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    • 专利摘要:
    Method for measuring the amount of gas introduced into a gas tank (2) via a filling station (1) provided with a filling line (4) comprising an upstream end (3) connected to at least one source (5) of pressurized gas and a downstream end (8) connected to a reservoir (2) to be filled, the filling line (4) comprising a flowmeter (9) and at least one downstream isolation valve (6) disposed between the flowmeter and the downstream end (8) of the filling line, the method comprising a step of transferring gas from the source (5) to the reservoir (2) during which the downstream isolation valve (6) is open, a step of interrupting the gas transfer with a valve closure (6) downstream, the method comprising a step of measuring, by the flow meter (5), the amount of gas transferred during the transfer step, the method characterized in that it comprises a step of generating a signal of qu the amount of corrected transferred gas being obtained by reducing or increasing by a fixed corrective amount the amount of transferred gas measured by the flow meter (5) during the transfer step;
    公开号:FR3065069A1
    申请号:FR1753046
    申请日:2017-04-07
    公开日:2018-10-12
    发明作者:Thibaut FRANCOIS
    申请人:Air Liquide SA；LAir Liquide SA pour lEtude et lExploitation des Procedes Georges Claude；
    IPC主号:
    专利说明:

    Holder (s): AIR LIQUIDE, ANONYMOUS COMPANY FOR THE STUDY AND EXPLOITATION OF GEORGES CLAUDE PROCESSES Société anonyme.
    Extension request (s)
    Agent (s): AIR LIQUIDE.
    VX) METHOD FOR MEASURING THE QUANTITY OF GAS INTRODUCED IN A RESERVOIR AND CORRESPONDING STATION.
    FR 3 065 069 - A1
    Method for measuring the quantity of gas introduced into a gas tank (2) via a filling station (1) provided with a filling pipe (4) comprising an upstream end (3) connected to at least one source (5) of pressurized gas and a downstream end (8) connected to a tank (2) to be filled, the filling pipe (4) comprising a flow meter (9) and at least one downstream isolation valve (6) disposed between the flow meter and the downstream end (8) of the filling pipe, the method comprising a step of transferring gas from the source (5) to the tank (2) during which the downstream isolation valve (6) is opened, a step of interrupting the transfer of gas with a valve closure (6) downstream, the method comprising a step of measuring, by the flow meter (5), the amount of gas transferred during the transfer step, the method being characterized in that it comprises a step of generating a signal for the quantity of corrected transferred gas, the quantity corrected transferred gas tee being obtained by reducing or increasing by a corrective quantity the quantity of transferred gas measured by the flow meter (5) during the transfer step

    The invention relates to a method for measuring the quantity of gas introduced from the reservoir and to a filling station.
    The invention relates more particularly to a method for measuring the quantity of gas introduced into a gas tank via a filling station provided with a filling pipe comprising an upstream end connected to at least one source of pressurized gas and a downstream end connected to a tank to be filled, the filling line comprising a flow meter and at least one downstream isolation valve disposed between the flow meter and the downstream end of the filling line, the method comprising a step of transferring gas from the source to the tank during which the downstream isolation valve is open, a step of interrupting the gas transfer with a downstream valve closure, the method comprising a step of measuring, by the flow meter, the amount of gas transferred during of the transfer step.
    Filling stations for pressurized gas tanks, in particular vehicle fuel gas tanks, require measuring the quantity of gas introduced into the tank with a relatively high level of precision. This applies in particular to the filling of pressurized hydrogen gas tanks.
    This quantity must be measured for billing (in the same way as a liquid fuel).
    In the case of a gas, for example hydrogen, many parameters have an influence on the measurement of this quantity (pressure, temperature, volume, flow rate ...).
    This quantity depends in particular on the initial conditions (pressure in the tank before filling in particular) and final conditions (pressure after filling in particular). This quantity is also difficult to measure because generally an amount of gas present in the circuit is purged outside after filling. This purge is intended to lower the pressure in the hose of the filling line to allow the user to disconnect the end of the filling line from the tank.
    Ideally, the flow rate of the transferred gas should be measured as close as possible to the tank (at the filling nozzle). However, for industrial and technical reasons, this flow measurement is in fact carried out further upstream. Thus, part of the gas measured by a flow meter is not transferred to the tank and risks being billed to the customer.
    To measure as accurately as possible the quantity of gas transferred (and therefore the quantity invoiced) it is known not to count the gas which is used if necessary during the test before filling (gas pulses can indeed be provided for leak tests and / or to calculate the tank volume or other parameters).
    An object of the invention is to propose a method and / or a device allowing an improvement in the precision of the measurement of this quantity of gas actually supplied to the tank.
    An object of the present invention is to overcome all or part of the drawbacks of the prior art noted above.
    To this end, the method according to the invention, furthermore in accordance with the generic definition given in the preamble above, is essentially characterized in that it comprises a step of generating a signal of quantity of gas transferred corrected, the quantity of corrected transferred gas being obtained by reducing or increasing by a corrective quantity the quantity of transferred gas measured by the flow meter during the transfer step.
