueling is made directly from one of the supply storages (1) and a second part of the refueling is made via a compressor module (2), — wherein the shift between the first and the second part is made when the flow in the dispense flow path (10) is estimated to be lower than the flow generated by the compressor module (2) in the output flow path (8).
    [14] 14. A large-scale refueling station according to any of the preceding claims, comprising a main controller (5) facilitating broadcasting a control reference of the list comprising: related to energy consumption, related to maintenance, related to pressure consolidation to the dispenser controller (18) and / or local controller (4).
    [15] 15. Method of refueling a vehicle vessel (14) from a large-scale refueling station comprising a plurality of supply storage (1), compressor modules (2) comprising a
    DK 2019 70036 A1 25 local controller (4), dispenser modules (3) comprising a dispenser controller (18), and a hydrogen production system (15) comprising a hydrogen production system controller (16) mutually connected by one or more flow paths (7, 8, 9, 10, 11, 12), the method comprising the following steps: — connecting the vehicle vessel (14) to a dispenser module (3), — -starting the refueling from a user interface, preferably on a dispenser module 3), — initiating flow of hydrogen gas from a supply storage (1) via a dispense flow path (10) during a first part of the refueling, — continuing the flow of hydrogen via a compressor module (2) during a second part of the refueling, and — disconnecting the dispenser module (3) from the vehicle vessel (14) when a target pressure is reached, wherein the refueling is initiated by a user who activates a dispenser controller (18), — the dispenser controller (18) change status of one or more valves (6) to facilitate flow of gas via a dispense flow path (10) during a first part of the refueling and activates the local controller (4) of the compressor module (2) and change status of one or more valves (6) to facilitate flow of gas via an outlet flow path (8) during a second part of the refueling
    [16] 16. A method according to claim 15, wherein during the second part of the refueling a first compressor module (2a) is used and simultaneously a second compressor (2b) is used for pressure consolidation between vessels 13 of one or two of the supply storages
    1.
    [17] 17. A method according to claim 16, wherein simultaneously a third compressor module (2c) is used for moving pressure from a low pressure storage connected to the hydrogen production system (15) to a medium or high pressure supply storage (1) or to a vehicle vessel (14).
    DK 2019 70036 A1 26
    [18] 18. Use of a large-scale refueling station according to any of the claims 1-14 and controlled according to the method of any of the claims 15-17.
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    同族专利:
    公开号 | 公开日
    CN113260810A|2021-08-13|
    WO2020147911A1|2020-07-23|
    DK180560B1|2021-06-23|
    EP3911889A1|2021-11-24|
    US20220003361A1|2022-01-06|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    JP6449860B2|2013-05-31|2019-01-09|ヌヴェラ・フュエル・セルズ，エルエルシー|Cascading method and system for replenishing distributed hydrogen|
    US9739418B2|2013-09-27|2017-08-22|Uchicago Argonne, Llc|Enhanced methods for operating refueling station tube-trailers to reduce refueling cost|
    EP3249281B1|2016-05-23|2022-02-23|Air Products And Chemicals, Inc.|Compressed gas dispensing|
    US10267456B2|2016-09-22|2019-04-23|Uchicago Argonne, Llc|Two-tier tube-trailer operation method and system to reduce hydrogen refueling cost|
    SE542134C2|2017-07-07|2020-03-03|Boh Westerlund|Hydrogen refuelling station comprising a fill tank arranged with a cooling system|CN113375047B|2021-08-11|2021-11-30|河南氢枫能源技术有限公司|Hydrogen station with double compression systems operating and operation method thereof|
    法律状态:
    2020-08-21| PAT| Application published|Effective date: 20200719 |
    2021-06-23| PME| Patent granted|Effective date: 20210623 |
    优先权:
    申请号 | 申请日 | 专利标题
    DKPA201970036A|DK180560B1|2019-01-18|2019-01-18|Large-scale hydrogen refueling station|DKPA201970036A| DK180560B1|2019-01-18|2019-01-18|Large-scale hydrogen refueling station|
    CN202080008034.9A| CN113260810A|2019-01-18|2020-01-16|Large hydrogen refueling station|
    PCT/DK2020/050020| WO2020147911A1|2019-01-18|2020-01-16|Large-scale hydrogen refueling station|
    US17/416,066| US20220003361A1|2019-01-18|2020-01-16|Large-scale hydrogen refueling station|
    EP20701528.0A| EP3911889A1|2019-01-18|2020-01-16|Large-scale hydrogen refueling station|
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