WO2004030794A2 - Compresseur de gaz a sechoir et commandes d'emissions radio - Google Patents

Compresseur de gaz a sechoir et commandes d'emissions radio Download PDF

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Publication number
WO2004030794A2
WO2004030794A2 PCT/CA2003/001474 CA0301474W WO2004030794A2 WO 2004030794 A2 WO2004030794 A2 WO 2004030794A2 CA 0301474 W CA0301474 W CA 0301474W WO 2004030794 A2 WO2004030794 A2 WO 2004030794A2
Authority
WO
WIPO (PCT)
Prior art keywords
gas
compressor
motor
condenser
flow
Prior art date
Application number
PCT/CA2003/001474
Other languages
English (en)
Other versions
WO2004030794A3 (fr
Inventor
Anthony Chan
Filip Antanassov
Ralph Rackman
Tome Mojsov
Tracey Demaline
Original Assignee
Fuelmaker Corporation
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
Priority claimed from US10/265,096 external-priority patent/US7011118B2/en
Priority claimed from CA002440255A external-priority patent/CA2440255A1/fr
Priority to CA2500915A priority Critical patent/CA2500915C/fr
Priority to AU2003273657A priority patent/AU2003273657A1/en
Priority to CN2003801049142A priority patent/CN1720090B/zh
Priority to JP2005500010A priority patent/JP4499659B2/ja
Application filed by Fuelmaker Corporation filed Critical Fuelmaker Corporation
Priority to EP03757569A priority patent/EP1558365A2/fr
Priority to BRPI0315044-5A priority patent/BR0315044B1/pt
Priority to MXPA05003602A priority patent/MXPA05003602A/es
Priority to US10/530,247 priority patent/US8016570B2/en
Publication of WO2004030794A2 publication Critical patent/WO2004030794A2/fr
Publication of WO2004030794A3 publication Critical patent/WO2004030794A3/fr

Links

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/26—Drying gases or vapours
    • B01D53/261—Drying gases or vapours by adsorption
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02—COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02B—INTERNAL-COMBUSTION PISTON ENGINES; COMBUSTION ENGINES IN GENERAL
    • F02B43/00—Engines characterised by operating on gaseous fuels; Plants including such engines
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02—COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02M—SUPPLYING COMBUSTION ENGINES IN GENERAL WITH COMBUSTIBLE MIXTURES OR CONSTITUENTS THEREOF
    • F02M21/00—Apparatus for supplying engines with non-liquid fuels, e.g. gaseous fuels stored in liquid form
    • F02M21/02—Apparatus for supplying engines with non-liquid fuels, e.g. gaseous fuels stored in liquid form for gaseous fuels
    • F02M21/0218—Details on the gaseous fuel supply system, e.g. tanks, valves, pipes, pumps, rails, injectors or mixers
    • F02M21/0227—Means to treat or clean gaseous fuels or fuel systems, e.g. removal of tar, cracking, reforming or enriching
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04B—POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS
    • F04B39/00—Component parts, details, or accessories, of pumps or pumping systems specially adapted for elastic fluids, not otherwise provided for in, or of interest apart from, groups F04B25/00 - F04B37/00
    • F04B39/0027—Pulsation and noise damping means
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04B—POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS
    • F04B39/00—Component parts, details, or accessories, of pumps or pumping systems specially adapted for elastic fluids, not otherwise provided for in, or of interest apart from, groups F04B25/00 - F04B37/00
    • F04B39/06—Cooling; Heating; Prevention of freezing
    • F04B39/066—Cooling by ventilation
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04B—POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS
    • F04B39/00—Component parts, details, or accessories, of pumps or pumping systems specially adapted for elastic fluids, not otherwise provided for in, or of interest apart from, groups F04B25/00 - F04B37/00
    • F04B39/16—Filtration; Moisture separation
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02T—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
    • Y02T10/00—Road transport of goods or passengers
    • Y02T10/10—Internal combustion engine [ICE] based vehicles
    • Y02T10/30—Use of alternative fuels, e.g. biofuels

