WO2023031336A1 - Dispositif et procédé de remplissage de réservoir de gaz sous pression - Google Patents
Dispositif et procédé de remplissage de réservoir de gaz sous pression Download PDFInfo
- Publication number
- WO2023031336A1 WO2023031336A1 PCT/EP2022/074338 EP2022074338W WO2023031336A1 WO 2023031336 A1 WO2023031336 A1 WO 2023031336A1 EP 2022074338 W EP2022074338 W EP 2022074338W WO 2023031336 A1 WO2023031336 A1 WO 2023031336A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- transfer fluid
- distributor
- heat
- heat transfer
- heat exchanger
- Prior art date
Links
- 238000000034 method Methods 0.000 title claims abstract description 9
- 239000013529 heat transfer fluid Substances 0.000 claims abstract description 62
- 239000012530 fluid Substances 0.000 claims abstract description 14
- 238000005057 refrigeration Methods 0.000 claims abstract description 13
- 239000012267 brine Substances 0.000 claims abstract description 11
- HPALAKNZSZLMCH-UHFFFAOYSA-M sodium;chloride;hydrate Chemical compound O.[Na+].[Cl-] HPALAKNZSZLMCH-UHFFFAOYSA-M 0.000 claims abstract description 11
- 238000001816 cooling Methods 0.000 claims abstract description 9
- 239000003507 refrigerant Substances 0.000 claims abstract description 7
- 238000011144 upstream manufacturing Methods 0.000 claims description 10
- 239000007789 gas Substances 0.000 description 11
- 239000002826 coolant Substances 0.000 description 5
- 239000001257 hydrogen Substances 0.000 description 5
- 229910052739 hydrogen Inorganic materials 0.000 description 5
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 4
- 230000002528 anti-freeze Effects 0.000 description 1
- 238000009795 derivation Methods 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 150000002431 hydrogen Chemical class 0.000 description 1
- 230000002035 prolonged effect Effects 0.000 description 1
Images
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
- F17C13/00—Details of vessels or of the filling or discharging of vessels
- F17C13/04—Arrangement or mounting of valves
-
- 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
- F17C2201/00—Vessel construction, in particular geometry, arrangement or size
- F17C2201/03—Orientation
- F17C2201/032—Orientation with substantially vertical main axis
-
- 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
- F17C2201/00—Vessel construction, in particular geometry, arrangement or size
- F17C2201/05—Size
- F17C2201/054—Size medium (>1 m3)
-
- 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
- F17C2201/00—Vessel construction, in particular geometry, arrangement or size
- F17C2201/05—Size
- F17C2201/058—Size portable (<30 l)
-
- 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
- F17C2205/00—Vessel construction, in particular mounting arrangements, attachments or identifications means
- F17C2205/03—Fluid connections, filters, valves, closure means or other attachments
- F17C2205/0302—Fittings, valves, filters, or components in connection with the gas storage device
- F17C2205/0323—Valves
- F17C2205/0329—Valves manually actuated
-
- 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
- F17C2205/00—Vessel construction, in particular mounting arrangements, attachments or identifications means
- F17C2205/03—Fluid connections, filters, valves, closure means or other attachments
- F17C2205/0302—Fittings, valves, filters, or components in connection with the gas storage device
- F17C2205/0323—Valves
- F17C2205/0332—Safety valves or pressure relief valves
-
- 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
- F17C2205/00—Vessel construction, in particular mounting arrangements, attachments or identifications means
- F17C2205/03—Fluid connections, filters, valves, closure means or other attachments
- F17C2205/0302—Fittings, valves, filters, or components in connection with the gas storage device
- F17C2205/0323—Valves
- F17C2205/0335—Check-valves or non-return valves
-
- 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
- F17C2205/00—Vessel construction, in particular mounting arrangements, attachments or identifications means
- F17C2205/03—Fluid connections, filters, valves, closure means or other attachments
- F17C2205/0302—Fittings, valves, filters, or components in connection with the gas storage device
- F17C2205/0382—Constructional details of valves, regulators
-
- 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
- F17C2205/00—Vessel construction, in particular mounting arrangements, attachments or identifications means
- F17C2205/03—Fluid connections, filters, valves, closure means or other attachments
- F17C2205/0388—Arrangement of valves, regulators, filters
- F17C2205/0394—Arrangement of valves, regulators, filters in direct contact with the pressure 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
- F17C2221/00—Handled fluid, in particular type of fluid
- F17C2221/01—Pure fluids
- F17C2221/013—Carbone dioxide
-
- 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
- F17C2221/00—Handled fluid, in particular type of fluid
- F17C2221/01—Pure fluids
- F17C2221/014—Nitrogen
-
- 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
- F17C2223/0107—Single phase
- F17C2223/0123—Single phase gaseous, e.g. CNG, GNC
-
- 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
- F17C2223/036—Very high pressure (>80 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
- 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
- F17C2225/036—Very high pressure, i.e. above 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
- F17C2227/03—Heat exchange with the fluid
- F17C2227/0367—Localisation of heat exchange
- F17C2227/0388—Localisation of heat exchange separate
-
- 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
- F17C2270/07—Applications for household use
- F17C2270/0736—Capsules, e.g. CO2
Definitions
- the invention relates to a device and a method for filling a pressurized gas tank.
