EP1672269A1 - Anordnung zum Fördern von gasförmigem Brennstoff zu einer Energieerzeugungseinheit eines Schiffes zum Transport von Flüssiggas - Google Patents

Anordnung zum Fördern von gasförmigem Brennstoff zu einer Energieerzeugungseinheit eines Schiffes zum Transport von Flüssiggas Download PDF

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Publication number
EP1672269A1
EP1672269A1 EP05111846A EP05111846A EP1672269A1 EP 1672269 A1 EP1672269 A1 EP 1672269A1 EP 05111846 A EP05111846 A EP 05111846A EP 05111846 A EP05111846 A EP 05111846A EP 1672269 A1 EP1672269 A1 EP 1672269A1
Authority
EP
European Patent Office
Prior art keywords
pressure
supply
evaporator
gas
outlet
Prior art date
Legal status (The legal status 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 status listed.)
Granted
Application number
EP05111846A
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English (en)
French (fr)
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EP1672269B1 (de
Inventor
Matthieu Lorang
Yves Blandeau
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Chantiers de lAtlantique SA
Original Assignee
Alstom SA
Aker Yards SA
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Filing date
Publication date
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Publication of EP1672269A1 publication Critical patent/EP1672269A1/de
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Publication of EP1672269B1 publication Critical patent/EP1672269B1/de
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

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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
    • F17C9/00—Methods or apparatus for discharging liquefied or solidified gases from vessels not under pressure
    • F17C9/02—Methods or apparatus for discharging liquefied or solidified gases from vessels not under pressure with change of state, e.g. vaporisation
    • 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
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B63—SHIPS OR OTHER WATERBORNE VESSELS; RELATED EQUIPMENT
    • B63H—MARINE PROPULSION OR STEERING
    • B63H21/00—Use of propulsion power plant or units on vessels
    • B63H21/38—Apparatus or methods specially adapted for use on marine vessels, for handling power plant or unit liquids, e.g. lubricants, coolants, fuels or the like
    • 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
    • F17C2205/01—Mounting arrangements
    • F17C2205/0123—Mounting arrangements characterised by number of vessels
    • F17C2205/013—Two or more vessels
    • 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
    • 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
    • F17C2205/0338—Pressure 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
    • F17C2221/00—Handled fluid, in particular type of fluid
    • F17C2221/03—Mixtures
    • F17C2221/032—Hydrocarbons
    • F17C2221/033—Methane, e.g. natural gas, CNG, LNG, GNL, GNC, 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
    • F17C2223/01—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
    • 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
    • F17C2225/0107—Single phase
    • F17C2225/0123—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
    • 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
    • F17C2227/01—Propulsion of the fluid
    • F17C2227/0128—Propulsion of the fluid with pumps or compressors
    • F17C2227/0157—Compressors
    • 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
    • F17C2227/0171—Arrangement
    • F17C2227/0178—Arrangement in 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
    • F17C2250/01—Intermediate tanks
    • 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
    • F17C2250/0443—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
    • F17C2265/00—Effects achieved by gas storage or gas handling
    • F17C2265/03—Treating the boil-off
    • 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
    • F17C2265/03—Treating the boil-off
    • F17C2265/032—Treating the boil-off by recovery
    • F17C2265/037—Treating the boil-off by recovery with 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
    • F17C2265/00—Effects achieved by gas storage or gas handling
    • F17C2265/06—Fluid distribution
    • F17C2265/066—Fluid distribution for feeding engines for propulsion
    • 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
    • F17C2270/0102—Applications for fluid transport or storage on or in the water
    • F17C2270/0105—Ships