    Furthermore, embodiments of the invention may include one or more of the following characteristics:
    the flow meter is of the type generating electrical signals in the form of successive pulses each corresponding to an elementary quantity of gas measured, the generation of a signal of quantity of corrected transferred gas being obtained by a modification step of at least 1 one of: the value of the elementary quantity of gas corresponding to a pulse generated by the flow meter and / or the number of pulses generated by the flow meter and / or the frequency of emission of the pulses generated by the flow meter and / or the number pulses counted among the pulses generated by the flow meter,
    - the generation of a signal for the quantity of corrected transferred gas is obtained by subtracting or adding a determined quantity of pulses to the pulses generated by the flow meter,
    - the modification step is carried out by modifying (by increasing or reducing) the frequency of the pulses generated by the flow meter, that is to say by removing or adding a determined duration to the time interval separating pulses successive generated by the flow meter,
    - the corrective quantity of gas is a determined proportion of the quantity of gas measured by the flow meter during the transfer step,
    - the determined proportion is fixed, that is to say independent of the operating conditions of the filling step, or variable, that is to say dependent on the operating conditions of the filling step,
    the filling line comprises, downstream of the downstream isolation valve, a controlled purge valve, the method comprises a step of purging outside the filling line of at least part of the trapped pressurized gas in the downstream part of the filling pipe after the transfer step,
    - the corrective quantity of gas is a determined percentage of the quantity of gas evacuated during the purge step,
    the percentage which varies as a function of the operating conditions of the filling step and in particular as a function of the pressure measured in the transfer line during the transfer step, said percentage being calculated regularly during the filling step and in particular at the end of the transfer step,
    - the percentage is proportional to the pressure in the transfer line,
    - the percentage is between 100% and 0% and preferably between 95% and 75%,
    - the filling line includes a purge flow meter configured to measure the quantity of gas evacuated during the purge step,
    - the modification stage is carried out during the transfer stage,
    - that the modification step is carried out is carried out in a regular time distribution during the transfer step,
    - the modification stage is carried out at the end or after the end of the transfer stage,
    the filling station comprises an electronic data processing and storage device, comprising in particular a microprocessor and / or a computer, said electronic device being configured to receive a signal representative of the quantity of transferred gas measured by the flow meter during the transfer step and for calculating and / or receiving and / or transmitting and / or displaying the signal for the quantity of corrected transferred gas,
    the operating conditions of the filling step include at least one at least among: the duration of the transfer step, the pressure measured or estimated in the filling line before the transfer step, the pressure measured or estimated in the filling line during the transfer step, the pressure measured or estimated in the filling line at the end of the transfer step, the pressure measured or estimated in the filling tank before the transfer step, the pressure measured or estimated in the filling tank during the transfer step, the pressure measured or estimated in the filling tank at the end of the transfer step, the temperature of the gas in the transfer line, the temperature of the gas in the tank, the volume of the transfer line downstream of the downstream isolation valve, the measured or estimated quantity of gas vented during a purge phase of the transfer line after the step transfer,
    - in the case where the corrected quantity of transferred gas consists in reducing the quantity of transferred gas measured by the flowmeter during the transfer step by a corrective quantity, this reduction is achieved by deleting and / or not counting not certain pulses determined among the pulses generated by the flow meter,
    - the corrective quantity is a function of at least one of the following parameters: the pressure measured or estimated in the filling line before the transfer step, the pressure measured or estimated in the filling line during the transfer step, the pressure measured or estimated in the filling line at the end of the transfer step, the pressure measured or estimated in the filling tank before the transfer step, the pressure measured or estimated in the filling tank during the transfer step, the pressure measured or estimated in the filling tank at the end of the transfer step, the temperature of the gas in the transfer line, the temperature of the gas in the tank, the volume of the transfer line in downstream of the downstream isolation valve, the measured or estimated quantity of gas vented during a purge phase of the transfer line after the transfer step
    - the proportion is a function of the final pressure in the tank (2) or in the transfer line,
    - the pressure in the tank or in the filling pipe during or at the end of the transfer step is measured or estimated, the corrective quantity determined being an amount which varies as a function (preferably only) of this pressure,
    - the corrective determined quantity of gas is removed from the measured quantity of transferred gas and is between 11 and 5 grams when the pressure in the tank to be filled or in the filling line is between 850 and 700 bar and between 8 and 2.5 grams when the pressure in the tank to be filled or in the filling line is between 700 and 400bar_and between 6 and 1 gram when the pressure in the tank to be filled or in the filling line is between 400 and 200bar ,
    - the corrective quantity of gas determined is a quantity which varies according to the temperature of the gas in the tank to be filled or in the filling pipe,
    - the percentage (%) determined of the quantity of gas evacuated during the purge step defining the corrective quantity is given by the formula% = (P-Pi) / (Pm-Pi) in which P is the pressure in the filling line during or at the end of the transfer step, Pi is the final pressure in the transfer line after the evacuation step, Pm being a determined reference value such as the maximum operating pressure in the line transfer, Pm being between 500 and 1000bar and preferably between 700 and 900bar, for example equal to 875bar, the pressure values being expressed for example in bar or Pa,
    the corrective determined quantity of gas is calculated by an equation of state of the gas and in particular the equation of ideal or real gases applied to the gas in the downstream part of the filling pipe before the purging step and after the step purge from the following parameters: the known volume of the filling line downstream of the downstream isolation valve, the final pressure measured in the tank to be filled or in the filling line during or at the end of the stage transfer and before the purging step, the measured or estimated temperature of the gas in the tank to be filled or in the filling line, the known nature of the gas and in particular its molar mass, the pressure in the filling line after purge step, the corrective quantity being the result of the difference between the amount of gas present in the in the downstream part of the filling line before the purge step and the amount of gas present in the in the downstream part of the idiot filling after the purging step,
    - the corrective determined quantity of gas is a fixed quantity.