Definitions

  • TITLE Gas Compressor with Drier and Radio Emission Controls
  • This invention relates to the compression of gases. More particularly, it relates to the compression of natural gas and/or hydrogen for use in vehicles propelled by such gases. Specifically, it relates to an apparatus and methods for removing moisture vapor as part of the compression procedure and separating removed moisture from contaminants therein. It also relates to minimizing the release of electromagnetic radiation.
  • de-watering processes generate extracted water that may contain traces of contaminants originating from the principal stream.
  • these contaminants include hydrogen sulphide, sulphur dioxide and mercaptans .
  • Disposal of water containing contaminants of this type can be subject to environmental restraints.
  • a compressor for a gas which normally operates on a gas compression ' cycle is provided with a gas drier stage comprising a single desiccant bed located in-line with the flow of gas passing through the compressor during the gas compression cycle. Also located in-line with such gas flow is a condenser which, during the compression cycle, is inactive.
  • the temperatures of the desiccant bed and condenser are both controllable, preferably by electrical means. During the compression cycle, such temperature controls are preferably inactive. However, upon entering into a regeneration cycle, the gas bed is heated and the condenser is cooled.
  • gas trapped within the compressor, desiccant bed and condenser is redirected from the outlet of the compressor for circulation in a closed loop as a recirculating gas flow through the compressor, with at least a portion of such recirculating gas passing through the dessicant bed and condenser.
  • the outlet from the compressor is connected through an electronically controlled valve to the delivery line which carries compressed gas off to a storage reservoir during the compression cycle.
  • the electronically controlled delivery valve switches the flow of gas .from the delivery line into the interior • volume of a casing cavity for the compressor. The compressor draws its input from the casing cavity.
  • the resulting drop of pressure in the delivery line causes a check valve at the external reservoir, which contains high pressure gas, to close.
  • the compressed gas trapped in the delivery line then "blows down" into the interior volume of the casing, producing a pressure condition that is moderately elevated above that of the supply line pressure eg 30-60 psi.
  • the check valve at the supply line inlet to the interior volume then closes as the source gas pressure is only of the order of 0.2 to 0.5 psi.
  • Circulation of the gas within this closed loop is effected at a low gas flow rate so that the circulating gas passing through the condenser is substantially, preferably fully, chilled when it exits the condenser. This maximizes the efficiency of transferring moisture from the desiccant bed to the condenser as a preferred mode of operation. Circulation may be effected at a low flow rate by reducing the speed of the compressor motor. Alternately, one or more valve-controlled bypass lines may divert a portion of the circulating gas around the dessicant bed, and/or the condenser, allowing only a limited amount of gas flow through these components.
  • the permitted flow rate over the bed is set so as to be commensurate with the condensation of vapor from such gas.
  • This arrangement allows the system to operate with a fixed speed motor.
  • water evolves from the desiccant bed, raising the moisture content of the circulating gas.
  • the desiccant bed is heated at . this stage to enhance its release of moisture.
  • the released water, in vapor form is then carried by the gas flow to the condenser where it condenses due to the low temperature condition maintained within the condenser. Circulating gas exiting the condenser leaves the condenser in a cooled, vapor saturated, condition.
  • the circulating gas By the time the circulating gas reaches the heated desiccant bed, its temperature has been raised and the gas is no longer vapor saturated.
  • the heated circulating gas is therefore able to absorb further moisture from the desiccant bed as it passes over such bed.
  • water may simply be collected.
  • the condensed water is directed, preferably flowing under gravity, into contact with a semi-permeable membrane which allows the water to evaporate.
  • aromatic compounds present within the condensate are retained by the membrane within the condenser.
  • an external fan and optional heater element may be preferably positioned to circulate warm air past the membrane surface.
  • the condenser is located in-line with the gas flow during the compression cycle. This exposes the condenser and semipermeable membrane to an elevated pressure condition.
  • the compressor is a multi-stage compressor and the desiccant bed and condenser are positioned in-line between consecutive stages, preferably between the first and second stages of the compressor.
  • condensed water accumulating in the condenser is directly, or eventually, disposed of by release into the environment, preferably through the semi-permeable membrane.
  • Use of such a membrane ensures separation and retention of complex
  • the compressor is contained within a sealed metal casing.
  • Supply gas enters the interior volume of this casing through a check valve and is drawn into the compressor from the crank-portion of this interior volume.