Definitions

  • the invention relates to an installation for supplying gaseous fuel to an energy production assembly of a liquefied gas transport vessel, said gaseous fuel being compressed at a certain supply pressure by one or more apparatuses before supplying fuel to the fuel. set of energy production through at least one supply manifold.
  • the invention relates to the regulation and servocontrol of the pressurized gas supply of the gas-powered energy generator of a liquefied gas transport vessel, this unit possibly comprising, for example, one or more diesel groups or one or more several gas turbines.
  • the operating characteristics of a gas-fed energy generator generally imply that this gas supply is carried out under a relatively low supply pressure which may be, for example, of the order of four bars. In steady state, this power supply is generally performed under the correct conditions by the existing compression devices that are capable of delivering the desired flow rate and supply pressure.
  • These devices which include, for example, a compressor and / or a pump supplying an evaporator are generally controlled by pressure regulators located in particular at the level of the supply manifold so as to maintain in this supply manifold a pressure close to the pressure of setpoint supply.
  • Such a variation in the load of the energy production unit may be due to a request for acceleration or deceleration of the speed of the ship, to the commissioning or stopping of large consumers such as cargo pumps or other.
  • the power generator speed and the power they deliver are disturbed, so that this transition can cause the undesired termination of the energy generator by lack of fuel gas pressure or damage to the compression apparatus by failure to respect acceptable minimum or maximum pressure constraints.
  • an evaporator is fed by a submerged pump at the bottom of the tank.
  • the flow rate of the evaporator is regulated by a valve located upstream according to the pressure in the tank and / or the pressure in the supply manifold.
  • These installations are subject to the problem of the response time of the evaporator following a pressure variation in the supply manifold. This response time is due, among other things, to the filling of the evaporator and the phase changes.
  • This non-compressible inertia has the consequence, in case of variation of the load of the entire energy production, a variation of the pressure in the supply manifold and therefore the risks put forward previously.
  • the object of the invention is therefore to overcome the inertia of forced evaporation.
  • the subject of the invention is an installation for supplying gaseous fuel to an energy production assembly of a liquefied gas transport vessel, from the contents of at least one vessel of said vessel, comprising at least a compressor whose inlet sucks gas in the vapor phase into said tank, the output of the compressor discharging into a supply manifold of said energy production assembly, further comprising a pump immersed at the bottom of the tank and connected to the inlet an evaporator, the outlet of the evaporator being connected to said supply manifold of said energy production assembly via a supply line, characterized in that the pump is adapted to supply the evaporator with liquefied gas at a higher pressure at the supply pressure of said assembly, and in that said supply line is equipped with means for regulating the flow rate of the gas supplied to said feed collector ntation.
  • These regulation means are intended to progressively discharge the gas at the feed pressure into the manifold to regulate and stabilize the pressure, in case of variation of the load of the energy production assembly tending to temporarily vary the pressure of the feed. 'food.
  • the power supply conditions of the power generation assembly are optimal, even during the transient phases of charge variation.
  • the flow control means of the gas supplied to the supply manifold are connected to means for measuring pressure in said manifold.
  • a buffer tank is located upstream of the flow control means. In this way, it is possible to permanently have a reserve of gas at a pressure greater than the supply pressure of the energy production assembly to overcome any pressure variation in said manifold.
  • This buffer tank solution makes it possible to increase the volume of excess gas reserve if the volume of the pipe does not provide a sufficient safety volume because of its length and / or its diameter.
  • a cooling device is located on the outlet pipe of the evaporator, and gas pressure regulating means at the outlet of the evaporator are located upstream of the evaporator.
  • the cooling device thus makes it possible to reduce the temperature of the gas leaving the evaporator, and the pressure regulating means make it possible to maintain a pressure at the outlet of the evaporator lower than the pressure at the pump outlet to ensure the operation of the cooling device while maintaining upstream of the flow control means a gas pressure greater than the pressure in the supply manifold.
  • the pressure regulating means are connected to means for measuring pressure downstream of the cooling device.
  • the cooling device may further comprise a device for evaporation of liquefied gas from at least one tank and activated by the temperature measured in the pipe at the outlet of the cooling device.
