Classifications

• • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
  • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
  • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
  • F17C5/00—Methods or apparatus for filling containers with liquefied, solidified, or compressed gases under pressures
  • F17C5/02—Methods or apparatus for filling containers with liquefied, solidified, or compressed gases under pressures for filling with liquefied gases
• • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
  • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
  • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
  • F17C7/00—Methods or apparatus for discharging liquefied, solidified, or compressed gases from pressure vessels, not covered by another subclass
  • F17C7/02—Discharging liquefied gases
• • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
  • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
  • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
  • F17C2223/00—Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel
  • F17C2223/01—Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel characterised by the phase
  • F17C2223/0146—Two-phase
  • F17C2223/0153—Liquefied gas, e.g. LPG, GPL
  • F17C2223/0161—Liquefied gas, e.g. LPG, GPL cryogenic, e.g. LNG, GNL, PLNG
• • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
  • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
  • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
  • F17C2223/00—Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel
  • F17C2223/03—Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel characterised by the pressure level
  • F17C2223/033—Small pressure, e.g. for liquefied gas
• • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
  • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
  • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
  • F17C2223/00—Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel
  • F17C2223/03—Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel characterised by the pressure level
  • F17C2223/035—High pressure (>10 bar)
• • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
  • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
  • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
  • F17C2223/00—Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel
  • F17C2223/04—Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel characterised by other properties of handled fluid before transfer
  • F17C2223/042—Localisation of the removal point
  • F17C2223/046—Localisation of the removal point in the liquid
• • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
  • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
  • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
  • F17C2225/00—Handled fluid after transfer, i.e. state of fluid after transfer from the vessel
  • F17C2225/01—Handled fluid after transfer, i.e. state of fluid after transfer from the vessel characterised by the phase
  • F17C2225/0146—Two-phase
  • F17C2225/0153—Liquefied gas, e.g. LPG, GPL
  • F17C2225/0161—Liquefied gas, e.g. LPG, GPL cryogenic, e.g. LNG, GNL, PLNG
• • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
  • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
  • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
  • F17C2225/00—Handled fluid after transfer, i.e. state of fluid after transfer from the vessel
  • F17C2225/03—Handled fluid after transfer, i.e. state of fluid after transfer from the vessel characterised by the pressure level
  • F17C2225/035—High pressure, i.e. between 10 and 80 bars
• • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
  • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
  • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
  • F17C2227/00—Transfer of fluids, i.e. method or means for transferring the fluid; Heat exchange with the fluid
  • F17C2227/01—Propulsion of the fluid
  • F17C2227/0107—Propulsion of the fluid by pressurising the ullage
• • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
  • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
  • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
  • F17C2227/00—Transfer of fluids, i.e. method or means for transferring the fluid; Heat exchange with the fluid
  • F17C2227/01—Propulsion of the fluid
  • F17C2227/0128—Propulsion of the fluid with pumps or compressors
  • F17C2227/0135—Pumps
• • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
  • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
  • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
  • F17C2227/00—Transfer of fluids, i.e. method or means for transferring the fluid; Heat exchange with the fluid
  • F17C2227/04—Methods for emptying or filling
  • F17C2227/044—Methods for emptying or filling by purging
• • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
  • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
  • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
  • F17C2250/00—Accessories; Control means; Indicating, measuring or monitoring of parameters
  • F17C2250/03—Control means
  • F17C2250/032—Control means using computers
• • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
  • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
  • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
  • F17C2250/00—Accessories; Control means; Indicating, measuring or monitoring of parameters
  • F17C2250/04—Indicating or measuring of parameters as input values
  • F17C2250/0404—Parameters indicated or measured
  • F17C2250/043—Pressure
• • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
  • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
  • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
  • F17C2250/00—Accessories; Control means; Indicating, measuring or monitoring of parameters
  • F17C2250/04—Indicating or measuring of parameters as input values
  • F17C2250/0404—Parameters indicated or measured
  • F17C2250/0439—Temperature
• • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
  • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
  • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
  • F17C2250/00—Accessories; Control means; Indicating, measuring or monitoring of parameters
  • F17C2250/04—Indicating or measuring of parameters as input values
  • F17C2250/0404—Parameters indicated or measured
  • F17C2250/0443—Flow or movement of content
• • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
  • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
  • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
  • F17C2250/00—Accessories; Control means; Indicating, measuring or monitoring of parameters
  • F17C2250/04—Indicating or measuring of parameters as input values
  • F17C2250/0486—Indicating or measuring characterised by the location
  • F17C2250/0491—Parameters measured at or inside the vessel
• • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
  • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
  • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
  • F17C2250/00—Accessories; Control means; Indicating, measuring or monitoring of parameters
  • F17C2250/06—Controlling or regulating of parameters as output values
  • F17C2250/0605—Parameters
  • F17C2250/0636—Flow or movement of content
• • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
  • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
  • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
  • F17C2260/00—Purposes of gas storage and gas handling
  • F17C2260/02—Improving properties related to fluid or fluid transfer
  • F17C2260/021—Avoiding over pressurising
• • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
  • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
  • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
  • F17C2260/00—Purposes of gas storage and gas handling
  • F17C2260/02—Improving properties related to fluid or fluid transfer
  • F17C2260/025—Reducing transfer time
• • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
  • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
  • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
  • F17C2265/00—Effects achieved by gas storage or gas handling
  • F17C2265/06—Fluid distribution
  • F17C2265/063—Fluid distribution for supply of refueling stations
• • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
  • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
  • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
  • F17C2270/00—Applications
  • F17C2270/01—Applications for fluid transport or storage
  • F17C2270/0134—Applications for fluid transport or storage placed above the ground
  • F17C2270/0139—Fuel stations
• • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
  • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
  • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
  • F17C2270/00—Applications
  • F17C2270/01—Applications for fluid transport or storage
  • F17C2270/0165—Applications for fluid transport or storage on the road
  • F17C2270/0168—Applications for fluid transport or storage on the road by vehicles
  • F17C2270/0171—Trucks

Definitions

• the present invention relates to a method and filling device.
• the invention relates more particularly to a method for filling a liquefied gas tank, in particular a cryogenic liquid tank, from a liquefied gas tank, in particular a cryogenic liquid tank, the tank being fluidly connected to the tank via a filling line, the method using a pressure differential generating member for selectively transferring liquid from the tank to the tank, the pressure differential generating member being switchable in a running state or in a a stopping state, the filling line comprising a liquid flow regulating member disposed downstream of the differential generating member, the flow regulating member being movable between a non-conducting position in which the flow of liquid is interrupted and at least one passing position in which the flow of liquid is transferred to the selo tank n a determined flow rate, the method comprising a step of starting the filling during which the flow control member is moved from the non-conducting position to a passing position and a measurement of a first instantaneous pressure in the downstream
• the invention can be applied to the filling of any cryogenic container (mobile or otherwise) from any other cryogenic container (mobile or otherwise).