  • the motor preferably a variable speed motor, and preferably control circuitry for delivering current to the motor.
  • the motor is an alternating current induction motor, and in the variable speed situation the control circuitry produces an alternating current signal of varying frequency, whereby the speed of the motor is varied in accordance with system requirements .
  • the control circuitry may deliver current at 360 volts DC provided through a sealed penetration of the casing wall.
  • the motor control circuitry operates to create alternating current having a frequency of on the order 60 Hz but with multiple harmonics.
  • the electrical power delivered to the motor provides current, at a typical maximum level, of on the order of 8 to 10 amps.
  • the electromagnetic radiation from the wiring extending between the control circuitry of the motor carrying a such current at such frequencies is a source of electromagnetic radiation. By confining this wiring to within the metallic casing, electromagnetic radiation from this source is shielded from entering into the environment.
  • low motor speeds are preferably adopted to reduce otherwise high start-up current drains on the electrical supply system.
  • This enables the unit to operate off of a standard household voltage, e.g. 110-120 volt, moderately fused electrical supply system.
  • initial compression can be effected with a high motor speed.
  • the motor speed is reduced in order to moderate ring wear and limit power consumption.
  • This procedure is especially suited to oil-less compressors as the wear rate of the sealing rings within the compressor cylinders of such units increases when the compressor system is operated at high speed against a high-back pressure.
  • the speed of the electric motor may also be controlled to avoid natural resonant frequencies arising from its mechanical components that would otherwise increase the noise and vibration generated by the unit.
  • Figure 1 is a pictorial representation of a gaseous fuel motor vehicle parked in a garage having a home refueling appliance according to the invention mounted on its inner wall.
  • Figure 2 is a schematic for the basic components of the appliance showing besides the motor and compressor, the desiccant bed, the main logic controller, the motor control circuitry and various sensors.
  • Figure 3 is a schematic variant of Figure 2 showing gas flow during the compression cycle.
  • Figure 4 is a schematic as in Figure 2 showing the basic flow diagram of the appliance during the regeneration cycle wherein the desiccant bed is recharged and the motor speed is variable.
  • Figure 5 is a cross-sectional side view of the compressor/motor assembly within its -immediate case and the drier components. This compressor casing - contains the motor, a blow-down volume, and the motor control circuitry. Also shown is an additional, outer case or ventilation shroud to contain cooling air flow.
  • Figure 6 is a detailed schematic cross-sectional front view of the drier, condenser, and semi -permeable membrane portions of Figure 2 with the semi-permeable membrane in the - form of a tube through which water condensate enters under gravity.
  • Figure 6A is a cross-sectional front view of the drier, condenser, and semi-permeable membrane portions of Figure 6 showing the semi -permeable membrane tube through which water condensate evaporates in the presence of a heated airflow created by a fan.
  • Figure 7 is a detailed, close-up, cross-sectional side view of the semi permeable membrane of Figures 5 and 6a showing airflow around the coiled tubing.
  • Figures 8A and 8B are schematics as in Figure 2 showing the basic flow diagram of the appliance during the regeneration cycle wherein the motor speed is fixed and the drier-condenser has a bypass line that can divert flow past the drier-condenser by switching flow into the circulating loop or to the casing cavity, or both, to permit a reduced gas flow rate to occur within the condenser.
  • FIG. 1 the home refueling appliance 1 is shown mounted on a garage wall with the high-pressure discharge or delivery hose 2 connected to a car, the inlet or supply hose 3 providing a source of gas 6, and the electrical cord 4 plugged into a standard household receptacle.
  • Figure 2 schematically depicts the unit operating in compression mode.
  • line gas 6 which may contain contaminants 8, enters the interior volume 14 of the casing 26 from which it drawn into the first of a series of four compression stages 28, 32, 33, 34 of compressor 5.
  • the line gas 6, which typically has a pressure of between 0.2 and 0.5 psi is drawn into the interior volume 14 by the suction created by the first compression stage 28.
  • a line gas pressure sensor 21 detects the line gas pressure, providing a signal to the main logic controller 46.
  • the gas 6 passes through - a desiccant bed 7 contained within an absorption chamber 29.
  • the dried gas Upon exiting the absorption chamber 29, the dried gas continues into the volume of a condenser 30 which is, at this stage, passive. Exiting the condenser 30 through conduit 55, the gas 6 proceeds to the next, second stage 32 of the compressor 5.
  • the flow of gas in this compression cycle is shown in Figure 3.
  • the desiccant 7 is regenerated by being exposed to a sweep gas 13 originating from the gas stream trapped in the compressor 5, motor 27, desiccant bed 7 and condenser 30 when the compression cycle is terminated.
  • the sweep gas 13 is drawn at a reduced flow rate through the absorbent bed 7, optionally by the slow speed operation of the change to motor 27.