    , The invention also relates to a filling station for pressurized fluid tanks, in particular for filling pressurized hydrogen tanks, comprising a filling pipe comprising an upstream end connected to at least one source of pressurized gas and to the at least one downstream end intended for connection to a tank to be filled, the filling line comprising a flow meter and at least one downstream isolation valve disposed between the flow meter and the downstream end of the filling line, the at least one valve being controlled to allow a gas transfer step from the source to the reservoir, the flow meter being configured to measure the quantity of gas transferred and generate a corresponding signal in response, the station comprising an electronic data processing and storage device, comprising in particular a microprocessor and / or a computer, the electronic device being configured to receive the signal from the flow meter and to generate a signal for the quantity of corrected transferred gas obtained by reducing or increasing by a corrective determined quantity the quantity of transferred gas measured by the flow meter during the transfer.
    The invention may also relate to any alternative device or process comprising any combination of the above or below characteristics.
    In particular, the electronic device can be configured to carry out all or part of the above or below actions.
    Other particularities and advantages will appear on reading the description below, made with reference to the figures in which:
    - Figure 1 shows a schematic and partial view illustrating an example of the structure and operation of a filling station according to a first possible embodiment of the invention,
    - Figure 2 shows a schematic and partial view illustrating an example of the structure and operation of a filling station according to a second possible embodiment of the invention.
    The filling station for pressurized fluid reservoirs shown diagrammatically in FIG. 1 conventionally comprises a filling pipe 4 comprising at least one upstream end 3 connected to at least one source 5 of pressurized gas and at least one downstream end 8 intended for connection to a tank 2 to be filled.
    The gas source (in particular hydrogen) may comprise at least one of: one or more pressurized gas tanks, in particular several tanks connected in parallel for cascade filling, a compressor, a source of liquefied gas and a vaporizer, and / or any other source of gas under appropriate pressure.
    The downstream end 8 comprises for example at least one flexible hose, the terminal end of which comprises a connector, preferably a quick connector, allowing its tight connection with the inlet of a tank 2 or of a filling circuit of a tank 2 (in particular of a vehicle).
    The filling pipe 4 comprising a flow meter 9 and at least one downstream isolation valve 6 disposed between the flow meter 9 and the downstream end 8 of the filling pipe 4. The isolation valve 6 is preferably a valve 6 controlled to allow a step of transferring gas from the source 5 to the tank 2 when it is open.
    The flow meter 9, preferably of the Coriolis effect type, is configured to measure the quantity of gas transferred and generate a corresponding signal (preferably electrical).
    Station 1 comprises an electronic device 12 for processing and storing data, for example comprising a microprocessor and / or a computer. This electronic device 12 is configured to receive the signal from the flow meter 9 and to generate a signal for the quantity of corrected transferred gas obtained by reducing or increasing by a corrective quantity the quantity of transferred gas measured by the flow meter 9 during the transfer.
    Preferably, the electronic device 12 can be configured to control all or part of the valves 6, 10 or organs of the station and / or to receive pressure and / or temperature measurements made by one or more sensors in the circuit 4 filling (upstream and / or downstream of the downstream isolation valve 6. In particular, preferably the electronic device 12 can be configured to control the transfer of gas to the tank 2 (flow control and / or sources. ..) according to a predetermined flow (fixed and / or variable pressure ramp).
    In addition, the electronic device 12 can comprise or be associated with a man-machine interface comprising for example a display 13 and / or a payment terminal 14 and / or an input and / or identification device. The electronic device 12 may include wireless communication devices for transmitting or receiving this data and / or other data. In particular, all or part of the data and / or data storage and / or display and / or billing means can be deported from the station or duplicated remotely (via the Internet or a local network and using example of wireless phone applications).
    As illustrated, the filling pipe 4 also preferably further comprises a purge valve 10 located downstream of the downstream isolation valve 6.