• the receiving tank and / or the filling device It is thus necessary to equip the receiving tank and / or the filling device with a safety system preventing overfilling or excessive pressure buildup of the tank which would cause the latter to break.
• the number of tanks to be filled is significantly greater than the number of filling devices, the safety system is preferably applied to the filling devices.
• a known solution consists in equipping the filling port of the reservoir with a pneumatic valve which closes when the pressure in the reservoir reaches a predetermined threshold.
• this solution has drawbacks among which the need to provide maintenance of this pneumatic valve, a high cost of installation on all tanks requiring protection.
• Another known solution is to provide a calibrated orifice at the filling port of the tank to maintain the filling rate in secure ranges, typically at a rate that can be evacuated by the existing security organs of the storage. This solution is also installed on the tanks and penalizes the filling time.
• Another solution consists in providing an electrical system for detecting overpressure at the reservoir (if necessary via a thermistor at the overflow gauge valve) which, in response, stops the filling pump.
• This solution requires a specific connection between each tank and each filling device and if necessary is based on an action by the operator.
• Another solution consists in providing specific fluidic connections between filling devices and the reservoirs according to determined pressure ranges. This solution imposes obvious constraints in terms of logistics in particular.
• US6212719 discloses a system for automatically stopping a filling pump in case of rupture of the supply hose via two pressure sensors arranged at both ends of the transfer hose. The detection of a pressure drop triggers the shutdown of the pump.
• An object of the present invention is to overcome all or part of the disadvantages of the prior art noted above.
• the method according to the invention is essentially characterized in that, after a determined duration following the start of filling, the method comprises a comparison from the first instantaneous pressure in the filling line or an average of this first instantaneous pressure with a determined high threshold and, when the first instantaneous pressure in the filling line or, respectively, the average of the first instantaneous pressure, exceeds the high threshold, a step of interrupting the filling.
• embodiments of the invention may include one or more of the following features:
• the flow regulator comprises or consists of a valve, for example a valve with variable opening,
• the first pressure in the filling line is measured when the latter communicates with the inside of the tank, ie the filling line is passing between the measuring point of the first pressure and the inside the tank,
• the determination of the first reference instantaneous pressure (PT3ref) or, respectively, the average of the instantaneous pressures (mPT3ref) of reference, in the filling line is carried out at least a first time via a measurement of the first pressure (PT3) instantaneous in the pipe, respectively of an average (mPT3) of this instantaneous first pressure (PT3), in a determined time interval between zero and 180 seconds around at least one of the following events: the switching of the stopped state (AR) in the operating state (M) of the differential generation member, the beginning of a transfer of fluid from the tank to the tank, - after the determination of the first reference instantaneous pressure (PT3ref), respectively of the average of the instantaneous pressures (mPT3ref) of reference, and during filling, the first instantaneous pressure (PT3) in the pipe is measured regularly and, if the first instantaneous pressure (PT3) measured in the pipe or its mean respectively becomes lower than the first reference pressure (PT3ref) previously selected or,
• a new high threshold (Pmax) is calculated for each measured drop in the first instantaneous pressure (PT3) below the first current reference instantaneous reference pressure (PT3ref), respectively, respectively, with each measured decrease of the reference average (mPT3) below the current reference average (mPT3ref) previously retained,
• the step of determining the first reference instantaneous pressure (PT3ref) in the filling line comprises at least one measurement of the first instantaneous pressure (PT3) in the pipe in a time interval of between zero and 180 seconds after a switching on (M) the generating member of a pressure differential or in a specified time interval between zero and 180 seconds after starting the actual transfer of a flow of liquid to the reservoir, the first pressure (PT3ref) reference instant being the value measured during the at least one pressure measurement or an average of this at least one pressure measurement,
• the step of interrupting the filling comprises at least one of: reducing or stopping the circulation of liquid in the filling line, stopping the generating member of a pressure differential , a purge of at least a portion of the filling line to a separate discharge zone of the tank, the activation of a by-pass returning liquid flowing in the filling line to the tank, the emission of a visual and / or audible alarm,
• the pressure differential generating member comprises at least one of: a pump, a selective pressurizing vaporizer of the tank, is selectively switchable between a running state and a stopping state, the method comprising starting up the pressure differential generating member and causing the pressure differential generating member to switch to its off state automatically in response to one of the less situations among: the variation of the first instantaneous pressure (PT3) in the filling line for a determined duration before effective transfer of a flow of liquid towards the reservoir is greater than a variation (V) determined (APT3> V),
• the first instantaneous pressure (PT3) in the pipe remains higher than a determined high level
• the differential (PT2-PT3) between on the one hand, a second instantaneous pressure (PT2) measured at the output of the generating member of a pressure differential, upstream of the flow control member and on the other hand, the first instantaneous pressure (PT3) measured in the pipe downstream of the flow control member is less than a minimum differential preferably of between 0.5 bar and 2bar, a fall of the first pressure ( PT3) of at least one bar per second is measured corresponding in particular to a rupture of the filling pipe
• the method comprises starting (M) the pressure differential generating member, the interrupting (AR) step of filling when the first instantaneous pressure (PT3) or, respectively, the average of instantaneous pressure (mPT3) in the filling line, exceeds the high threshold (Pmax), being carried out only after a step (A) of delay provided in particular to allow the stabilization of the liquid transfer conditions to the reservoir , step (A) of delay starting at start-up of the generating member of a pressure differential or during the passage of the regulating member in the passing position, and having a finite duration determined,
• the method comprises a measurement of the so-called "reference" value of the instantaneous first pressure (PT3ref) or of an average of the reference instantaneous pressure (mPT3ref) in the filling line, and, when the reference instantaneous pressure (PT3ref) or the average of the instantaneous pressures (mPT3ref) of reference is greater than a predetermined low value and less than a predetermined high value, the high threshold (Pmax) is less than or equal to twice and preferably less than one and a half times the value of the first reference pressure (PT3ref) or, respectively, the average of the instantaneous pressures (mPT3ref) of reference (Pmax ⁇ 2PT3ref, and preferably Pmax ⁇ 1, 5PT3ref respectively Pmax ⁇ 2mPT3ref and preferably Pmax ⁇ 1, 5mPT3ref), the predetermined low value being preferably between three and five bar, the predetermined high value As preferably between nineteen and twenty
• the member for generating a pressure differential comprises at least one of: a pump, a heater, a vaporizer,
• the start of the filling corresponds to at least one of: starting the pressure differential generating member, the beginning of the actual fluid transfer from the tank (2) to the reservoir,
• the filling line comprises in series, from upstream to downstream, the pressure differential generating member, a second pressure sensor, the liquid flow control member in the filling line and the first Pressure sensor,
• the filling line further comprises a fluid flow measuring member, located between the first and second pressure sensors, the duration of the delaying step is between five and one hundred and eighty seconds and preferably between ten and one hundred and twenty seconds and even more preferably between thirty and ninety seconds,
