WO2006034748A1 - Procede et dispositif de compression d'un agent gazeux - Google Patents

Procede et dispositif de compression d'un agent gazeux Download PDF

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Publication number
WO2006034748A1
WO2006034748A1 PCT/EP2005/008370 EP2005008370W WO2006034748A1 WO 2006034748 A1 WO2006034748 A1 WO 2006034748A1 EP 2005008370 W EP2005008370 W EP 2005008370W WO 2006034748 A1 WO2006034748 A1 WO 2006034748A1
Authority
WO
WIPO (PCT)
Prior art keywords
liquid
gaseous medium
compression
cylinder
cylinders
Prior art date
Application number
PCT/EP2005/008370
Other languages
German (de)
English (en)
Inventor
Robert Adler
Georg Siebert
Original Assignee
Linde Aktiengesellschaft
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Linde Aktiengesellschaft filed Critical Linde Aktiengesellschaft
Priority to AT05768562T priority Critical patent/ATE530772T1/de
Priority to JP2007532789A priority patent/JP4986161B2/ja
Priority to EP05768562A priority patent/EP1792087B1/fr
Priority to CA002581280A priority patent/CA2581280A1/fr
Priority to US11/575,956 priority patent/US20070258828A1/en
Priority to CN2005800319092A priority patent/CN101023272B/zh
Priority to AU2005289219A priority patent/AU2005289219A1/en
Publication of WO2006034748A1 publication Critical patent/WO2006034748A1/fr

Links

Classifications

    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04F—PUMPING OF FLUID BY DIRECT CONTACT OF ANOTHER FLUID OR BY USING INERTIA OF FLUID TO BE PUMPED; SIPHONS
    • F04F1/00—Pumps using positively or negatively pressurised fluid medium acting directly on the liquid to be pumped
    • F04F1/06—Pumps using positively or negatively pressurised fluid medium acting directly on the liquid to be pumped the fluid medium acting on the surface of the liquid to be pumped
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04F—PUMPING OF FLUID BY DIRECT CONTACT OF ANOTHER FLUID OR BY USING INERTIA OF FLUID TO BE PUMPED; SIPHONS
    • F04F1/00—Pumps using positively or negatively pressurised fluid medium acting directly on the liquid to be pumped
    • F04F1/06—Pumps using positively or negatively pressurised fluid medium acting directly on the liquid to be pumped the fluid medium acting on the surface of the liquid to be pumped
    • F04F1/10—Pumps using positively or negatively pressurised fluid medium acting directly on the liquid to be pumped the fluid medium acting on the surface of the liquid to be pumped of multiple type, e.g. with two or more units in parallel
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
    • C10N2020/00—Specified physical or chemical properties or characteristics, i.e. function, of component of lubricating compositions
    • C10N2020/01—Physico-chemical properties
    • C10N2020/077—Ionic Liquids