    The purge valve 10 is preferably controlled to evacuate outside the filling pipe 4 at least part of the pressurized gas trapped in the downstream part of the filling pipe 4 after a transfer step (at the end of a filling). The purged gas is evacuated to the atmosphere or to a recovery zone.
    By reducing or increasing the quantity of gas transferred measured by the flow meter 9 during the transfer step by a determined corrective quantity, it is thus possible to display and / or charge the user a quantity of gas which is closer to or equal to the amount of gas actually transferred to tank 2.
    Preferably, the flow meter 5 is of the type generating electrical signals in the form of successive pulses ("pulses") each corresponding to an elementary quantity of gas measured (for example one gram or three grams or "x" gram for each pulse). That is to say, each time the flow meter measures the passage of a quantity of gas (for example a gram) it emits a pulse. The flow rate corresponds to the number of pulses per unit of time (for example a certain number of grams of gas per minute).
    The generation of a corrected transferred gas quantity signal can be obtained by a modification step of at least one of: the value of the elementary quantity of gas corresponding to a pulse generated by the flow meter 5 and / or the number of pulses generated by the flow meter 5 and / or the frequency of transmission of the pulses generated by the flow meter 5 and / or the number of pulses counted among the pulses generated by the flow meter 5.
    The generation of a signal for the quantity of corrected transferred gas can in particular be obtained by subtracting or adding a determined quantity of pulses to the pulses generated by the flow meter. The drawdown can be obtained for example by not taking into account (by not counting) certain pulses.
    For example, the corrective quantity of gas is a determined proportion of the quantity of gas measured by the flow meter 5 during the transfer step
    For example, only a percentage of pulses is subtracted or not counted or added to the pulses generated by the flow meter 9. This percentage (or corrective quantity) is preferably a function of the pressure in the filling line 4 during and / or at the end of the gas transfer step.
    The amount of gas purged after filling (after a gas transfer step) essentially depends on the final pressure in the withdrawal line 4. This final pressure depends on the maximum operating pressure of the tank (for example 200bar or 300bar or 700bar or 875bar or an intermediate or higher value).
    According to an advantageous embodiment, the corrective determined quantity of gas is a determined percentage of the quantity of gas evacuated during the purging step. This percentage can be arbitrarily fixed or calculated according to the operating conditions of the filling.
    The corrective quantity is for example a function (in particular proportional) of the current and / or final pressure in the transfer line 4 during the gas transfer.
    For example, we can define a proportional relationship between:
    - the current pressure P (measured regularly) in the transfer line 4 during the transfer step,
    - the total number Nf of pulses generated by the flow meter 9 at the instant considered in the transfer step,
    - the percentage (%) of impulse not counted / deleted / added,
    - the corrected Ncorrect number of pulses (after calculating the corrected quantity of transferred gas),
    - The quantity Ni of pulses corresponding to the quantity of gas purged during a purge step consecutive to a transfer step.
    This quantity Ni of pulses corresponding to the quantity of gas purged during a purge step can be calculated or measured or predefined arbitrarily. This quantity Ni of pulses corresponding to the quantity of gas purged during a purging step depends for example:
    - the volume (known) of the purged filling pipe 4,
    - the maximum final pressure Pm allowed in the filling line 4 (or a maximum reference pressure determined), for example between 500 and 1000bar and preferably between 700 and 900bar, for example equal to 875bar,
    the final pressure Pi in the filling pipe 4 after the evacuation step (purge), this pressure being measured or estimated, and, optionally predefined, for example at a few bars, in particular 3bar,
    - the measured or estimated temperature of the gas in the filling pipe 4.
    For example, the percentage (%) of unrecognized / suppressed impulses can be given by the following formula:
    % = (P-Pi) / (Pm-Pi) in which P is the current pressure in the filling line 4 during the transfer step, Pi is the final pressure in the transfer line after the evacuation step / purge, Pm being the determined reference value such as the maximum operating pressure in line 4 of transfer, for example equal to 875bar.
    Thus, by determining this percentage% (in a fixed manner beforehand or in real time), it is possible to define the corrected number Ncorrect of pulses as the difference between the total number Nf of pulses generated by the flow meter 9 and the product the percentage with the quantity Ni of pulses corresponding to the quantity of gas purged:
    Ncorrect = Nf -%. Ni
    In an example of possible implementation, at the start of filling the conditions can be as follows: P = 0bar, Pi = 3bar, Pm = 875bar therefore% = 2percent, Nf is for example equal to one hundred pulses (the quantity of total gas to be transferred as being equal to 100 measured pulses), and Ni equal to three pulses.
    During filling, the conditions can be as follows: P = 400bar, Pi = 3bar, Pm = 875bar therefore% = 46 percent, Nf = one hundred pulses, and Ni equal to three pulses. Then Ncorrect = between 98 and 99 pulses. That is to say, the correction was to remove one to two pulses.