• the start-up of the pressure differential generating member comprises a control of the liquid flow delivered by the pressure differential generating member for maintaining the instantaneous liquid flow rate in the filling line; downstream of the generating member of a pressure differential above a determined minimum flow rate,
• the first instantaneous pressure (PT3) in the filling line is maintained above a determined minimum pressure threshold (PT3min),
• the method comprises, during the start of filling, a step of comparing an average of the first instantaneous pressure (PT3) in the filling line with the determined high threshold (Pmax) and, when the average of first pressure (PT3) ) instant exceeds the high threshold, a step of automatic interruption of the filling, the average of the first instantaneous pressure (PT3) being the average of several values of the first instantaneous pressure (PT3) measured successively during a time interval between 0 , 1 and 10 seconds and preferably between 0.25 seconds and 1 second,
• the method comprises, at the end of step (A) of delaying, a step of comparing an average of the first instantaneous pressure (PT3) in the filling pipe with high threshold (Pmax) determined and, when the average of the first instantaneous pressure (mPT3) exceeds the high threshold, a step of automatic interruption of the filling, the average of the first instantaneous pressure (PT3) being the average of several first instantaneous pressures (PT3) measured successively during an interval a time of between 0.1 and 10 seconds and preferably between 0.25 seconds and 1 second, the reference instantaneous pressure determining step PT3ref in the filling line comprises at least one measurement of the first instantaneous pressure (PT3) in the pipe in a time interval of between zero and ten seconds around the switching on the generating member of a pressure differential or around the end of the delay step (A), the reference instantaneous pressure (PT3ref) in the filling line being the value measured during the at least one pressure measurement or an average of this at least one pressure measurement,
• the value of the pressure jump is a fixed value which may or may not be adjustable and is between 0.1 bar and 2 bar and preferably between 0.3 and 1 bar and even more preferably between 0.4 and 0.6 bar,
• the step of measuring the instantaneous first pressure (PT3) in the filling line downstream of the pressure differential generating member is carried out continuously or periodically,
• the value of the pressure jump is a function of the value of the first reference instantaneous pressure (PT3ref)
• the pressure jump is between 0.1 and 0.9bar and preferably between 0.3 and 0.7 bar.
• the pressure jump is between 0.8 and 1.4 bar and preferably between 0.9 and 1.2 bar
• the pressure jump is between 1, 2 and 2bar and preferably between 1, 2 and 1, 7bar
• the pump is stopped by switching the pump in a passive mode, in particular by stopping its drive motor and / or by closing at least one controlled valve,
• the possible variations of the first instantaneous pressure (PT3) measured in the filling line or the variations of the average of these first instantaneous pressures (PT3) measured above the high threshold (Pmax) do not trigger not stopping the filling, the pressure in the tank is maintained above a determined value via a liquid withdrawal from the tank, the vaporization of this liquid taken and the reinjection of the vaporized liquid into the tank,
• the fluid pressure in the filling line downstream of the pressure differential generating member is maintained above the pressure value (PT4) in the reservoir by decreasing / interrupting the direct return of fluid from the device for generating a differential pressure towards the tank,
• the filling pipe comprises an integral upstream portion of the tank and a downstream portion, the downstream portion is preferably flexible and has a first end removably connected to the upstream portion and a second downstream end removably connected to an inlet filling the tank,
• the flow regulator comprises or consists of a variable opening valve
• the measurement of the first instantaneous pressure (PT3) in the filling line downstream of the pressure differential generating member is carried out via at least a first pressure sensor
• the method is implemented by an installation comprising an electronic logic receiving the measurements of the first instantaneous pressure (PT3) in the filling line, the electronic logic ensuring the control of the operation of the generating member of a differential of pressure,
• PT3 first instantaneous pressure
• the filling line is provided with a variable opening valve arranged downstream of the pressure differential generating member, for regulating the flow of liquid delivered to the reservoir, said variable opening valve being preferably of the type one-way, that is to say preventing the backflow of fluid upstream to the pressure differential generating member,
• the flowrate of fluid transferred to the reservoir is regulated via said variable opening valve disposed downstream of the pressure differential generating member,
• the pressure differential generation member can only be restarted after a determined waiting period preferably comprised between one second and fifteen minutes,
• the start of the pressure differential generating member is prevented when the measurement of the first instantaneous pressure (PT3) in the filling line downstream of the pump is unavailable, at least one of the following steps is performed automatically or manually: the step of measuring the first instantaneous pressure (PT3) in the filling line downstream of the pressure differential generating member, step (A) of delaying, the step of comparing the first instantaneous pressure (PT3) in the filling line with a determined high pressure threshold (Pmax), the step of interrupting the filling, the stability control the first pressure,
• the selective purge of at least a portion of the filling line to a separate discharge zone of the tank uses a discharge pipe comprising an end open to the atmosphere, said discharge pipe being provided with a valve said selective purge being carried out during a specified purge time of between two and sixty seconds and preferably between five and thirty seconds,
• the by-pass selectively returning the liquid exiting the pump to the tank comprises a pipe (8) provided with at least one bypass valve,
• the step of interrupting the filling by activation of the bypass returning the liquid downstream of the pump to the tank comprises an opening of the at least one bypass valve for a predetermined period preferably between two and sixty seconds
• the start of the pressure differential generation member is possible only after a first positive stability check of the first instantaneous pressure (PT3) in the filling line, the first control the stability of the pressure being positive if the first pressure (PT3) is greater than the atmospheric pressure and at least one of the following conditions is met:
• the first instantaneous pressure (PT3) in line (3) is greater than a predetermined pressure, for example between 15 and 25 bar,
• the variation of the first instantaneous pressure (PT3) during at least one determined interval is less than a determined level of variation corresponding for example to a variation of between 0.005 and 0.020 bar per second,
• the maximum pressure threshold is a predetermined fixed pressure value of between 5 and 9 bar and preferably equal to between 5.2 and 7 bar
• the step of limiting the first instantaneous pressure (PT3) below a maximum pressure threshold (PT3sup) comprises at least one of: manual or automatic regulation of the flow of fluid transferred via the regulating member flow, a manual or automatic regulation of the pressure differential generated by the pressure differential generating member,
• the step of limiting the first instantaneous pressure (PT3) below the maximum pressure threshold (PT3sup) is carried out for a finite determined duration of limitation and in that, when the first instantaneous pressure (PT3) remains above the threshold maximum pressure (PT3sup) at the end of the determined limitation period, the filling is interrupted (AR) automatically,
• the determined limitation period is between fifteen and two hundred seconds and preferably between thirty and one hundred and eighty seconds and for example between fifteen and sixty seconds or for example equal to ninety seconds,
• the method comprises measuring the quantity (Q) of fluid transferred from the tank (2) to the tank (1) and that, when this quantity of fluid (Q) transferred exceeds a threshold quantity (Qs) before the end of the determined limitation period, said limitation period initially provided is reduced,
• the invention also relates to a device for filling a liquefied gas tank comprising a cryogenic liquid tank, the tank being selectively fluidically connected to the tank via a filling line having a first upstream end connected to the tank and a second downstream end.