  • the means for regulating the gas flow rate supplied to the supply manifold are also connected to means for measuring the gas flows produced by the compressor and the evaporator and consumed by the energy production unit and by a gas oxidation device, sometimes called incinerator or "oxidizer" in English.
  • a gas oxidation device sometimes called incinerator or "oxidizer” in English.
  • Figure 1 is a schematic representation of a first embodiment of the invention
  • Figure 2 is a schematic representation of a second embodiment of the invention.
  • FIG. 1 and 2 the elements dedicated to the production of energy on a LNG carrier are shown schematically and here comprise an assembly 1 for producing electrical energy and / or heat.
  • This set 1 may comprise diesel engines driving alternators for the production of electrical energy for the electrical installations of the ship and its propulsion, but could alternatively comprise a conventional assembly comprising a boiler for producing steam supplying a steam turbine for the propeller drive.
  • the energy production unit 1 is fed with gas that is taken from one or more tanks 2 of the LNG carrier.
  • the feed gas is most often methane which is directly taken from the tanks under a supply pressure of a few bars.
  • This feed gas is taken in parallel in two ways.
  • the gas in the vapor phase 4 is taken from the tank 2, above the surface of the liquid methane 5, to be compressed in a compressor 6 which is driven by a not shown electric motor.
  • This gas is then injected into a supply manifold 7 at the desired pressure to feed the assembly 1 of energy production.
  • a pump 8 immersed at the bottom of the tank 2 and electrically powered takes liquid methane 3 which is conducted in an evaporator 9.
  • the methane is in gaseous form to also feed the collector.
  • supply 7 of the assembly 1 of energy production via a supply line 10.
  • An overpressure evacuation pipe is connected to the supply manifold 7, downstream of the connection of the pipe 10 to this supply manifold, and leads to an oxidation device 11 of the gas.
  • overpressure can occur following a sudden decrease in the load of the unit 1, leading to a sudden drop in its gas consumption.
  • a gas flow control valve 12 is placed at the outlet of the pipe 10 and upstream of the supply manifold 7 of the assembly 1 so as to overcome a pressure variation. in this power collector.
  • This valve 12 may be slaved in particular by a pressure regulator 13 connected to the supply manifold and more generally be controlled by a control automaton.
  • the pump 8 supplies the evaporator 9 with liquefied gas at a pressure greater than the supply pressure of the energy production assembly 1.
  • the gas in the vapor phase at the outlet of the evaporator 9 is delivered to an pressure higher than the supply pressure established in the supply manifold 7, and which creates in the pipe 10 a reserve of high-pressure gas that can supply this supply manifold as required for the assembly 1 via the valve 12.
  • the valve 12 which connects the pipe 10 to the supply manifold 7 adapts its opening to discharge into the manifold a part of the reserve gas in the pipe 10, at the required supply pressure at the manifold. This makes it possible, for example, to compensate for a supply pressure drop in the collector due to a load increase of the assembly 1, in order to maintain the supply pressure at its setpoint.
  • a buffer tank 14 situated on the pipe 10 upstream of the regulation valve 12 is inflated to the outlet pressure of the evaporator 9, which pressure is greater than the pressure of supply of the assembly 1.
  • a buffer tank 14 situated on the pipe 10 upstream of the regulation valve 12 is inflated to the outlet pressure of the evaporator 9, which pressure is greater than the pressure of supply of the assembly 1.
  • FIG. 2 also shows a cooling device 15 comprising a device for injecting liquefied gas from at least one tank 2.
  • This device makes it possible to cool the gas at the outlet of the evaporator 9 so as to be in a temperature and pressure range allowing a reactivity of the valve 12 sufficient to maintain the supply pressure in the collector at its set point.
  • this cooling device 15 is activated by measuring the temperature at the outlet of the evaporator 9, the conventional measuring means not being shown in the figures.
  • another control valve 16 is situated at the inlet of the evaporator 9 in order to regulate the pressure at the outlet of said evaporator 9 from the measurement of this pressure by means 17. This ensures that this pressure is lower than the pump output pressure 8 supplying the cooling device 15 so as to create a fluid call.
  • This valve 16 also has as regulation set a pressure greater than the supply pressure of the supply manifold 7, so that the valve 12 can perform its function.
  • the valve 16 can also be regulated by means for measuring the flow rates of the gas consumed by the set 1 of energy production and by the gas oxidation device 11 and measuring the flow rates produced by the compressor 6 and the evaporator 9, in order to measure the difference between the gas flow rates respectively in production and consumption and to regulate the valve 16 in function.
  • This variant makes it possible to provide additional stability in pressure at the outlet of the evaporator 9, by a better reactivity.