  • Moisture in the adsorbent bed 7 is encouraged to vaporize into the sweep gas 13 by its dry condition, as described further below, by its pressure and the by the additional supply of heating to the absorbent bed 7.
  • the gas flows into condenser 30 which contains a heat-exchange surface.
  • This heat-exchange surface is preferably cooled by an electrical- actuated cooling block 53 operating on the basis of the Peltier effect. Cooled, circulating sweep gas 13, which has now been de- moisturized in the condenser 30, then passes into a return conduit 55 that leads to the second stage 32 of the compressor. The slow operation of the motor 27 and compressor 5 causes this sweep gas 13 to circulate endlessly until the regeneration cycle is terminated.
  • a thermostatically controlled electrical element 52 warms the desiccant 7.
  • the warmed, moisturized sweep gas more effectively releases moisture as it passes through the condenser 30.
  • liquified water 54 accumulates in the bottom of the condenser 30 as a condensate, below the level of the return conduit 55 within the condenser.
  • the condensed water 54 will contain some residual contaminants 8a.
  • This water condensate 54, including residual contaminants 8a present therein, may be simply accumulated and collected or it may then be passed to a separation chamber preferably in the form of tubing 31 that has walls formed of a semi -permeable membrane 61.
  • the semi -permeable membrane 61 allows only the penetration of water as the permeate.
  • water diffusing therethrough evaporates. This process may be accelerated by an airflow originating from a fan 42.
  • the shroud 43 serves to duct a constant air flow over the membrane 61.
  • the air flow in the vicinity of the membrane may be heated by a membrane heater 56.
  • the circulating airflow 60 from the fan 42 may also be used to cool the condenser 30, preferably using separate ducting (not shown) .
  • the semi-permeable membrane 61 could be in the form of a plate fitted as part of a wall of a separation chamber.
  • Figures 6 and 7 show a preferred variant in which the semi-permeable membrane is shown as a tube 31.
  • This tube 31 is preferably has a wall formed of semi-permeable hydroscopic ion exchange membrane material.
  • Membranes in the form of tubes- made of modified Teflon (TM) have been found suitable for this application, showing life-times of practical duration.
  • the absorbent chamber 29 and condenser 30 are contained within the • high pressure zone of the compressor 5, between the first stage 28 and the second stage 32.
  • the pressure in this zone is only on order of 200 psi during the compression cycle. In fact, this pressure level enhances the gas drying effect. It has been found that, at these pressure levels, the semi-permeable membrane 61 in tubing format can extend outside this pressurized zone, relying on secure couplings 57 to seal the connection between the tubing 31 and the condenser, chamber 30.
  • the use of the multistage compressor especially facilitates this arrangement .
  • FIG. 2 Further components as shown in Figure 2 include an inlet filter 22, a high pressure transducer 24, a pressure relief valve 25 leading to a vent opening 50, a burst disc 35 in the fourth stage 34 to relieve excessive over-pressure, an in-line breakaway connector 36, the vehicle connection nozzle 38, a gas leak-detecting sensor 39, an air flow sensor 40, and an ambient air temperature sensor 41.
  • FIGs 8A and 8B a fixed speed motor variant is shown wherein a bypass line 60 or 60A is opened by valve 61 actuated by the main logic controller 46 during regeneration. Due to this bypass, the sweep gas 13 passes through the desiccant material 7 and condenser 30 at a preferred flow rate. The amount of sweep gas 13 allowed by valve 61 and associated flow-limiting means to pass through this regeneration branch is set to maximize the efficiency of the vapor evaporation and condensation process. Recirculating gas 13 is either diverted to the second stage 32 through bypass .line 60, or to the casing volume 14 through bypass line 60A, or both bypass lines may be used in combination.
  • the compressor 5, motor 27 and motor control circuitry 45 are all located within the casing 26, (counting the compressor block as part of the casing), which is in turn, surrounded by an outer shroud 43.
  • the electronic motor controller 45 which supplies current to the electrical motor 27, is preferably located within the totally contained environment of ' the motor/compressor assembly. This sealed environment is provided by the same metal casing 26 that surrounds the motor and compressor parts.
  • the motor control circuitry 45 is, in particular, located in the blow-down volume 14, sealed entirely within the casing 26.
  • the metallic wall of -the casing 26 acts as heat sink for the heat produced by the motor control circuitry 45 and as a shield for outgoing electromagnetic emissions arising from wiring extending between the motor 27 and motor controller 45.
  • the main logic controller 46 fed power from a power supply 47, , is able to activate the motor 27, and govern its speed in the variable speed version, through motor control circuitry 45.
  • the command logic circuitry 46 sends and receives commands and data through digitally encoded signals transmitted along optical fibers. This minimizes the electrical penetrations made into the interior 14 of the metal cavity of the casing 26 which contains natural gas in a slightly pressurized condition.