• the device comprising a pressure differential generating member for transferring liquid from the tank to the tank via a filling line, a liquid flow control member in the filling line, the flow regulating member being movable between a non-conducting position in which the flow of liquid is interrupted and at least one passing position in which the flow of liquid is transferred to the reservoir according to a determined respective flow, the device further comprising a first pressure sensor disposed on the downstream filling line the flow control member and an electronic logic connected to the pressure differential generating member, the first pressure sensor and at least one selector or selectively interrupting the filling, the electronic logic being configured to perform during filling, after a predetermined period of time following the start of the transfer of a flow of liquid to the reservoir, a comparison of the first pressure instantaneous or an average of this first instantaneous pressure (PT3) with a determined high threshold (Pmax) and, when the first instantaneous pressure (PT3) or, respectively, the average of the first instantaneous pressures (PT3)
• the at least one limiting or interrupting element comprises at least one of:
• a purge pipe provided with a controlled valve and connected to the electronic logic, the purge pipe comprising a first end connected to the filling pipe and a second end opening into a separate discharge zone of the tank,
• bypass pipe provided with a controlled valve and connected to the electronic logic, the bypass pipe comprising a first end connected to the filling pipe and a second end opening into the tank,
• a controlled isolation valve connected to the electronic logic.
• the invention may also relate to any alternative device or method comprising any combination of the above or below features.
• FIG. 1 represents a schematic and partial view illustrating a first example of structure and operation of a device for filling a tank according to the invention
• FIG. 2 represents a schematic and partial view illustrating a second example of structure and operation of a filling device according to the invention
• FIGS. 3 to 8 show schematic, simplified and partial views respectively illustrating six other possible embodiments of structure and operation of a filling device according to the invention
• FIG. 9 represents a schematic and partial view illustrating yet another example of structure and operation of a filling device according to the invention.
• FIG. 10 illustrates a first possible example of a succession of steps implemented during a filling according to one embodiment of the invention
• FIG. 11 illustrates a second example of a succession of steps that can be implemented during a filling according to one embodiment of the invention
• FIG. 12 illustrates a third example of a succession of steps that can be implemented during a filling according to one embodiment of the invention
• FIG. 13 shows a schematic, simplified and partial view similar to Figures 3 to 8 illustrating yet another possible embodiment of structure and operation of a filling device according to the invention.
• FIGS. 1 and 9 illustrate in simplified manner an example of a filling installation that can be used according to the invention.
• the filling device comprises a tank 2 of cryogenic liquid.
• This tank 2 is for example a double-walled tank whose inter-wall is isolated under vacuum.
• the tank 2 is for example mobile and transportable if necessary on a delivery truck such as a semi-trailer.
• the tank 2 contains liquefied gas and can be selectively fluidically connected to a tank 1 to be filled via a filling line 3.
• the filling pipe 3 comprises an upstream end connected to the storage volume of the tank 2 and a downstream end selectively connectable to the tank 1.
• the filling line 3 is provided with a member 4 for generating a fluid pressure differential and, downstream of the latter, a valve 12 with variable opening.
• the member 4 for generating a pressure differential is a pump.
• the member for generating a pressure differential may conventionally comprise a vaporizer and / or a heater associated with at least one valve making it possible to increase the pressure in the tank 2 and to allow its transfer to a tank. Any other member for generating a pressure differential for causing the transfer of fluid from the tank 2 to the tank 1 can also be used.
• the member 4 for generating a pressure differential can be controlled to vary its power, that is to say to increase or decrease the level of pressure differential generated (for example by controlling the power of the pump or rise in pressure in the tank 2).
• the valve 12 with variable opening is preferably a manually operated valve (although this is not limiting for all that).
• the device further comprises a first pressure sensor 13 disposed on the filling pipe 3 downstream of the variable opening valve 12.
• the filling pipe 3 communicates fluidly with the inside of the tank 1, that is to say that the pipe is passing at least between the pressure sensor 13 and the inside of the tank 1, the sensor 13 measures a pressure representative of the PT4 pressure in the tank 1.
• the device further comprises an electronic logic 16 connected to the pump 4 and the pressure sensor 13.
• the electronic logic 16 comprises for example a microprocessor and an associated memory.
• the electronic logic 16 may be connected to at least one controlled valve 128, 12 located on the filling pipe 3.
• the pressure differential generating member comprises a vaporizer 11 located in a pressurization pipe 10 associated with a valve 128 in order to increase the pressure in the tank 2.
• the increase in pressure is carried out by withdrawing liquid from the tank 2, vaporizing it and reintroducing it into the tank 2.
• This rise in pressure in the tank generates a pressure differential which makes it possible to create a flow of liquid in the tank 2.
• the actual filling and stopping of the filling can be defined by the state or not of a valve 12 on the pipe 3 filling.
• the electronic logic 16 is configured to control or detect an M start or an AR stop of the generation member 4 of a pressure differential.
• the operating state M or AR stop can respectively correspond to the on or off state of its drive motor.
• the on and off state can correspond to the open / closed state of at least one valve or the actual pressurization or tanker 2. The following description concerns the case of a pump but can be applied by analogy to the case of another member for generating a pressure differential.
• the electronic logic 16 controls the start-up M of the pump 4 (see step 100, FIG. 10) and can trigger an optional delay A to allow in particular the stabilization of the liquid transfer conditions towards the reservoir 1.