Definitions

  • the invention relates to a method for compressing a gaseous medium, in particular hydrogen.
  • the invention relates to an apparatus for compressing a gaseous medium, in particular of hydrogen.
  • Piston compressor systems for use. Piston compressors require appropriate sealing systems in order to keep the medium to be compressed separated from the drive (drive) medium which drives the piston, for example hydraulic oil.
  • Generic methods and devices are used, for example, in natural gas compressor stations, as implemented in natural gas filling stations.
  • Object of the present invention is to provide a generic method and a generic device for compressing a gaseous medium, in particular of hydrogen, indicate that or avoid the aforementioned disadvantages.
  • this object is achieved in that the compression of the gaseous medium is carried out by a liquid, wherein a liquid in which the gaseous medium does not dissolve and / or which is separable from the gaseous medium without residue, is used.
  • the inventive device for compressing a gaseous medium is characterized in that it a) one or more cylinders, b) supply and discharge lines, which serve to supply and discharge of the gaseous medium to be compressed in or out of the cylinder or cylinders, c ) per cylinder at least one liquid line, which serves to supply and discharge of the gaseous medium-compressing liquid in the cylinder, and d).
  • the liquid is a liquid in which the gaseous medium to be compressed does not dissolve and / or which is separable from the gaseous medium without residue comprises.
  • the invention makes it possible to dispense with the compression of a gaseous medium to a piston and any (piston) sealing systems. This is achieved by realizing a compression of the gaseous medium to be compressed via a column of liquid which can be changed within a cylinder.
  • the previously used pistons which consist of a solid material, are replaced by a non-compressible liquid or liquid column. By moving up and down the liquid column - analogous to the upward and downward movement of a piston - the gaseous medium to be compressed is sucked in and compacted.
  • a liquid is preferably selected in which the gaseous medium to be compressed does not dissolve and which can be separated from the gaseous medium without residue.
  • an ionic liquid a high-boiling Hydrauliköi or liquids which have a very low vapor pressure, such as vacuum pump oils, molten salts and metals low melting point, or liquids having a Gaslösiichkeit of less than 10 "4 mol / l bar used.
  • Ionic liquids are low-melting, organic salts with melting points between 100 and -90 0 C, wherein most of the known ionic liquids are already in liquid form at room temperature. In contrast to conventional molecular liquids, ionic liquids are entirely ionic and therefore show new and unusual properties. Ionic liquids can be adapted comparatively well by varying the structure of anion and / or cation and by varying their combinations in terms of their properties to given technical problems. For this reason, they are often referred to as so-called "Designer Solvents". With conventional molecular liquids, however, only a variation of the structure is possible.
  • ionic liquids In contrast to conventional molecular liquids, ionic liquids also have the advantage that they have no measurable vapor pressure. This means that, as long as their decomposition temperature is not reached, they do not evaporate in the slightest traces, even in a high vacuum. This results in the properties of incombustibility and environmental friendliness, since ionic liquids can not escape into the atmosphere.
  • the melting points of known ionic liquids are by definition below 100 ° C.
  • the so-called liquidus range-this is the range between melting point and thermal decomposition-is generally 400 ° C. or more.
  • ionic liquids have a high thermal stability. Often, their decomposition points are above 400 0 C. The density and the mixing behavior with other liquids can beei ⁇ flus ⁇ t or adjusted in ionic liquids by the choice of the ions. Ionic liquids also have the advantage that they are electrically conductive and thereby can prevent electrical charging - which represent a potential hazard. Ionic liquids have the advantage that their complete separation from the compressed medium with a comparatively low expenditure on equipment is mögiich.
  • the figure shows a possible embodiment of the invention, in which the compression takes place in two separate cylinders Z1 and 22.
  • the compression can also be realized only in one or in more than two cylinders.
  • the cylinders Z1 and Z2 are supplied with the gaseous medium to be compressed via lines 1, 1 'and 1 ", and inlet valves a and b are arranged in the aforesaid conduits, after which the compressed gaseous medium from the cylinders Z1 and Z2 is transferred the discharge lines 2 'and 2 ", in which also valves c and d are arranged, deducted.
  • the compressed gaseous medium is in a separation device A of the cylinders Z1 and Z2 possibly entrained liquid, which will be discussed in more detail below, freed and then fed via line 2 its further use and / or intermediate storage.