- the invention relates more particularly to a device for filling pressurized gas tanks comprising a distributor intended to supply a pressurized gas tank from a source of fluid, the device comprising a refrigeration system for cooling the flow of gas of the distributor, the refrigeration system comprising a refrigerant circuit such as brine and a heat exchanger providing heat exchange between the heat transfer fluid and the gas flow from the distributor, the heat transfer fluid circuit comprising, arranged in series in a loop, a reserve of heat transfer fluid, a member for circulating the heat transfer fluid in the circuit and at least one evaporator providing heat exchange between the heat transfer fluid and a cold source.
- a refrigerant circuit such as brine
- a heat exchanger providing heat exchange between the heat transfer fluid and the gas flow from the distributor
- the heat transfer fluid circuit comprising, arranged in series in a loop, a reserve of heat transfer fluid, a member for circulating the heat transfer fluid in the circuit and at least one evaporator providing heat exchange between the heat transfer fluid and a cold source.
- a first method of cooling hydrogen in or upstream of the distributor of a filling station consists in supplying a heat exchanger with an antifreeze heat transfer fluid, typically brine.
- This heat transfer fluid or refrigerant
- This heat transfer fluid is itself cooled in the evaporator of a refrigeration unit (see for example JP2015092108A).
- This second embodiment is generally more efficient. Indeed, at a given brine temperature, the distributor's exchanger can be supplied at a lower temperature because the evaporator provides additional cooling by being inserted between the brine tank and the distributor's exchanger. In addition, for a given cooling target on hydrogen, the evaporator being supplied with hotter brine, the evaporation temperature of the refrigerant can be higher and therefore the coefficient of performance of the refrigeration unit is increased. Moreover, for a given compressor size on the refrigeration unit, the second embodiment makes it possible to cool the hydrogen at a lower temperature and/or to have more cooling power.
- An object of the present invention is to overcome all or part of the drawbacks of the prior art noted above.
- the device according to the invention is essentially characterized in that the circuit comprises a bypass portion and a set of valve(s) of diversion allowing all or part of the heat transfer fluid to avoid passing through the heat exchanger of the distributor to cool the heat transfer fluid in the reserve and to accumulate cold temperatures therein independently of the need for cold temperatures at the level of the distributor.
- embodiments of the invention may include one or more of the following features:
- the invention also relates to a method for filling a pressurized gas tank by means of a device according to any one of the characteristics above or below, in which a flow of gas is circulated in the distributor and through the heat exchanger and a flow of heat transfer fluid is also circulated in the heat transfer fluid circuit and passes into the heat exchanger (5) of the distributor.
- the method comprises a step of circulating at least part of the heat transfer fluid in the bypass portion without passing through the heat exchanger of the distributor to cool the heat transfer fluid in the reserve and/or to reduce the cold power supplied to the heat exchanger.
- the invention may also relate to any alternative device or method comprising any combination of the characteristics above or below within the scope of the claims.
- FIG. 1 represents a schematic and partial view illustrating a possible example of structure and operation of the invention according to a fourth embodiment.
- the device 1 for filling pressurized gas tanks illustrated is, for example, a pressurized hydrogen tank filling station.
- This device 1 comprises a distributor 2 (flexible provided with a nozzle for example) intended to supply a reservoir 3 with pressurized gas from a source 4 of fluid (storage(s) and/or compressor(s) and/or Or other).