• the control logic 16 receives as input parameter the start-up information M of the pump and / or the opening information of at least one controlled valve 12, 128.
• the delay step A (see FIG. 10, FIG. 10) preferably starts when the pump 4 is turned on and has a finite duration.
• the electronic logic 16 can be configured to interrupt automatically the filling AR R as soon as the first instantaneous pressure PT3 measured in the filling line 3 during the filling exceeds a predetermined high threshold Pmax (see references 103 "O" and 104, Figure 10).
• step A of delaying the variations of the first pressure PT3 in the filling line 3 beyond the high threshold Pmax do not interrupt the filling (reference 102, FIG. 10).
• This configuration makes it possible to detect effectively and early enough an overflow at the tank 1 that can lead to an overpressure in the reservoir 1 during filling without the need for expensive auxiliary systems for detection or communication.
• the inventors have in fact found that this configuration also makes it possible to avoid untimely detections of overfilling.
• the operator is not forced to additional operations during a filling.
• This configuration also contributes to stabilizing the tank filling conditions. This makes it possible to increase the life of the equipment by reducing harmful pressure variations.
• the electronic logic 16 can be configured to control an average of first instantaneous pressures PT3max measured in the filling line 3 . That is to say that the device controls the stop filling as soon as this average of first pressure PT3 exceeds a predetermined high threshold Pmax.
• the filling device preferably comprises a return line 8 (or bypass) provided with a bypass valve.
• the bypass pipe 8 comprises a first end connected to the filling pipe 3 downstream of the pump 4 and a second end opening into the tank 2 for selectively returning pumped liquid.
• the filling device may comprise a pipe 10 for selective pressurization of the tank 2.
• the pressurizing pipe 10 may comprise two first ends connected to the filling pipe 3 respectively upstream and downstream of the pump 4 (cf. Figures 1 and 2).
• the pressurizing line comprises a second end connected to the storage volume of the tank 2.
• the pressurizing line comprises a heat exchanger 11 for selectively vaporizing the pumped liquid before it is reintroduced into the tank 2.
• the filling pipe 3 may comprise an upstream portion 20 integral with the tank 2 and a downstream portion 30.
• the downstream portion 30 is preferably flexible and has a first end 14 removably connected to the portion upstream 20 and a second downstream end 15 demountably connected to a filling inlet of the tank 1.
• the downstream circuitry 40 of the second end 15 of the downstream portion 30 may comprise a check valve 1 19 preventing the backflow of fluid from the tank 1 to the filling pipe 3.
• the circuitry 40 may then comprise two lines 21, 22 respectively connected to the lower and upper parts of the tank 1 via respective valves 121, 122.
• the tank 1 is for example a vacuum insulated cryogenic tank.
• the tank 1 also preferably comprises a lower pressure measurement system 25 and a higher pressure measurement system 24 (or a system for measuring a pressure differential between the parts).
• a lower pressure measurement system 25 and a higher pressure measurement system 24 (or a system for measuring a pressure differential between the parts).
• FIG. 2 illustrates another more detailed example of a filling device architecture corresponding in particular to the upstream portion 20 of the filling line of FIG. 1.
• the filling pipe 3 is connected to the lower part of the tank 2 and may comprise, from upstream to downstream (that is to say from the tank 2 towards the end connected to a hose), a first 1 1 1 and a second 107 valves arranged in series upstream of the pump 4. As shown, a safety valve 207 and a filter 26 may be arranged upstream of the pump 4. Downstream of the pump 4, the pipe 3 filling comprises the valve 12 with variable opening. As shown, between the pump 4 and the valve 12 with variable opening, the filling pipe 3 may comprise at least one of: a temperature sensor 27 and a flow measurement member 9 such as a flow meter. Downstream of the variable opening valve 12, the pipe preferably comprises the first pressure sensor 13 mentioned above.
• the filling line 3 may also comprise, downstream of the first pressure sensor 13, a purge line 60 provided with at least one controlled valve 6 for discharging liquid to a discharge zone 18.
• a bypass pipe 28 may be provided to pressurize the tank via the pump 4.
• This bypass pipe 28 comprises an upstream end connected downstream of the pump 4 and a downstream end connected to the tank 2.
• the bypass pipe 28 comprises for example two pump bypass valves 128, 228 arranged in series.
• the device comprises a pipe 10 for selective pressurization of the tank 2.
• the pressurizing pipe 10 comprises a first end connected between the two pump bypass valves 128, 228 and one end. downstream connected to the tank 2.
• downstream end of the pressurizing pipe 10 may also be connected to a discharge line 17 having a discharge valve 310 and a valve 410.
• a bypass line 8 is provided for selectively returning the pumped liquid to the tank 2.
• the bypass pipe 8 has an upstream end connected to the filling pipe 3, downstream of the pump 4 (by example between the temperature sensor 27 and the optional flow meter 9).
• the bypass pipe 8 has a downstream end connected to the tank 2.
• the bypass pipe 8 comprises at least one bypass valve 5 and, in the example shown, two valves 5, 55 arranged in parallel, the valve 55 being preferably controlled.
• the bypass line 8 may comprise a pressure sensor 1 13 PT2 upstream of the valves 5, 55 by-pass. This sensor actually measures a second pressure PT2 in the filling line 3 upstream of the valve 12 with variable opening and downstream of the member 4 for generating a pressure differential.
• By-pass line 8 optionally includes another PT50 pressure sensor 29 disposed downstream of the bypass valves 5, 55.
• the circuit Downstream of the first valve 1 1 1, the circuit may comprise a pipe
• This pipe 21 1 to fill the tank 2 which is parallel to the pipe 3 filling.
• This pipe 21 1 comprises, from upstream to downstream, a first safety valve 41 1, a valve 31 1, a second safety valve 51 1 and an end 61 1 connectable to an application.
• This pipe 21 1 can be connected to the bypass line 8, downstream of the bypass valves 5, 55 via a branch 31.
• the filling operation of a tank 1 is at least partially manual and in particular an operator can manually control the valve 12 with variable opening.
• all or part of these actions can be automated, in particular by using appropriate controlled devices (valve controlled in particular).
• the pump 4 is of the type delivering a rate controlled by a frequency converter, including a centrifugal type pump.
• a frequency converter including a centrifugal type pump.
• any other type of pump is also appropriate.
• the pump 4 Before starting the filling, if the pump model 4 requires it, the pump 4 is first cooled and stabilized for a determined period of time. To do this, the operator can return the liquid pumped via the bypass line 8 to the tank 2 (for example by opening the bypass valve 5 and keeping the variable opening valve 12 closed).