  • a suitable liquid D which serves for the compression of the gaseous medium, is provided inside the cylinders Z1 and Z2.
  • the cylinders Z1 and Z2 are connected via the lines 3 to 6 and the hy rauiikpumpe X, which is driven by an electric motor M connected.
  • the fluid levels D in the cylinders Z1 and Z2 are varied in such a way that one of the cylinders sucks the medium to be compressed, while at the same time or substantially simultaneously in the other cylinder a compression of the gaseous medium takes place.
  • an axial piston pump with swashplate control is preferably used, wherein through a simple adjustment of the swashplate flow rate and / or conveying direction can be changed.
  • the invention also has the advantage over the prior art that an at least partial removal of the (compression) heat produced during the compression can take place via the liquid D.
  • heat exchangers or coolers K1 and K2 are provided, via which the heat generated in the cylinders Z1 and Z2 during compression can be dissipated, for example, to the environment and / or another suitable medium.
  • the device according to the invention can be arranged in the cylinders Z1 and Z2 heat exchangers E1 and E2.
  • heat exchanger here are any constructions of heat exchangers - hereinafter referred to as “active heat exchanger” - and heat storage - hereinafter referred to as “passive heat exchanger” - to understand.
  • the aforementioned advantageous embodiment of the device according to the invention thus enables a substantial reduction of the required compression energy and thus an approximately isothermal compression. Furthermore, lower gas outlet temperatures can be realized and a reduction of the thermal load of the compressor valves can be achieved.
  • the liquid separated from the compressed medium in the separating device A and originating from the cylinders Z1 and Z2 is optionally provided via line 9, in which a stop valve e is arranged
  • the liquid can be supplied according to the need in the cylinders Z1 and Z2 via the lines T and 8 and the two shut-off valves f and h the cylinders Z1 and / or Z2.
  • the dosing of liquid required for the compression takes place during a suction cycle.
  • Liquid feed in which the prescribed requirements can be kept &.
  • the time for the make-up of liquid required for the compression should be based on the current power consumption of the system; Preferably, the dosing of liquid should be done during or near a performance minimum. At this time, the system or the drive pump has sufficient power reserves that can be used for the Nacfispeisen the liquid.
  • the liquid to be replenished D is passed during a suction cycle via the line 10, which has a feed pump P, in the corresponding cylinder Z1 and Z2.
  • the make-up does not take place immediately in the vicinity of the reversal point, since then there is the danger that liquid D u. U. from the corresponding cylinder Z1 or Z2 via the pressure line 2 'and 2 "exits.
  • the separation device A- which serves to separate from the cylinders Z1 and Z2 entrained liquid, correspondingly larger
  • a liquid feed during the suction cycle minimizes the energy requirement of the feed pump P.
  • the detection of the fluid loss takes place via a measure of the deviations of the fluid levels in the cylinders Z1 and Z2 from a reference value, which is normally determined at the beginning of the compression process.
  • the liquid is exposed to an electric field.
  • the device side Mittet for generating an electric field in the cylinder or cylinders are provided
  • a mixing and formation of a two-phase mixture may occur at the separation surface.
  • such a two-phase mixture may, for example, arise within the cylinder (s) at the interface between ionic liquid and the medium to be compressed.
  • ionic liquids which have a corresponding dipole moment and / or a corresponding electrical conductivity.
  • the influence of ionic liquids by means of an electric field makes it possible to increase the acceleration in the reversal points of the pistonless compressor, without there being an increased risk of phase mixing. Furthermore, a clean and reliable separation of ionic liquids from a two-phase mixture is possible even if the
  • Density differences between the ionic liquid and the medium to be compressed are comparatively low.
  • embodiments of erfindungsgernä H method and apparatus of the invention can be realized in which only one cylinder or three or more cylinders are provided. While a cylinder is not capable of delivering the compressed medium continuously with respect to the compression pressure, such often desired delivery of the compressed medium is possible with two or more cylinders.
  • the invention is suitable for compression of gaseous media to pressures of 1000 bar, which is currently feasible. It should be emphasized, however, that in principle also arbitrarily higher pressures can be achieved.
  • the invention further enables compression to maximum pressure with only a single compression stage. Furthermore, the flow rate can be varied as desired.
  • the invention provides a cost effective way to compress such media to very high pressures.