- a source 4 of fluid storage(s) and/or compressor(s) and/or Or other).
- the device 1 comprises a refrigeration system for cooling the flow of gas from the distributor 2.
- This refrigeration system comprises a circuit 6 of heat transfer fluid such as brine and a heat exchanger 5 providing heat exchange between the flow of fluid heat transfer fluid and the gas flow from the distributor 2.
- the heat exchanger 5 may include a conductive mass which can be pre-cooled by the heat transfer fluid to increase the thermal inertia of the cooling (and if necessary cool even without simultaneous passage of coolant).
- the circuit 6 of heat transfer fluid is for example a closed loop and comprises, arranged in series in the loop, a reserve 7 of heat transfer fluid (for example a reserve of brine), a member 8 for circulating the heat transfer fluid in the circuit 6 (for example a pump) and an evaporator 9 providing heat exchange between the heat transfer fluid and a cold source 10 (for example a heat exchanger).
- a reserve 7 of heat transfer fluid for example a reserve of brine
- a member 8 for circulating the heat transfer fluid in the circuit 6 for example a pump
- an evaporator 9 providing heat exchange between the heat transfer fluid and a cold source 10 (for example a heat exchanger).
- the circuit comprises a bypass portion 11 and a set of bypass valve(s) 12 allowing all or part of the heat transfer fluid to avoid passing through the heat exchanger 5 of the distributor 2.
- This bypass of the flow without passing into the heat exchanger 5 makes it possible to cool the heat transfer fluid in the reserve 7 and to accumulate there cold temperatures independently of the need for cold temperatures at the level of the distributor 2. That is to say that the circulation of the heat transfer fluid in the circuit without passing through the heat exchanger 5 makes it possible to cool this coolant.
- This derivation also makes it possible to regulate the quantity of cold supplied to the hydrogen in the heat exchanger 5 . That is to say that this bypass makes it possible to control (reduce) the cold power supplied to the heat exchanger 5.
- the evaporator 9 is located between the reserve 7 and the heat exchanger 5 of the distributor 5, downstream of the member 8 for circulating the fluid and upstream of the heat exchanger 5 of the distributor (according to the direction of circulation of the heat transfer fluid in the heat transfer fluid circuit 6).
- the evaporator 9 is located between the heat exchanger 5 of the distributor 5 and the reserve 7, downstream from the heat exchanger 5 of the distributor 5 and upstream of the reserve 7 (according to the direction of circulation of the heat transfer fluid in the heat transfer fluid circuit 6).
- the heat transfer fluid circuit 6 may comprise two evaporators 9, a first evaporator 9 located downstream of the reserve 7 and upstream of the heat exchanger 5, for example between the member 8 for circulating the fluid and the heat exchanger 5 of distributor 5 and a second evaporator 9 located between heat exchanger 5 of distributor 2 and reserve 7.
- the device may comprise several distributors 2 intended to supply separate reservoirs 3 and for example simultaneously or not and each comprising a heat exchanger 5
- the heat transfer fluid circuit 6 is common to the plurality of distributors 2 and comprises a set of parallel branches passing respectively through the various heat exchangers 5 and a set of valve(s) 13 for distributing to control the flow of coolant to the heat exchanger(s) 5.
- the device 1 may comprise a bypass portion 11 and a set of valve(s) 12 as described above for each of the heat exchangers 5 .
- the cold source comprises a loop circuit of a refrigerant which comprises a pump 16, evaporator 17, a reserve 18 of refrigerant then a passage in the evaporator 9 which cools the brine circulating in the circuit 6 of fluid coolant.
- This type of cold source can be used in the other embodiments.
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Filling Or Discharging Of Gas Storage Vessels (AREA)
Abstract
Description
- selon le sens de circulation du fluide caloporteur dans le circuit de fluide caloporteur, le au moins un évaporateur est situé entre la réserve et l’échangeur de chaleur du distributeur, en aval de l’organe de mise en circulation du fluide et en amont de l’échangeur de chaleur du distributeur,
- selon le sens de circulation du fluide caloporteur dans le circuit de fluide caloporteur, le au moins un évaporateur est situé entre l’échangeur de chaleur du distributeur et la réserve, c’est-à-dire en aval de l’échangeur de chaleur du distributeur et en amont de la réserve,
- le circuit de fluide caloporteur comprend deux évaporateurs disposés respectivement en amont et en aval de la réserve, un premier évaporateur situé entre la réserve et l’échangeur de chaleur du distributeur et un second évaporateur entre l’échangeur de chaleur du distributeur et la réserve,
- le circuit de fluide caloporteur comprend une dérivation du au moins un évaporateur et un ensemble de vanne(s) pour permettre une alimentation directe de l’échangeur de chaleur du distributeur à partir de la réserve ?