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  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Mechanical Engineering (AREA)
  • Combustion & Propulsion (AREA)
  • General Engineering & Computer Science (AREA)
  • Ocean & Marine Engineering (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Filling Or Discharging Of Gas Storage Vessels (AREA)
EP05111846A 2004-12-10 2005-12-08 Anordnung zum Fördern von gasförmigem Brennstoff zu einer Energieerzeugungseinheit eines Schiffes zum Transport von Flüssiggas Expired - Fee Related EP1672269B1 (de)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
FR0452932A FR2879261B1 (fr) 2004-12-10 2004-12-10 Installation pour la fourniture de combustible gazeux a un ensemble de production energetique d'un navire de transport de gaz liquefie

Publications (2)

Publication Number Publication Date
EP1672269A1 true EP1672269A1 (de) 2006-06-21
EP1672269B1 EP1672269B1 (de) 2007-07-04

Family

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Family Applications (1)

Application Number Title Priority Date Filing Date
EP05111846A Expired - Fee Related EP1672269B1 (de) 2004-12-10 2005-12-08 Anordnung zum Fördern von gasförmigem Brennstoff zu einer Energieerzeugungseinheit eines Schiffes zum Transport von Flüssiggas

Country Status (7)

Country Link
EP (1) EP1672269B1 (de)
JP (1) JP4850503B2 (de)
KR (1) KR101167320B1 (de)
CN (1) CN100519335C (de)
DE (1) DE602005001546T2 (de)
ES (1) ES2290858T3 (de)
FR (1) FR2879261B1 (de)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP2072885A1 (de) * 2007-12-21 2009-06-24 Cryostar SAS Naturgasversorgungsverfahren und -vorrichtung
WO2009112478A1 (de) * 2008-03-10 2009-09-17 Burckhardt Compression Ag Vorrichtung und verfahren zum bereitstellen von erdgasbrennstoff
EP2121425A2 (de) * 2007-07-19 2009-11-25 Daewoo Shipbuilding & Marine Engineering Co., Ltd Kraftstoff-gas-zufuhrsystem und lieferverfahren
EP2332825A1 (de) * 2007-05-08 2011-06-15 Daewoo Shipbuilding & Marine Engineering Co., Ltd Brennstoffzufuhrsystem und -verfahren für einen LNG-Träger
US9234472B2 (en) 2012-08-08 2016-01-12 Caterpillar Inc. Dual fuel engine and evaporated natural gas system
WO2018162790A1 (en) * 2017-03-08 2018-09-13 Wärtsilä Finland Oy A liquefied gas tank arrangement and method of operating a liquefied gas tank arrangement
CN112512917A (zh) * 2018-11-14 2021-03-16 大宇造船海洋株式会社 用于向船舶供应燃料的系统和方法