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Reciprocating Pumps (AREA)
  • Compressors, Vaccum Pumps And Other Relevant Systems (AREA)
  • Compressor (AREA)
  • Filling Or Discharging Of Gas Storage Vessels (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Hydrogen, Water And Hydrids (AREA)
  • Manufacture Of Iron (AREA)
  • Jet Pumps And Other Pumps (AREA)

Abstract

L'invention concerne un procédé et un dispositif de compression d'un agent gazeux, notamment d'hydrogène. Selon l'invention, la compression (ZI, Z2) de l'agent gazeux s'effectue par un liquide (D). On utilise un liquide (D) dans lequel l'agent gazeux ne se dissout pas et/ou qui peut se séparer sans résidu de l'agent gazeux. A cet effet, on utilise comme liquide (D) un liquide ionique, une huile hydraulique ayant un point d'ébullition élevé ou un liquide ayant une pression de vapeur très basse.
PCT/EP2005/008370 2004-09-24 2005-08-02 Procede et dispositif de compression d'un agent gazeux WO2006034748A1 (fr)

Priority Applications (7)

Application Number Priority Date Filing Date Title
AT05768562T ATE530772T1 (de) 2004-09-24 2005-08-02 Verfahren und vorrichtung zum verdichten eines gasförmigen mediums
JP2007532789A JP4986161B2 (ja) 2004-09-24 2005-08-02 ガス状媒体の圧縮方法及び装置
EP05768562A EP1792087B1 (fr) 2004-09-24 2005-08-02 Procede et dispositif de compression d'un agent gazeux
CA002581280A CA2581280A1 (fr) 2004-09-24 2005-08-02 Procede et dispositif de compression d'un agent gazeux
US11/575,956 US20070258828A1 (en) 2004-09-24 2005-08-02 Method and Device for Compressing a Gaseous Medium
CN2005800319092A CN101023272B (zh) 2004-09-24 2005-08-02 用于压缩气体介质的方法和装置
AU2005289219A AU2005289219A1 (en) 2004-09-24 2005-08-02 Method and device for compressing a gaseous medium

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE102004046316A DE102004046316A1 (de) 2004-09-24 2004-09-24 Verfahren und Vorrichtung zum Verdichten eines gasförmigen Mediums
DE102004046316.6 2004-09-24

Publications (1)

Publication Number Publication Date
WO2006034748A1 true WO2006034748A1 (fr) 2006-04-06

Family

ID=34978927

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/EP2005/008370 WO2006034748A1 (fr) 2004-09-24 2005-08-02 Procede et dispositif de compression d'un agent gazeux

Country Status (11)

Country Link
US (1) US20070258828A1 (fr)
EP (1) EP1792087B1 (fr)
JP (1) JP4986161B2 (fr)
KR (1) KR20070057813A (fr)
CN (1) CN101023272B (fr)
AT (1) ATE530772T1 (fr)
AU (1) AU2005289219A1 (fr)
CA (1) CA2581280A1 (fr)
DE (1) DE102004046316A1 (fr)
WO (1) WO2006034748A1 (fr)
ZA (1) ZA200702362B (fr)

Cited By (14)

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WO2006120145A1 (fr) * 2005-05-06 2006-11-16 Linde Ag Liquide pour etancheifier un milieu gazeux et utilisation de celui-ci
WO2008025432A1 (fr) * 2006-08-31 2008-03-06 Linde Aktiengesellschaft Compresseur sans piston
WO2008031527A1 (fr) 2006-09-13 2008-03-20 Linde Aktiengesellschaft Compresseur sans piston
WO2010128224A1 (fr) * 2009-05-07 2010-11-11 Ecoren Procédé et équipement de transmission d'énergie mécanique par compression et/ou détente quasi-isotherme d'un gaz
DE102011007639A1 (de) 2010-04-23 2011-10-27 Basf Se Verfahren zur mechanischen Bearbeitung von Werkstücken mit einem Hochdruckstrahl
FR2975141A1 (fr) * 2011-05-13 2012-11-16 Linde Ag Procede et dispositif de compression d'un milieu sature en eau
US8667788B2 (en) 2010-04-09 2014-03-11 Shipstone Corporation System and method for energy storage and retrieval
WO2014146956A1 (fr) 2013-03-21 2014-09-25 Siemens Aktiengesellschaft Système d'étanchéité et turbocompresseur équipé d'un tel système d'étanchéité
US9611868B2 (en) 2010-04-09 2017-04-04 Shipstone Corporation System and method for energy storage and retrieval
DE102016124636A1 (de) 2016-08-01 2018-02-01 Sang-Bae Choi Flüssiggaskompressor mit einer Druck-Volumen-Umwandlungseinrichtung und einem Drehmomentwandler
WO2019007556A1 (fr) * 2017-07-04 2019-01-10 Linde Aktiengesellschaft Liquide ionique associé à un lubrifiant sec
CN111561430A (zh) * 2020-04-23 2020-08-21 北京航空航天大学 一种基于气体溶解和气液转换的等温膨胀装置及使用方法
WO2022234089A1 (fr) 2021-05-06 2022-11-10 Van Halteren Technologies Boxtel B.V. Appareil de compression de gaz et procédé de remplissage d'un réservoir à l'aide dudit appareil
WO2024081660A1 (fr) * 2022-10-14 2024-04-18 Steelhead Composites, Inc. Système d'accumulateur de liquide ionique pour distribuer un gaz