    Later during filling, the conditions can be as follows: P = 750bar, Pi = 3bar, Pm = 875bar therefore% = 86 percent, Nf = one hundred pulses, and Ni equal to three pulses. Then Ncorrect = about 97 pulses. That is to say, the correction consisted in removing three pulses.
    Of course, the percentage is not limited to the above expression and could be a predefined determined value as a function of the pressure P in the filling line 4 at the start or at the end of filling or a reference value independent of the pressure in the filling line 4.
    Similarly, the percentage could be a predefined determined value as a function of the pressure differential (PO-Pi) between the pressure PO in the transfer line 4 before the transfer step and the pressure (Pi) in the measured transfer line during the transfer step and / or at the end of the transfer step.
    The quantity Ni of pulses corresponding to the quantity of gas purged during a purging step can be predetermined and quantified by measurements according to the operating conditions or by calculation (equation of state of the gas, thermodynamic equation).
    Thus, knowing Nf,% and Ni, the station can continuously adjust during the gas transfer (and / or at the end of the gas transfer) the quantity of corrected transferred gas which will actually be billed / taken into account.
    The advantage of carrying out this adjustment continuously during the transfer step (and not at the end of the transfer step) is to have an accurate measurement (display) in real time which makes it possible, if necessary, to deliver information which does not undergo any variation when filling stops.
    In particular, if the user wishes to stop the transfer of gas at a certain displayed level of pressure or quantity of gas or billing, the continuous adjustment will not modify the quantity of gas displayed / billed at the end of filling.
    On the contrary, in the event of an adjustment at the end of gas transfer, the quantity of gas displayed in real time may be subject to variation after shutdown. This may surprise a user, if any, who precisely wishes to stop a gas transfer based on a precise value reached for the amount of gas invoiced.
    This adjustment can be carried out continuously at each predefined time interval of time (seconds), and / or at each pressure interval in the predefined reservoir (bar) and / or at each predefined quantity of pulses or in real time.
    For example, the adjustment could consist in removing ten percent of gas from the quantity of gas measured by the flow meter 9. If the flow meter 9 generates a pulse for every ten grams measured and a kilogram of gas is transferred, the signal generated by the flow meter will contain one hundred pulses (10gx100 = 1000g). In this case, the 10% adjustment consists of removing (not counting) ten pulses. These ten pulses can be removed at the end (the last ten) or regularly, one every ten pulses generated during the transfer step.
    The remaining ninety pulses (10gx90 = 900grams) constitute the quantity of transferred gas corrected and actually transferred or invoiced.
    Thus, the corrective amount of gas can be known at each pressure level during filling. For each gram of gas measured by the flow meter 9 a small percentage (two to fifteen percent for example) can be considered not introduced into the tank 2 and purged.
    Instead of removing (not counting) / adding pulses to those measured by the flow meter 9, it is also possible to play on another parameter such as the phase or frequency modulation of the pulses. Thus the time interval between the pulses can be used as an adjustment variable to arrive at the quantity of gas corrected.
    Thus, it is possible to "reconstruct / modify" the frequency of the pulses generated by the flow meter 9 to take account of this correction.
    For example, if a hundred pulses are generated during a duration D by the flow meter 9, these are reprocessed (signal processing) in ninety pulses regularly distributed during the same duration D.
    The time added or subtracted between two pulses can be determined to correspond to the amount of gas corrected.
    That is, the Ncorrect pulses are "distributed" regularly during the predefined filling time.
    The filling time D can be defined / estimated beforehand (before filling) as a function of the initial pressure in the tank 2, the speed of pressure increase expected (predefined pressure ramp) and the desired final pressure.
    For example for a tank of 122 liters, and a pressure ramp of 218 bar / minute, and a target pressure of 819 bar, the duration D of filling is 3 minutes and 15 seconds (quantity injected is 4.2 kg and the temperature of filling is -33 ° C). These filling conditions are defined, where appropriate, by standardized conditions.
    The link between the time added or removed between the pulses measured by the flow meter 9 can be based on:
    - the estimated or calculated duration of the filling which can be divided into determined intervals (delta t),
    - the volume of the determined filling pipe 4 intended to be purged, this volume associated with the pressure before purging makes it possible to define the quantity Ni of pulses corresponding to the quantity of gas purged,
    - It is then possible to match the quantity of gas to be purged and the equivalent duration of the corresponding Ni pulses.
    Indeed, the pressure variation multiplied by the duration defines the pressure reached. The pressure being known, it makes it possible to determine the density of the gas via an equation of state (measured or assumed to be known temperature). The density multiplied by the volume to be purged defines the quantity (mass) of gas to be purged and therefore Ni.
    This duration can be divided by the estimated duration D of the filling and distributed for each of the calculated time intervals (delta t). So we add (or remove) a time (t1) to each interval (delta t). The frequency of the pulses generated is therefore modified to continuously take into account the quantity of corrective gas to be added / removed.