- le dispositif comprend plusieurs distributeurs destinés à alimenter des réservoirs distincts et comprenant chacun un échangeur de chaleur, le circuit de fluide caloporteur étant commun à la pluralité de distributeurs et comprenant un ensemble de branches parallèles transitant respectivement dans les différents échangeurs de chaleur et un ensemble de vanne(s) de répartition pour contrôler le flux de fluide caloporteur vers le ou les échangeurs de chaleur, le dispositif comprenant une portion de dérivation et un ensemble de vanne(s) pour tout ou partie des échangeurs de chaleur.
Claims (8)
- Dispositif de remplissage de réservoirs de gaz sous pression comprenant un distributeur (2) destiné à alimenter un réservoir (3) en gaz sous pression à partir d’une source (4) de fluide, le dispositif (1) comprenant un système de réfrigération pour refroidir le flux de gaz du distributeur (2), le système de réfrigération comprenant un circuit (6) de fluide frigorigène tel que de la saumure et un échangeur (5) de chaleur assurant un échange de chaleur entre le fluide caloporteur et le flux de gaz du distributeur (2), le circuit (6) de fluide caloporteur comprenant, disposés en série dans une boucle, une réserve (7) de fluide caloporteur, un organe (8) de mise en circulation du fluide caloporteur dans le circuit (6) et au moins un évaporateur (9) assurant un échange thermique entre le fluide caloporteur et une source (10) de froid, caractérisé en ce que le circuit comprend un portion (11) de dérivation et une ensemble de vanne(s) (12) de dérivation permettant à tout ou partie du fluide caloporteur d’éviter le passage dans l’échangeur (5) de chaleur du distributeur (2) pour refroidir le fluide caloporteur dans la réserve (7) et d’y accumuler des frigories indépendamment du besoin de frigories au niveau du distributeur (2).
- Dispositif selon la revendication 1, caractérisé en ce que, selon le sens de circulation du fluide caloporteur dans le circuit (6) de fluide caloporteur, le au moins un évaporateur (9) est situé entre la réserve (7) et l’échangeur (5) de chaleur du distributeur (5), en aval de l’organe (8) de mise en circulation du fluide et en amont de l’échangeur (5) de chaleur du distributeur (2).
- Dispositif selon la revendication 1 ou 2, caractérisé en ce que, selon le sens de circulation du fluide caloporteur dans le circuit (6) de fluide caloporteur, le au moins un évaporateur (9) est situé entre l’échangeur (5) de chaleur du distributeur (2) et la réserve (7), c’est-à-dire en aval de l’échangeur (5) de chaleur du distributeur (5) et en amont de la réserve (7).
- Dispositif selon l’une quelconque des revendication 1 à 3, caractérisé en ce que le circuit (6) de fluide caloporteur comprend deux évaporateurs (9) disposés respectivement en amont et en aval de la réserve (7), un premier évaporateur (9) situé entre la réserve (7) et l’échangeur (5) de chaleur du distributeur (2) et un second évaporateur (9) entre l’échangeur (5) de chaleur du distributeur (2) et la réserve (7).
- Dispositif selon l’une quelconque des revendication 1 à 4, caractérisé en ce que le circuit (6) de fluide caloporteur comprend une dérivation du au moins un évaporateur (9) et un ensemble de vanne(s) pour permettre une alimentation directe de l’échangeur (5) de chaleur du distributeur (2) à partir de la réserve (7).
- Dispositif selon l’une quelconque des revendication 1 à 5, caractérisé en ce qu’il comprend plusieurs distributeurs (2) destinés à alimenter des réservoirs (3) distincts et comprenant chacun un échangeur (5) de chaleur, le circuit (6) de fluide caloporteur étant commun à la pluralité de distributeurs (2) et comprenant un ensemble de branches parallèles transitant respectivement dans les différents échangeurs (5) de chaleur et un ensemble de vanne(s) (13) de répartition pour contrôler le flux de fluide caloporteur vers le ou les échangeurs (5) de chaleur, le dispositif (1) comprenant une portion (11) de dérivation et un ensemble de vanne(s) (12) pour tout ou partie des échangeurs (5) de chaleur.