• the operator can gradually close the bypass valve 5 and begin the actual filling of the tank by opening the valve 12 with variable opening (examples of stabilized operating conditions of the pump 4 will be described below. after).
• the first instantaneous PT3 pressure on the filling line 3 is measured downstream of the variable opening valve 12 via the first sensor 13.
• the first pressure PT3 in the filling line 3 is preferably maintained higher than the pressure in the tank 1 to be filled and the pressure in the tank 2 is also maintained above a minimum value.
• the delaying step A has for example a duration of between five and one hundred and eighty seconds and preferably between ten and ninety seconds and even more preferably between thirty and sixty seconds. This duration of the delay step A is preferably chosen as a function, in particular, of the technical characteristics of the pump 4 and the procedures necessary to control it.
• an abnormal increase of the first pressure PT3 can be detected by monitoring the first instantaneous pressure PT3.
• the device can determine a first reference instantaneous pressure PT3ref in line 3.
• the high threshold Pmax can be defined as being the sum of the part of the first pressure PT3ref instantaneous reference reference and, secondly, a determined pressure jump Po. That is to say that the high threshold Pmax (in bar) which triggers the stop of filling is given by:
• the determination of the first reference instantaneous pressure PT3ref can comprise at least one measurement of the first instantaneous pressure PT3 in the line 3 in a time interval comprised between zero and ten seconds around the end of the delaying step A.
• This first instant reference pressure PT3ref can be a point value, a maximum or minimum value measured by the sensor 13 during the at least one measurement or an average of several measurements.
• the value of the pressure jump Po can itself be a value (in bar) fixed in bar and between 0.1 bar and 2 bar and preferably between 0.3 and 1 bar and even more preferentially between 0.4 and 0.6 bar.
• the value of the pressure jump Po and the duration of the delay step can be adjusted according to the characteristics of the filling device (type of pump, type of circuit, type of tank, etc.).
• the value of the pressure jump is a function of the value of the first instantaneous reference pressure PT3ref.
• This pressure jump Po is defined according to the characteristics of the filling device. Thus, for example, if after step A of delaying the device is stabilized and that the first pressure PT3 downstream of the variable opening valve 12 reaches 9.5 bar and the pressure jump is defined at 0.5bar, so
• the device can control an average mPT3ref of the first instantaneous pressures PT3ref maximum measured by the sensor 13. That is to say that the device calculates an average mPT3ref of the first instant maximum pressure PT3 measured.
• the average of the first instantaneous pressure mPT3 is, for example, the average of several instantaneous pressures PT3 measured successively during a determined time interval.
• control of an overpressure can use other parameters that result from the first measured pressure PT3.
• the first measured pressure PT3 (respectively the mean of the first pressure mPT3) should decrease below the reference value PT3ref retained (respectively mPT3ref)
• this new value of reference PT3refb replaces the previous value (see steps 105 and 106 figure 10).
• This new high threshold which is reduced compared to the previous high threshold, thus adapts to a decrease in the first pressure PT3 during filling, in particular due to the thermodynamic conditions of the filling.
• the first pressure PT3 does not decrease ("N reference 105 in FIG. 10)
• the high threshold Pmax is unchanged.
• the first measured measured reference pressure PT3ref is the most recent minimum measured value.
• This decrease of the high threshold Pmax can be updated as often as necessary.
• This calculation of the high threshold Pmax, the monitoring of not exceeding the high threshold Pmax and the stopping if necessary of the filling can be carried out automatically by the electronic logic 16. In a non preferred variant, it could be envisaged that the exceeding of the high threshold Pmax is signaled to the operator who will then have the task of stopping the filling.
• the electronic logic 16 preferably controls the automatic shutdown of the filling.
• FIG. 3 represents the electronic logic 16 connected to the first pressure sensor 13 and to the pump 4.
• the electronic logic 16 is also connected, if appropriate, to a display member 7 such as a man-machine interface for signaling. all or part of the operating state of the device during filling.
• the operation of the pump 4 can be interrupted. That is to say that the control setpoint of the pump 4 is reduced to a minimum and / or the motor of the pump 4 is switched from a running state to a stopped state and / or a pump member 4 driven by a motor is disconnected from the motor of the pump 4 (set "freewheeling"). If necessary the control of the pump 4 is achieved via a speed converter (not shown for the sake of simplification). In the absence of pump 4, the interruption of filling can be obtained by closing the valve 12 with variable opening.
• stopping the filling can be achieved by decreasing or eliminating the circulation of liquid in the filling line 3 upstream of the pump 4. As illustrated in FIG. be achieved by closing a valve 1 1 1 of the filling line (for example the first valve 1 1 1 or the second valve 1 12 of Figure 2).
• This measurement used in a complementary manner to the shutdown of the pump 4, makes it possible to increase the efficiency of the stoppage of the filling, in particular by reducing the effect of inertia of the system and in particular the inertia of the pump 4. Indeed, even after stopping the pump 4 can continue to provide liquid for a time. This feature also makes it possible to reduce the possible effects of a vaporization of cryogenic liquid present in the circuit.
• stopping the filling can be achieved by purging at least a portion of the filling line 3 downstream of the pump 4 to a separate discharge zone 18 of the tank 1.
• the device may comprise, for this purpose, downstream of the pump 4, a purge line 60 provided with at least one valve 6 controlled by the electronic logic 16 for discharging liquid to an evacuation zone 18.
• This characteristic thus makes it possible to drain at least cryogenic fluid into the filling line 3 to the atmosphere.
• the purge 4 is preferably carried out during a limited purge period of for example between two and sixty seconds and preferably between five and thirty seconds.
• the purge time can be adapted according to the characteristics of the purge valve (typically the flow coefficient Cv of the valve) and those of the pipe to be purged (typically length and diameter). This makes it possible in particular to limit the risk of hypoxia of the operators depending on the nature of the gas released. This purge thus makes it possible at least partially to empty, in particular, the downstream portion of the filling pipe 3, in particular in the flexible part.
• the stop filling can be achieved by activating a by-pass returning the liquid downstream of the pump 4 to the tank 2. As shown in Figure 6, this can be achieved by opening the bypass controlled valve 55 of the bypass line 8.
• This solution also increases the efficiency and speed of stopping the filling and avoids rejecting a dangerous fluid around the tank 2.
• valve 12 with variable opening is of the type preventing the return of fluid upstream, this return of fluid to the tank 2 does not make it possible to evacuate the fraction of fluid present downstream of this valve 12. However, this characteristic still makes it possible to improve the stopping of the rise in pressure in the tank 1.