    Thus, for example for the same filling time D and n pulses measured by the flow meter 9 separated by a time interval (delta t) between two pulses (n integer> 0) can be modified into m pulses (m integer> 0 and m <n) separated by an increased time interval (delta t + t1) between two pulses.
    In the case where a corrective quantity of gas has to be added, there could be, after adjustment, q pulses (q integer> 0 and q> n) separated by a reduced time interval (delta t -11) between two pulses.
    To simplify the process, all or part of the filling parameters (duration) D, amount of gas transferred, ambient temperature, temperature of the gas in the filling line 4, pressure before the transfer step in the filling line 4, temperature final in the filling line 4 at the end of the transfer step, etc.) can be fixed beforehand according to conditions deemed standard.
    The quantity of gas transferred corrected would then be calculated on these fixed conditions. This allows in particular to limit the number of parameters to be measured and therefore the number of devices whose operation must be certified.
    Likewise, in another possible embodiment, the value of the unit quantity of the pulses can be used as an adjustment variable to arrive at the quantity of gas corrected.
    For example, the pulses are no longer generated every gram but every 1.1 grams of gas measured.
    Preferably, in this case the known value of the volume of the reservoir 2 to be filled is used.
    The correction precision can be adapted to a type of tank 2 (volume in particular).
    This adjustment is also adapted when the station 1 is modified (volume of the filling line 4 in particular).
    Thus, the quantity of corrective gas can be defined or predefined for each increase in pressure in the filled tank 2 (and if necessary as a function of other parameters such as the temperature of the gas).
    According to another possibility, the corrective determined quantity of gas can be a fixed quantity (for example a determined mass of gas) whatever the filling conditions. For example, the corrective quantity determined is between ten and two grams and preferably between nine and six grams.
    For example, the corrective amount will be independent of the final pressure at the end of the gas transfer step. This quantity will be preset for maximum filling pressure conditions (200 bar, 350 bar or 700 bar for example). In this case, it is not necessary to provide a pressure sensor 15 in the measurement and calculation loop or not necessary to use its measurement in the calculation of the corrective quantity.
    As a variant or in combination, this corrective quantity is a fixed quantity or a percentage (fixed or variable) which is a function (which varies) according to the filling conditions and for example the final pressure.
    Thus, in the case where different tanks 2 are filled at different pressures, the corrective quantities determined may be different.
    The corrective determined quantity can correspond to a predetermined value corresponding to determined thermodynamic conditions: volume, temperature, pressure and / or density.
    The corrective determined quantity of gas can optionally also vary as a function of the temperature of the gas in the tank 2 to be filled or in the filling line 4.
    The corrective determined quantity of gas may possibly vary as a function of the volume of the tank 2 (known or measured) and / or of the known or measured volume of the filling circuit 4.
    The corrective determined quantity of gas can be the calculated or measured quantity of gas evacuated via the purge valve 10 or a fraction thereof.
    For example, the quantity of gas purged can be estimated from the known volume in the circuit 4 between the downstream isolation valve 6 and the downstream end 8, the pressure 15 measured in this part of the circuit 4, the measured temperature or estimated in this part of circuit 4, of the characteristics of the gas (its nature, its molar mass, etc.), and of the final pressure in line 4 after the transfer step and after the purge step. On the basis of these parameters the density and / or the mass of purged gas can be calculated.
    For example, the corrective determined quantity of gas is calculated by an equation of state (equation of ideal or real gases) applied to the gas in the downstream part of the filling pipe before the purging step and after the purging step from the following parameters: the known volume of the filling pipe downstream of the downstream isolation valve 6, the final pressure measured in the tank 2 to be filled or in the filling pipe 4 at the end of the transfer before the purging step, the measured or estimated temperature of the gas in the tank 2 to be filled or in the filling line 4, the known nature of the gas and in particular its molar mass, the pressure in the filling line 4 after l 'purge step. The corrective quantity can be the result of the difference between the calculated quantity of gas present in the downstream part of the filling pipe 4 before the purging step and the calculated quantity of gas present in the in the downstream part of the pipe 4 filling after the purge step.
    As illustrated in Figure 2, the station may include a second purge flow meter 11 located downstream of the purge valve 10 configured to measure the amount of gas purged during the purge step. The corrective determined quantity of gas is for example the quantity of gas measured by the purge flow meter 11 or a determined fraction thereof.
    As shown diagrammatically in the figures, the electronic device 12 for processing and storing data can comprise or be associated with a body 16 for counting pulses and a body 17 for correcting recorded pulses (this or these bodies 16, 17 may include electronic cards or any other suitable device).
    Of course the filling circuit 4 may comprise other element (s) and in particular valve (s) 7 upstream or downstream of the downstream isolation valve 6 and / or a buffer volume between the flow meter 9 and the valve 6 downstream insulation, an exchanger 19 for cooling the gas downstream of the downstream isolation valve 6, etc.