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • General Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Analytical Chemistry (AREA)
  • Drying Of Gases (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)
  • Compressor (AREA)
  • Separation By Low-Temperature Treatments (AREA)

Abstract

Cette invention concerne une unité compresseur de gaz comprenant un seul lit de dessiccation du gaz et un condenseur (qui est inactif pendant la phase de compression) introduit dans le circuit d'écoulement du gaz du cycle de compression. Dans le cas d'un compresseur à plusieurs étages, le lit de dessiccation du gaz unique est placé de préférence entre le premier et le deuxième étage. L'humidité absorbée par le lit est périodiquement évacuée au moyen d'un procédé consistant à exposer le lit à un cycle de régénération. Le cycle de régénération utilisé repose sur la recirculation fermée du gaz présent dans le compresseur et le lit de dessiccation lui-même, ainsi que d'un autre gaz présent dans la boucle de recirculation lorsque le compresseur interrompt la distribution de gaz comprimé. L'humidité évacuée du lit de dessiccation est condensée et de préférence s'évapore dans le milieu ambiant par une membrane semi-perméable. Le moteur et l'unité de commande du moteur sont placés avec le compresseur dans un logement commun afin que les émissions électromagnétiques soient réduites au minimum.
PCT/CA2003/001474 2002-10-04 2003-10-06 Compresseur de gaz a sechoir et commandes d'emissions radio WO2004030794A2 (fr)

Priority Applications (8)

Application Number Priority Date Filing Date Title
US10/530,247 US8016570B2 (en) 2002-10-04 2003-10-06 Gas compressor with drier and radio emission controls
MXPA05003602A MXPA05003602A (es) 2002-10-04 2003-10-06 Compresor de gas con secador.
AU2003273657A AU2003273657A1 (en) 2002-10-04 2003-10-06 Gas compressor with drier
CN2003801049142A CN1720090B (zh) 2002-10-04 2003-10-06 压缩机设备
JP2005500010A JP4499659B2 (ja) 2002-10-04 2003-10-06 乾燥器を有する気体用の圧縮器
CA2500915A CA2500915C (fr) 2002-10-04 2003-10-06 Compresseur de gaz a sechoir et commandes d'emissions radio
EP03757569A EP1558365A2 (fr) 2002-10-04 2003-10-06 Compresseur de gaz a sechoir
BRPI0315044-5A BR0315044B1 (pt) 2002-10-04 2003-10-06 sistema de compressão para gás.

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
US10/265,096 2002-10-04
US10/265,096 US7011118B2 (en) 2002-10-04 2002-10-04 Residential compressor for refueling motor vehicles that operate on gaseous fuels
CA2,440,255 2003-09-09
CA002440255A CA2440255A1 (fr) 2003-09-09 2003-09-09 Compresseur a gaz avec sechoir et commandes d'emissions radioelectriques

Publications (2)

Publication Number Publication Date
WO2004030794A2 true WO2004030794A2 (fr) 2004-04-15
WO2004030794A3 WO2004030794A3 (fr) 2004-06-17

Family

ID=32070534

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/CA2003/001474 WO2004030794A2 (fr) 2002-10-04 2003-10-06 Compresseur de gaz a sechoir et commandes d'emissions radio

Country Status (7)

Country Link
EP (1) EP1558365A2 (fr)
JP (1) JP4499659B2 (fr)
AU (1) AU2003273657A1 (fr)
BR (1) BR0315044B1 (fr)
MX (1) MXPA05003602A (fr)
RU (1) RU2336434C2 (fr)
WO (1) WO2004030794A2 (fr)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2009031005A2 (fr) * 2007-09-04 2009-03-12 Toyota Jidosha Kabushiki Kaisha Moteur à hydrogène du type à circulation de gaz de travail
RU2469696C2 (ru) * 2006-10-16 2012-12-20 Кэафьюжн 303, Инк. Вентилируемый адаптер для флаконов, снабженный фильтром для задержания аэрозоля
EP3486486A1 (fr) * 2017-11-16 2019-05-22 Multisorb Technologies, Inc. Système de climatisation avec corps de sorbant intégré