• this opening of the bypass valve 8 of the bypass line 8 is preferably performed for a limited period, for example between two and sixty seconds and preferably between two and thirty seconds.
• the device avoids any risk of cavitation of the pump 4 and any risk of fluid return from the tank 1 to the tank 2 in the case where the valve 12 variable opening leaks.
• the electronic logic 16 or the pump 4 itself prevents a restart of the pump 4 after a determined waiting time preferably between one second and fifteen minutes.
• the device described above While being simple and inexpensive structure, the device described above and allows to detect sufficiently rapidly and non-inadvertently abnormally high pressure in the tank 1 during filling.
• the device also makes it possible to limit this abnormally high pressure by effectively stopping the filling to avoid a rupture of the tank 1.
• the device can perform a stability check 301 ST of the first pressure PT3 in the filling line 3 (reference 301, Figure 1 1) .
• This first pressure PT3 is the one measured while the filling pipe communicates with the interior of the tank 1. That is to say that this first measured pressure PT3 then reflects the pressure in the tank 1 to fill (opening of the valves of the tank 1 downstream of the first pressure sensor 13).
• this stability check of the first pressure PT3 is positive if at least one of the following conditions is met:
• the first instantaneous pressure (PT3) in line (3) is greater than a predetermined pressure, for example between 15 and 25 bar,
• the variation of the first instantaneous pressure (PT3) during at least one determined interval is less than a determined level of variation corresponding, for example, to a variation in absolute value of between 0.005 and 0.020 bar per second, and preferably 0, 01 bar per second.
• Another possible cumulative condition could be that the first measured pressure PT3 is greater than the atmospheric pressure.
• the first condition (i) above filled indicates that the reservoir 1 to be filled is of the high pressure type and therefore accepts high pressures.
• the second condition (ii) above filled can be measured in various ways.
• the value of the first pressure PT3 can be read over several successive intervals of ten seconds, for example five intervals of ten seconds each. Within each time interval of ten seconds, the value of the first PT3 pressure must not diverge by more than 0.1 bar.
• the five ten-second intervals overlap in part.
• the five ten-second intervals begin alternately successively every second. Alternatively, an average of this pressure can be observed.
• the definition of the intervals depends in particular on the accuracy of the pressure sensor. This check is preferably carried out after sweeping the filling pipe 3, especially if the latter comprises a nonreturn valve 1 19.
• the pressure PT4 in the tank 1 is determined solely by a first pressure measurement (PT3-> PT4) at the level of the filling line 3 (step 302) .
• a predetermined correction coefficient (multiplicative K and / or additive C) can be used to determine the pressure PT4 in the tank 1 from the first measured pressure PT3.
• the method may comprise at the same time a flow test to determine that the flow rate supplied by the pump 4 is sufficient and that the pump 4 is not hollow.
• the method may comprise a verification of a minimum flow rate at the pump outlet 4 to the tank 1, for example 30 liters per minute and / or a minimum pressure increase at the pump outlet 4 at the level of the pressure sensor. 1 13 of the bypass line 8 and the first sensor of pressure 13, for example 6bar and 1 bar respectively (step 303, FIG. 1 1 and FIG. 9). If this check is negative, the pump 4 is stopped automatically (N, return to step 300). If this condition is positive, "O" the filling process can continue.
• the method then comprises a step 304 for limiting the first instantaneous pressure PT3 below a maximum pressure threshold PT3sup.
• This step of limiting the first instantaneous pressure PT3 below the maximum pressure threshold PT3sup is preferably performed for a finite determined duration of limitation.
• the limitation of the first instantaneous pressure PT3 below a maximum pressure threshold PT3sup is preferably performed by the operator via a manual regulation of the fluid flow transferred via the flow control member 12 and / or via a regulating the pressure differential generated by the pump 4.
• the determined limitation period is for example between thirty and one hundred and eighty seconds and preferably equal to sixty seconds.
• An additional safety condition may be adopted if necessary to interrupt the filling if the first instantaneous pressure PT3 becomes too great during the limitation period (excessive value determined).
• the limitation period can be variable, in particular as a function of the rate delivered in the storage. If the flow is high, the duration is lower and vice versa.
• the method comprises a measurement of the quantity Q of fluid transferred from the tank 2 to the tank 1.
• this quantity of fluid Q transferred exceeds a threshold quantity Qs before the end of the determined limitation period, said limitation period initially provided is reduced, for example, a limitation period of five seconds is granted at most to complete the step 304 of limitation.
• the maximum pressure threshold PT3sup is defined according to the previously determined value of the pressure PT4 in the tank 1. For example, when this determined value of the pressure PT4 in the tank 1 is less than or equal to a first determined level between three and five bar, for example equal to three bar, the maximum pressure threshold PT3sup is preferably a value of predetermined fixed pressure between 5 and 9 bar and preferably equal to 7bar.
• the maximum pressure threshold PT3sup in bar can be given by the following formula:
• the maximum pressure threshold PT3sup in bar can be given by the following formula:
• z being a fixed predetermined coefficient and without unit between 0.80 and 1 and preferably equal to 0.98, and with PA a fixed pressure increase in bar between two and four bar and preferably equal to four bar.
• the maximum pressure threshold PT3sup in bar can be given by the following formula
• the threshold of maximum pressure PT3sup in bar is given by the following formula:
• the maximum pressure threshold PT3sup in bar can be a fixed fixed value between 30 and 50 bar and preferably equal to 37bar.
• the process can be continued by then comparing the first instantaneous pressure PT3 with the high threshold Pmax and interrupting the filling if the high threshold Pmax is exceeded as described above with reference to FIG. 10 (steps referenced 103, 104, 105 and 106 in particular).
• the value of first reference pressure PT3ref used initially to calculate the first high threshold Pmax is for example the value of the first pressure PT3 measured at the end or after a step 304 of positive limitation.
• the value of the first reference pressure PT3ref used initially to calculate the first high threshold Pmax is, for example, the value of the first pressure PT3 measured in line 3 in a time interval between zero and 180s seconds after an implementation. running the pump 4.
• this first reference pressure PT3ref is measured in a determined time interval between zero and 180 seconds after the start of the actual transfer of a flow of liquid to the reservoir 1 (corresponding for example to step 303 of FIG. 1 during which the pump provides a minimum flow to the tank 1 and / or there is a minimum pressure increase at the pump outlet 4 and a level of the first pressure sensor 13).
• the first instantaneous reference pressure PT3ref is the value measured during the at least one pressure measurement or an average of this at least one pressure measurement.