    权利要求:
    Claims (19)
    [1" id="c-fr-0001]
    1. Method for measuring the quantity of gas introduced into a gas tank (2) via a filling station (1) provided with a filling pipe (4) comprising an upstream end (3) connected to at least one source ( 5) of pressurized gas and a downstream end (8) connected to a tank (2) to be filled, the filling line (4) comprising a flow meter (9) and at least one downstream isolation valve (6) disposed between the flow meter and the downstream end (8) of the filling pipe, the method comprising a step of transferring gas from the source (5) to the tank (2) during which the downstream isolation valve (6) is open , a step of interrupting the transfer of gas with a valve closure (6) downstream, the method comprising a step of measurement, by the flow meter (5), of the quantity of gas transferred during the transfer step, the method being characterized in that it comprises a step of generating a signal for the quantity of corrected transferred gas, the qua The amount of corrected transferred gas being obtained by reducing or increasing by a corrective quantity the quantity of transferred gas measured by the flow meter (5) during the transfer step.
    [2" id="c-fr-0002]
    2. Method according to claim 1, characterized in that the flow meter (5) is of the type generating electrical signals in the form of successive pulses each corresponding to an elementary quantity of gas measured and in that the generation of a signal of corrected quantity of transferred gas is obtained by a modification step of at least one of: the value of the elementary quantity of gas corresponding to a pulse generated by the flow meter (5) and / or the number of pulses generated by the flow meter (5) and / or the transmission frequency of the pulses generated by the flow meter (5) and / or the number of pulses counted among the pulses generated by the flow meter (5).
    [3" id="c-fr-0003]
    3. Method according to claim 2, characterized in that the generation of a signal for the quantity of corrected transferred gas is obtained by subtracting or adding a determined quantity of pulses to the pulses generated by the flow meter (5).
    [4" id="c-fr-0004]
    4. Method according to any one of claims 2 to 3, characterized in that the modification step is carried out by modifying (by increasing or reducing) the frequency of the pulses generated by the flow meter (5), that is to say ie by removing or adding a determined duration to the time interval separating successive pulses generated by the flow meter (5).
    [5" id="c-fr-0005]
    5. Method according to any one of claims 1 to 4, characterized in that the corrective determined quantity of gas is a determined proportion of the quantity of gas measured by the flow meter (5) during the transfer step.
    [6" id="c-fr-0006]
    6. Method according to claim 5, characterized in that the determined proportion is fixed, that is to say independent of the operating conditions of the filling step or variable, that is to say dependent on the operating conditions of the filling step.
    [7" id="c-fr-0007]
    7. Method according to any one of claims 1 to 6, characterized in that the filling pipe (4) comprises, downstream of the downstream isolation valve (6), a controlled purge valve (10), the method includes a step of purging outside the pipe (4) for filling at least part of the pressurized gas trapped in the downstream part of the pipe (4) for filling after the transfer step.
    [8" id="c-fr-0008]
    8. Method according to claim 7 combined with any one of claims 1 to 5, characterized in that the corrective determined quantity of gas is a determined percentage of the quantity of gas evacuated during the purging step.
    [9" id="c-fr-0009]
    9. Method according to claim 8, characterized in that the percentage which varies as a function of the operating conditions of the filling step and in particular as a function of the pressure measured (15) in the transfer line (4) during the transfer step, said percentage being calculated regularly during the filling step and in particular at the end of the transfer step.
    [10" id="c-fr-0010]
    10. Method according to claim 9, characterized in that the percentage is proportional to the pressure in the transfer line (4).
    [11" id="c-fr-0011]
    11. Method according to one of claim 8 to 10, characterized in that the percentage is proportional to the difference (P-Pi) between on the one hand the pressure (P) in the line (4) of measured transfer (15 ) during the transfer step or at the end of the transfer step and, on the other hand, the pressure (Pi) in the transfer line after the purge step.
    [12" id="c-fr-0012]
    12. Method according to any one of claims 8 to 11, characterized in that the percentage is between 100% and 0% and preferably between 95% and 75%.
    [13" id="c-fr-0013]
    13. Method according to any one of claims 7 to 12, characterized in that the filling pipe (4) comprises a purge flow meter (11) configured to measure the quantity of gas evacuated during the purging step.
    [14" id="c-fr-0014]
    14. Method according to any one of claims 3 to 13, characterized in that the modification step is carried out during the transfer step.
    [15" id="c-fr-0015]
    15. The method of claim 14, characterized in that the modification step is carried out is carried out in a uniform time distribution during the transfer step.
    [16" id="c-fr-0016]
    16. Method according to any one of claims 1 to 15, characterized in that the modification step is carried out at the end or after the end of the transfer step.
    [17" id="c-fr-0017]
    17. Method according to any one of claims 1 to 16, characterized in that the filling station (1) comprises an electronic device (12) for processing and storing data, comprising in particular a microprocessor and / or a computer, said electronic device (12) being configured to receive a signal representative of the quantity of gas transferred measured by the flow meter (5) during the transfer step and to calculate and / or receive and / or transmit and / or display the corrected gas quantity signal.