Families Citing this family (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100812723B1 (ko) * 2006-12-18 2008-03-12 삼성중공업 주식회사 액화가스운반선의 연료 공급 장치 및 방법
DE102006061251B4 (de) * 2006-12-22 2010-11-11 Man Diesel & Turbo Se Gasversorgungsanlage für einen Antrieb
FR2927321B1 (fr) * 2008-02-08 2010-03-19 Gaztransp Et Technigaz Dispositif pour l'alimentation en combustible d'une installation de production d'energie d'un navire.
KR100961869B1 (ko) * 2009-10-16 2010-06-09 대우조선해양 주식회사 액화연료가스 주 추진 엔진과 액화연료가스 발전 엔진을 선택적으로 구동하는 선박
JP2012076561A (ja) * 2010-09-30 2012-04-19 Mitsubishi Heavy Ind Ltd 舶用燃料供給システム
JP5627628B2 (ja) * 2012-03-30 2014-11-19 三菱重工業株式会社 船舶、燃料供給装置、推進用主機への液化燃料ガスの供給方法
KR102044266B1 (ko) * 2012-10-24 2019-11-13 대우조선해양 주식회사 선박용 엔진의 연료공급 시스템 및 방법
JP5746301B2 (ja) * 2013-10-11 2015-07-08 三井造船株式会社 液化ガス運搬船用燃料ガス供給システム
KR101613204B1 (ko) * 2014-01-08 2016-04-29 대우조선해양 주식회사 선박용 엔진의 연료 공급 제어 시스템 및 방법
KR102234666B1 (ko) * 2014-10-23 2021-04-05 삼성중공업(주) 선박의 저압 연료 공급장치
KR20160120373A (ko) * 2015-04-07 2016-10-18 삼성중공업 주식회사 연료가스 공급시스템
KR101672175B1 (ko) * 2015-04-09 2016-11-04 삼성중공업 주식회사 연료가스 공급시스템
JP6541059B2 (ja) * 2015-04-10 2019-07-10 三井Ｅ＆Ｓ造船株式会社 液化ガス運搬船用燃料ガス供給システム
SG11201912007XA (en) * 2017-10-30 2020-01-30 Daewoo Shipbuilding & Marine Engineering Co Ltd Fuel oil supply system and method for ship
CN115414772B (zh) * 2022-08-30 2023-08-29 内蒙古伊东集团东兴化工有限责任公司 一种vcm压缩工艺装置

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EP1348620A1 (de) * 2002-03-26 2003-10-01 Alstom Vorrichtung zur Förderung von Gasbrennstoff zur Kraftanlage eines LNG-Schiffes
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EP2332825A1 (de) * 2007-05-08 2011-06-15 Daewoo Shipbuilding & Marine Engineering Co., Ltd Brennstoffzufuhrsystem und -verfahren für einen LNG-Träger
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EP2121425A4 (de) * 2007-07-19 2011-08-10 Daewoo Shipbuilding & Marine Kraftstoff-gas-zufuhrsystem und lieferverfahren
EP2072885A1 (de) * 2007-12-21 2009-06-24 Cryostar SAS Naturgasversorgungsverfahren und -vorrichtung
WO2009081278A1 (en) * 2007-12-21 2009-07-02 Cryostar Sas Natural gas supply method and apparatus
WO2009112478A1 (de) * 2008-03-10 2009-09-17 Burckhardt Compression Ag Vorrichtung und verfahren zum bereitstellen von erdgasbrennstoff
US9234472B2 (en) 2012-08-08 2016-01-12 Caterpillar Inc. Dual fuel engine and evaporated natural gas system
WO2018162790A1 (en) * 2017-03-08 2018-09-13 Wärtsilä Finland Oy A liquefied gas tank arrangement and method of operating a liquefied gas tank arrangement
CN112512917A (zh) * 2018-11-14 2021-03-16 大宇造船海洋株式会社 用于向船舶供应燃料的系统和方法
CN112512917B (zh) * 2018-11-14 2022-10-25 大宇造船海洋株式会社 用于向船舶供应燃料的系统和方法

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JP2006168719A (ja) 2006-06-29
CN1785748A (zh) 2006-06-14
ES2290858T3 (es) 2008-02-16
EP1672269B1 (de) 2007-07-04
FR2879261B1 (fr) 2007-04-13
KR20060065535A (ko) 2006-06-14
CN100519335C (zh) 2009-07-29
DE602005001546T2 (de) 2008-03-13
FR2879261A1 (fr) 2006-06-16
DE602005001546D1 (de) 2007-08-16
KR101167320B1 (ko) 2012-07-23
JP4850503B2 (ja) 2012-01-11

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