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EP2433000A2 (fr) * 2009-05-22 2012-03-28 General Compression Inc. Dispositif compresseur/détendeur
JP5892945B2 (ja) * 2009-12-24 2016-03-23 ジェネラル コンプレッション インコーポレイテッド 液圧作動システムの効率を最適化するシステム及び方法
JP5766045B2 (ja) * 2011-06-29 2015-08-19 日東精工株式会社 気体注入装置および気液接触装置
ITRM20130313A1 (it) * 2013-05-30 2014-12-01 Gia E Lo Sviluppo Economico Sostenibile Enea Compressore idrodinamico per gas combustibili e detonanti
CN103308446B (zh) * 2013-05-31 2016-01-20 重庆大学 基于波纹管的流体可压缩性测试装置
US10801482B2 (en) * 2014-12-08 2020-10-13 Saudi Arabian Oil Company Multiphase production boost method and system
CN104728083B (zh) * 2015-01-23 2017-06-23 西南科技大学 一种压缩机
FR3042236B1 (fr) * 2015-10-08 2019-09-06 Ortec Expansion Procede et dispositif pour le pompage d'un produit par aspiration.
JP6890588B2 (ja) * 2015-11-25 2021-06-18 イソカレント エナジー インコーポレーテッド 可変圧力容器
DE102016220345A1 (de) 2016-10-18 2018-04-19 Bayerische Motoren Werke Aktiengesellschaft Druckbehältersystem und Betriebsmittelversorgungssystem für ein Kraftfahrzeug
CN106761986B (zh) * 2016-12-27 2019-01-15 北京交通大学 一种常温气体能量转换的装置及其使用方法
DE102017007921A1 (de) * 2017-08-22 2019-02-28 Linde Aktiengesellschaft Verfahren zum Betreiben eines Verdichters und Verdichter
PL240516B1 (pl) * 2018-01-09 2022-04-19 Dobrianski Jurij Maszyna parowa
DE102018003356A1 (de) * 2018-04-19 2019-10-24 Michael Semakin Verdichter
DE102019129495B3 (de) * 2019-10-31 2021-04-15 Deutsches Zentrum für Luft- und Raumfahrt e.V. Verdichteranordnung, Wärmepumpenanordnung und Verfahren zum Betreiben der Verdichteranordnung
EP4061983A1 (fr) 2019-11-21 2022-09-28 EEG Elements Energy GmbH Dispositif d'électrolyse
DE102020207827A1 (de) 2020-06-24 2021-12-30 Argo Gmbh Befüllvorrichtung zur Befüllung von Speicherbehältern mit verdichtetem Wasserstoff, Tankstelle aufweisend selbige und Verfahren zur Befüllung eines Speicherbehälters
CN112442405A (zh) * 2020-12-15 2021-03-05 苏州金宏气体股份有限公司 一种作为液压式加氢工质的离子液体组合物
CN112408318B (zh) * 2020-12-15 2022-09-23 苏州金宏气体股份有限公司 一种用于压缩氢气的离子液体组合物
KR102561244B1 (ko) * 2021-07-26 2023-08-01 한국기계연구원 과열방지 수소 충전시스템 및 이를 이용한 수소 충전방법
CN113623036A (zh) * 2021-09-14 2021-11-09 西安热工研究院有限公司 一种提升蒸汽压力的系统和方法
GB2613202A (en) * 2021-11-29 2023-05-31 Catagen Ltd Method of compressing hydrogen gas, hydrogen gas compressor system and hydrogen gas storage unit