    [18" id="c-fr-0018]
    18. Method according to any one of claims 1 to 17, characterized in that the corrected amount of transferred gas signal is used in a step of calculating a billing of the amount of gas introduced into the tank (2).
    [19" id="c-fr-0019]
    19.Filling station for pressurized fluid tanks, in particular for filling pressurized hydrogen tanks, comprising a filling pipe (4) comprising an upstream end (3) connected to at least one gas source (5) under pressure and at least
    5 a downstream end (8) intended for connection to a tank (2) to be filled, the filling pipe (4) comprising a flow meter (9) and at least one downstream isolation valve (6) disposed between the flow meter and the downstream end (8) of the filling pipe, the at least one valve (6) being controlled to allow a gas transfer step from the source (5) to the tank
    10 (2), the flow meter (5) being configured to measure the quantity of gas transferred and generate a corresponding signal in response, the station (1) comprising an electronic device (12) for processing and storing data, comprising in particular a microprocessor and / or computer, the electronic device (12) being configured to receive the signal from the flow meter and
    15 to generate a signal for the quantity of corrected transferred gas obtained by reducing or increasing by a determined corrective quantity the quantity of transferred gas measured by the flow meter (5) during the transfer.
    1/1
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    同族专利:
    公开号 | 公开日
    CN110621964A|2019-12-27|
    JP2020516868A|2020-06-11|
    CA3059181A1|2018-10-11|
    EP3607280A1|2020-02-12|
    KR20190138818A|2019-12-16|
    US20200041323A1|2020-02-06|
    FR3065069B1|2019-07-26|
    WO2018185401A1|2018-10-11|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    EP0813022A1|1996-06-14|1997-12-17|Provençale d'Automation et de Mécanique|Apparatus for filling bottles with liquefied petroleum gas|
    JP2006300156A|2005-04-19|2006-11-02|Tatsuno Corp|High-pressure gas charging device|
    JP2007024152A|2005-07-14|2007-02-01|Tokiko Techno Kk|Gas supply device|
    JP2014043882A|2012-08-27|2014-03-13|Tatsuno Corp|Gas charging apparatus|EP3715698A4|2019-02-01|2020-11-25|Iwatani Corporation|Hydrogen gas dispenser inspecting device|JP2015197190A|2014-04-02|2015-11-09|Ｊｘ日鉱日石エネルギー株式会社|Hydrogen gas charging facility|CN111486339A|2020-04-02|2020-08-04|北京科荣达航空设备科技有限公司|Automatic filling device for airplane oxygen cylinder|
    DE102020115645A1|2020-06-12|2021-12-16|Westenergie Ag|Method for determining an amount of hydrogen gas delivered to a vehicle at a hydrogen filling station|
    法律状态:
    2018-04-20| PLFP| Fee payment|Year of fee payment: 2 |
    2018-10-12| PLSC| Search report ready|Effective date: 20181012 |
    2019-04-18| PLFP| Fee payment|Year of fee payment: 3 |
    2020-04-20| PLFP| Fee payment|Year of fee payment: 4 |
    2021-04-23| PLFP| Fee payment|Year of fee payment: 5 |
    优先权:
    申请号 | 申请日 | 专利标题
    FR1753046A|FR3065069B1|2017-04-07|2017-04-07|METHOD FOR MEASURING THE QUANTITY OF GAS INTRODUCED INTO A RESERVOIR AND CORRESPONDING STATION|
    FR1753046|2017-04-07|FR1753046A| FR3065069B1|2017-04-07|2017-04-07|METHOD FOR MEASURING THE QUANTITY OF GAS INTRODUCED INTO A RESERVOIR AND CORRESPONDING STATION|
    CN201880031422.1A| CN110621964A|2017-04-07|2018-03-29|Method for measuring the amount of gas introduced into a reservoir and corresponding filling station|
    PCT/FR2018/050767| WO2018185401A1|2017-04-07|2018-03-29|Method for measuring the quantity of gas introduced into a reservoir and corresponding filling station|
    KR1020197032628A| KR20190138818A|2017-04-07|2018-03-29|A method for measuring the amount of gas introduced into the reservoir, and a corresponding filling station|
    EP18722656.8A| EP3607280A1|2017-04-07|2018-03-29|Method for measuring the quantity of gas introduced into a reservoir and corresponding filling station|
    US16/603,437| US20200041323A1|2017-04-07|2018-03-29|Method for measuring the quantity of gas introduced into a reservoir and corresponding filling station|
    JP2019554504A| JP2020516868A|2017-04-07|2018-03-29|Method and corresponding filling station for measuring the amount of gas introduced into a reservoir|
    CA3059181A| CA3059181A1|2017-04-07|2018-03-29|Method for measuring the quantity of gas introduced into a reservoir and corresponding filling station|
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