- Procédé de remplissage de réservoir de gaz sous pression au moyen d’un dispositif selon l’une quelconque des revendications précédentes, dans lequel un flux de gaz est mis en circulation dans le distributeur (2) et au travers de l’échangeur (5) de chaleur et un flux de fluide caloporteur est mis en circulation également dans le circuit (6) de fluide caloporteur et passe dans l’échangeur (5) de chaleur du distributeur (2).
- Procédé selon la revendication 7, caractérisé en ce qu’il comprend une étape de mise en circulation d’au moins une partie du fluide caloporteur dans la portion (11) de dérivation sans passage dans l’échangeur (5) de chaleur du distributeur (2) pour refroidir le fluide caloporteur dans la réserve (7) et/ou diminuer la puissance froide fournie à l’échangeur (5) de chaleur.
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
KR1020247010877A KR20240057429A (ko) | 2021-09-06 | 2022-09-01 | 가압 가스 탱크를 충전하는 장치 및 방법 |
CA3230438A CA3230438A1 (fr) | 2021-09-06 | 2022-09-01 | Dispositif et procede de remplissage de reservoir de gaz sous pression |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR2109311A FR3126744B1 (fr) | 2021-09-06 | 2021-09-06 | Dispositif et procédé de remplissage de réservoir de gaz sous pression |
FRFR2109311 | 2021-09-06 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2023031336A1 true WO2023031336A1 (fr) | 2023-03-09 |
Family
ID=77999209
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/EP2022/074338 WO2023031336A1 (fr) | 2021-09-06 | 2022-09-01 | Dispositif et procédé de remplissage de réservoir de gaz sous pression |
Country Status (4)
Country | Link |
---|---|
KR (1) | KR20240057429A (fr) |
CA (1) | CA3230438A1 (fr) |
FR (1) | FR3126744B1 (fr) |
WO (1) | WO2023031336A1 (fr) |
Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2015092108A (ja) | 2014-11-27 | 2015-05-14 | 株式会社前川製作所 | 燃料ガスの充填制御方法とその装置 |
JP2015158213A (ja) * | 2014-02-21 | 2015-09-03 | 株式会社神戸製鋼所 | ガス供給システムおよび水素ステーション |
US9574709B2 (en) * | 2013-12-27 | 2017-02-21 | Shinwa Controls Co., Ltd. | Cooled-hydrogen supply station and hydrogen cooling apparatus |
EP3457019A1 (fr) | 2017-09-15 | 2019-03-20 | Kabushiki Kaisha Kobe Seiko Sho (Kobe Steel, Ltd.) | Dispositif d'alimentation en gaz et procédé de démarrage de fonctionnement d'un dispositif d'alimentation en gaz |
US20200041070A1 (en) * | 2018-08-01 | 2020-02-06 | L'air Liquide, Societe Anonyme Pour L'etude Et L?Exploitation Des Procedes Georges Claude | Device and process for refueling containers with pressurized gas |
KR20210094731A (ko) * | 2020-01-22 | 2021-07-30 | 주식회사 효성 | 가스공급시스템 및 이를 사용한 가스충전장치 |
-
2021
- 2021-09-06 FR FR2109311A patent/FR3126744B1/fr active Active
-
2022
- 2022-09-01 WO PCT/EP2022/074338 patent/WO2023031336A1/fr active Application Filing
- 2022-09-01 CA CA3230438A patent/CA3230438A1/fr active Pending
- 2022-09-01 KR KR1020247010877A patent/KR20240057429A/ko unknown
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US9574709B2 (en) * | 2013-12-27 | 2017-02-21 | Shinwa Controls Co., Ltd. | Cooled-hydrogen supply station and hydrogen cooling apparatus |
JP2015158213A (ja) * | 2014-02-21 | 2015-09-03 | 株式会社神戸製鋼所 | ガス供給システムおよび水素ステーション |
JP2015092108A (ja) | 2014-11-27 | 2015-05-14 | 株式会社前川製作所 | 燃料ガスの充填制御方法とその装置 |
EP3457019A1 (fr) | 2017-09-15 | 2019-03-20 | Kabushiki Kaisha Kobe Seiko Sho (Kobe Steel, Ltd.) | Dispositif d'alimentation en gaz et procédé de démarrage de fonctionnement d'un dispositif d'alimentation en gaz |