• the pump 4 is automatically stopped (reference 400, Figure 1 1).
• This safety measure makes it possible to detect a pressure drop that is synonymous with an abnormally late opening of the valves of the tank 1. That is, if this decrease of the first pressure PT3 occurs during filling, it means that previously the tank 1 was isolated from the pipe 3 and the previous measurements and calculations were incorrect, including the determination of PT4 pressure in the tank.
• the start M of the pump 4 may comprise a pre-control of the flow actually delivered by the pump.
• This pre-flow control comprises a determination of an effective transfer of liquid in the tank 1 by the pump 4 during this time TQ pre-flow control.
• the determination of an actual transfer of liquid in the tank 1 by the pump 4 may consist of determining whether the operator (or the device if it is partially automated) begins the actual transfer of liquid to the tank 1. Indeed, before starting the filling, the pump 4 can be cooled and stabilized during a determined period of time during which the liquid pumped into the tank 2 is returned to the tank via the bypass line 8 (for example by opening the by-pass valve 5 and by keeping the valve 12 with variable opening closed).
• the electronic logic 16 is configured to compare the transfer of liquid in the tank 1 with a determined threshold S and, when the transfer of liquid in the tank 1 does not reach this threshold S during the duration TQ of pre - Flow control, the electronic logic 16 interrupts AR operation of the pump 4 (see references 201 and 202 Figure 12). Such a stoppage of the pump 4 means that the start is not satisfactory to continue the process of priming the filling.
• the determination of a transfer of liquid in the tank 1 may for example comprise a measurement 9 of the flow rate Q of instantaneous liquid in the filling line 3 downstream of the pump 4 and upstream of the tank 1 (see FIG.
• the filling line may comprise a flow meter 9 connected to the electronic logic 16.
• the electronic logic 16 can compare the instantaneous flow rate Q of the measured liquid with a minimum flow rate threshold Qmin determined and, when the instantaneous flow rate Q of the measured liquid does not reach the threshold of minimum flow rate Qmin during the determined duration TQ of pre - flow control, an interruption step AR of the operation of the pump 4.
• the minimum flow rate threshold Qmin determined can be chosen beforehand according to the technical characteristics of the filling device (type of pump, etc.). This threshold minimum flow Qmin is for example between one and fifty liters per minute and preferably between ten and forty liters per minute or between three and eight liters per minute, for example five liters per minute.
• the predetermined duration TQ pre-flow control may be between twenty and two hundred and forty seconds and preferably between thirty and one hundred and twenty seconds, for example ninety seconds.
• the determination of a transfer of liquid in the tank 1 can be performed differently.
• the determination of a transfer of liquid in the tank 1 may comprise a measurement of the first instantaneous pressure PT3 in the filling line 3 downstream of the pump 4 and upstream of the tank 1, in particular downstream of the valve 12 with variable opening via the first pressure sensor 13 described above.
• This instantaneous pressure PT3 can be compared with a predetermined reference level and, when this measurement of the first instantaneous pressure PT3 in the filling line 3 does not reach the reference level during the predetermined time TQ pre-flow control, pump 4 is stopped.
• the determination of a transfer of liquid in the tank 1 is carried out by controlling the evolutions or pressure differentials.
• the device controls in real time the instantaneous PT3 and PT50 pressures respectively at the filling line 3 downstream of the variable opening valve 12, and at the return line 8.
• the device can use the PT50 pressure sensor 29 upstream of the bypass valves 5, 55 (see Figure 2).
• an increase of the first pressure PT3 above a threshold determined simultaneously with a decrease in the pressure PT50 determined in the bypass line 8 corresponds to a sufficient effective transfer. If this sufficient effective transfer is not performed during the determined pre-control time TQ, the pump 4 is stopped.
• the first instantaneous pressure PT3 in the filling line 3 is measured downstream of the pump 4 at the moment when the transfer of liquid into the tank 1 reaches the determined threshold S (PT3 (S), see reference 204, Figure 12). This value can be stored by the electronic logic.
• the process then comprises an additional pre-check of the first pressure PT3 in the filling line.
• the method may then comprise a step of pre-checking the first pressure PT3 in the filling line 3 downstream of the variable opening valve 12 during a determined period of pressure pre-control TP.
• the operation of the pump 4 is interrupted AR (see references 205 and 206, Figure 10).
• This pre-pressure control is preferably provided to ensure that the pressure regulated in the filling line 3 downstream of the pump 4 is maintained in a determined range.
• the inventors have indeed determined that such an action improves the filling and in particular the possible subsequent detection of abnormal overpressure as previously described.
• the maximum pressure threshold PT3sup in bar may be identical to that described in the example of FIG.
• the minimum pressure threshold PT3min is a predetermined fixed value, possibly adjustable, for example between two bar and ten bar and preferably between four and ten bar, in particular five bar.
• the determined duration TP pre-pressure control is for example between five and one hundred eighty seconds and preferably between ten and thirty seconds, for example fifteen seconds.
• the method may then comprise a filling control as described above with reference in particular to FIG. 10.
• FIG. 12 reproduces, by way of example, the steps 103, 104, 105 and 106 of FIG. concisely this process will not be described a second time.
• the predetermined high threshold Pmax used to interrupt the filling, if any, mentioned above is calculated or defined at the end of the determined duration TP pre-pressure control. That is, the first PT3 pressure measurement or measurements used to define the first reference pressure PT3ref (or an average of these pressures mPT3ref) is carried out at the end of the determined pre-control duration TP. pressure (in the case of course where the pump 4 is not stopped).
• timer A mentioned above may include the controls described with reference to FIG.

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• Engineering & Computer Science (AREA)
• Mechanical Engineering (AREA)
• General Engineering & Computer Science (AREA)
• Filling Or Discharging Of Gas Storage Vessels (AREA)

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• 2012
  • 2012-11-23 FR FR1261153A patent/FR2998642B1/fr not_active Expired - Fee Related
• 2013
  • 2013-10-10 WO PCT/FR2013/052414 patent/WO2014080099A1/fr active Application Filing
  • 2013-10-10 CN CN201380061041.5A patent/CN104797877A/zh active Pending
  • 2013-10-10 BR BR112015011818A patent/BR112015011818A2/pt not_active Application Discontinuation
  • 2013-10-10 US US14/646,073 patent/US9765931B2/en not_active Expired - Fee Related
  • 2013-10-10 EP EP13785543.3A patent/EP2923141A1/de not_active Withdrawn
  • 2013-10-10 CA CA2887105A patent/CA2887105A1/fr not_active Abandoned

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