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Cited By (23)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2006120145A1 (fr) * 2005-05-06 2006-11-16 Linde Ag Liquide pour etancheifier un milieu gazeux et utilisation de celui-ci
WO2008025432A1 (fr) * 2006-08-31 2008-03-06 Linde Aktiengesellschaft Compresseur sans piston
US8267670B2 (en) 2006-09-13 2012-09-18 Linde Aktiengesellschaft Pistonless compressor
WO2008031527A1 (fr) 2006-09-13 2008-03-20 Linde Aktiengesellschaft Compresseur sans piston
JP2010503787A (ja) * 2006-09-13 2010-02-04 リンデ アクチエンゲゼルシヤフト ピストンレス圧縮機
KR101422807B1 (ko) * 2006-09-13 2014-07-23 린데 악티엔게젤샤프트 피스톤 없는 압축기
FR2945327A1 (fr) * 2009-05-07 2010-11-12 Ecoren Procede et equipement de transmission d'energie mecanique par compression et/ou detente quasi-isotherme d'un gaz
WO2010128224A1 (fr) * 2009-05-07 2010-11-11 Ecoren Procédé et équipement de transmission d'énergie mécanique par compression et/ou détente quasi-isotherme d'un gaz
US8667788B2 (en) 2010-04-09 2014-03-11 Shipstone Corporation System and method for energy storage and retrieval
EP3147518A1 (fr) 2010-04-09 2017-03-29 Daniel John Kenway Système et procédé de stockage d'énergie et de recherche
US9611868B2 (en) 2010-04-09 2017-04-04 Shipstone Corporation System and method for energy storage and retrieval
DE102011007639A1 (de) 2010-04-23 2011-10-27 Basf Se Verfahren zur mechanischen Bearbeitung von Werkstücken mit einem Hochdruckstrahl
FR2975141A1 (fr) * 2011-05-13 2012-11-16 Linde Ag Procede et dispositif de compression d'un milieu sature en eau
WO2014146956A1 (fr) 2013-03-21 2014-09-25 Siemens Aktiengesellschaft Système d'étanchéité et turbocompresseur équipé d'un tel système d'étanchéité
DE102013205027A1 (de) 2013-03-21 2014-09-25 Siemens Aktiengesellschaft Dichtungseinrichtung und Turboverdichter mit einer derartigen Dichtungseinrichtung
DE102016124636A1 (de) 2016-08-01 2018-02-01 Sang-Bae Choi Flüssiggaskompressor mit einer Druck-Volumen-Umwandlungseinrichtung und einem Drehmomentwandler
DE102016124636B4 (de) 2016-08-01 2021-08-19 Sang-Bae Choi Flüssiggaskompressor mit einer Druck-Volumen-Umwandlungseinrichtung und einem Drehmomentwandler
WO2019007556A1 (fr) * 2017-07-04 2019-01-10 Linde Aktiengesellschaft Liquide ionique associé à un lubrifiant sec
CN111561430A (zh) * 2020-04-23 2020-08-21 北京航空航天大学 一种基于气体溶解和气液转换的等温膨胀装置及使用方法
WO2022234089A1 (fr) 2021-05-06 2022-11-10 Van Halteren Technologies Boxtel B.V. Appareil de compression de gaz et procédé de remplissage d'un réservoir à l'aide dudit appareil
DE102021204586A1 (de) 2021-05-06 2022-11-10 Robert Bosch Gesellschaft mit beschränkter Haftung Vorrichtung zur Kompression eines Gases und Verfahren zum Füllen eines Tanks mit einer derartigen Vorrichtung
WO2022234087A1 (fr) 2021-05-06 2022-11-10 Van Halteren Technologies Boxtel B.V. Appareil pour comprimer un gaz et procédé de remplissage d'un réservoir faisant appel audit appareil
WO2024081660A1 (fr) * 2022-10-14 2024-04-18 Steelhead Composites, Inc. Système d'accumulateur de liquide ionique pour distribuer un gaz

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DE102004046316A1 (de) 2006-03-30
CN101023272B (zh) 2012-06-27
US20070258828A1 (en) 2007-11-08
ZA200702362B (en) 2008-08-27
ATE530772T1 (de) 2011-11-15
JP4986161B2 (ja) 2012-07-25
CN101023272A (zh) 2007-08-22
CA2581280A1 (fr) 2006-04-06
JP2008514844A (ja) 2008-05-08
AU2005289219A1 (en) 2006-04-06
EP1792087A1 (fr) 2007-06-06
KR20070057813A (ko) 2007-06-07
EP1792087B1 (fr) 2011-10-26

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