US20200041070A1 (en) * | 2018-08-01 | 2020-02-06 | L'air Liquide, Societe Anonyme Pour L'etude Et L?Exploitation Des Procedes Georges Claude | Device and process for refueling containers with pressurized gas |
KR20210094731A (ko) * | 2020-01-22 | 2021-07-30 | 주식회사 효성 | 가스공급시스템 및 이를 사용한 가스충전장치 |
Also Published As
Publication number | Publication date |
---|---|
KR20240057429A (ko) | 2024-05-02 |
CA3230438A1 (fr) | 2023-03-09 |
FR3126744B1 (fr) | 2023-08-25 |
FR3126744A1 (fr) | 2023-03-10 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US7207298B2 (en) | Cooling system for an engine | |
EP0696968B1 (fr) | Procede de climatisation de vehicule avec boucle de chauffage | |
FR2846280A1 (fr) | Systeme de conditionnement d'air pour vehicules | |
FR2589560A1 (fr) | Circuit de refrigeration et circuit de pompe a chaleur, et procede de degivrage | |
US20070193717A1 (en) | Heat exchanger for hydrogen-operated fuel supply systems | |
US4819454A (en) | Liquid cryogenic vaporizer utilizing ambient air and a nonfired heat source | |
JP6806524B2 (ja) | エアコンシステムと統合されたハイブリッド型インタークーラシステムおよびその制御方法 | |
EP3465050B1 (fr) | Procédé et dispositif de refroidissement d'au moins une charge chaude à bord d'un véhicule tel qu'un aéronef à boucle fluide partiellement réversible | |
FR2829432A1 (fr) | Dispositif de gestion thermique, notamment pour vehicule automobile equipe d'une pile a combustible | |
US10677545B2 (en) | Method of flowing coolant through exhaust heat recovery system after engine shutoff | |
WO2023031336A1 (fr) | Dispositif et procédé de remplissage de réservoir de gaz sous pression | |
KR101324612B1 (ko) | 천연가스 연료공급 시스템 | |
KR20030044149A (ko) | 엔진 냉각 시스템 및 방법 | |
JPH0914587A (ja) | 天然ガス焚きガスタービン複合サイクル発電所の燃料用lng気化装置 | |
FR2872267A1 (fr) | Dispositif de regulation de la temperature d'un fluide a traiter et installation de regulation comprenant ce dispositif | |
FR2905310A1 (fr) | Systeme de climatisation pour vehicule automobile | |
KR101324614B1 (ko) | 천연가스 연료공급 시스템 | |
KR101324613B1 (ko) | 천연가스 연료공급 시스템 | |
WO2020065193A1 (fr) | Systeme de gestion de confort de passager | |
EP3459770B1 (fr) | Transport cryogenique de produits thermosensibles valorisant le fuel operant le moteur du véhicule a l'aide d'un module eutectique de stockage du froid | |
FR3140414A1 (fr) | Dispositif et procédé de remplissage de réservoir de gaz sous pression | |
CN115217574B (zh) | 一种机油输送系统及机油温度的控制方法 | |
FR3055660B1 (fr) | Procede de regulation d’un debit dans un echangeur de chaleur de ligne de recirculation de gaz d’echappement d’un moteur | |
FR3075708B1 (fr) | Procede de gestion du fonctionnement d'un camion de transport frigorifique de produits thermosensibles du type a injection indirecte | |
JPH06313687A (ja) | 蓄冷熱利用の液化天然ガス気化装置 |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
121 | Ep: the epo has been informed by wipo that ep was designated in this application |
Ref document number: 22772495 Country of ref document: EP Kind code of ref document: A1 |
|
WWE | Wipo information: entry into national phase |
Ref document number: 3230438 Country of ref document: CA |
|
ENP | Entry into the national phase |
Ref document number: 20247010877 Country of ref document: KR Kind code of ref document: A |
|
WWE | Wipo information: entry into national phase |
Ref document number: 2022772495 Country of ref document: EP |
|
NENP | Non-entry into the national phase |
Ref country code: DE |
|
ENP | Entry into the national phase |
Ref document number: 2022772495 Country of ref document: EP Effective date: 20240408 |