Families Citing this family (3)

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Publication number Priority date Publication date Assignee Title
WO2014116260A1 (fr) * 2013-01-28 2014-07-31 Gas Technology Energy Concepts Llc Module d'alimentation en combustible
WO2020109846A1 (fr) * 2018-11-29 2020-06-04 Хайджен, Сиа Dispositif pour assurer la sécurité de remplissage d'un moyen de transport par du carburant gazeux comprimé plus léger que l'air et procédé correspondant
BE1027367B1 (nl) 2019-06-13 2021-01-21 Atlas Copco Airpower Nv Statische droger

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US4966206A (en) * 1987-07-23 1990-10-30 Sulzer Brothers Limited Device for filling a gaseous fuel container
US5029622A (en) * 1988-08-15 1991-07-09 Sulzer Brothers Limited Gas refuelling device and method of refuelling a motor vehicle
US5263826A (en) * 1991-05-30 1993-11-23 Sulzer Brothers Limited Device for refueling a gaseous fuel tank
EP0799635A1 (fr) * 1996-04-02 1997-10-08 Atlas Copco Airpower N.V. Procédé et dispositif pour le séchage d'un gaz comprimé
US6117211A (en) * 1994-02-21 2000-09-12 Fuelmaker Corporation Gas desiccation and contaminant disposal method and apparatus
WO2001078872A2 (fr) * 2000-04-13 2001-10-25 Atlas Copco Airpower, Naamloze Vennootschap Installation de compresseur dote d'un dispositif de sechage

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US6220052B1 (en) * 1999-08-17 2001-04-24 Liberty Fuels, Inc. Apparatus and method for liquefying natural gas for vehicular use

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Publication number Priority date Publication date Assignee Title
US4966206A (en) * 1987-07-23 1990-10-30 Sulzer Brothers Limited Device for filling a gaseous fuel container
US5029622A (en) * 1988-08-15 1991-07-09 Sulzer Brothers Limited Gas refuelling device and method of refuelling a motor vehicle
US5263826A (en) * 1991-05-30 1993-11-23 Sulzer Brothers Limited Device for refueling a gaseous fuel tank
US6117211A (en) * 1994-02-21 2000-09-12 Fuelmaker Corporation Gas desiccation and contaminant disposal method and apparatus
EP0799635A1 (fr) * 1996-04-02 1997-10-08 Atlas Copco Airpower N.V. Procédé et dispositif pour le séchage d'un gaz comprimé
WO2001078872A2 (fr) * 2000-04-13 2001-10-25 Atlas Copco Airpower, Naamloze Vennootschap Installation de compresseur dote d'un dispositif de sechage

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See also references of EP1558365A2 *

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
RU2469696C2 (ru) * 2006-10-16 2012-12-20 Кэафьюжн 303, Инк. Вентилируемый адаптер для флаконов, снабженный фильтром для задержания аэрозоля
WO2009031005A2 (fr) * 2007-09-04 2009-03-12 Toyota Jidosha Kabushiki Kaisha Moteur à hydrogène du type à circulation de gaz de travail
WO2009031005A3 (fr) * 2007-09-04 2009-06-18 Toyota Motor Co Ltd Moteur à hydrogène du type à circulation de gaz de travail
EP3486486A1 (fr) * 2017-11-16 2019-05-22 Multisorb Technologies, Inc. Système de climatisation avec corps de sorbant intégré

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RU2336434C2 (ru) 2008-10-20
BR0315044B1 (pt) 2011-08-23
JP2006502374A (ja) 2006-01-19
WO2004030794A3 (fr) 2004-06-17
EP1558365A2 (fr) 2005-08-03
JP4499659B2 (ja) 2010-07-07
BR0315044A (pt) 2005-09-06
AU2003273657A1 (en) 2004-04-23
MXPA05003602A (es) 2006-04-05
RU2005113866A (ru) 2005-10-10
AU2003273657A8 (en) 2004-04-23

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