JPWO2021061253A5 - - Google Patents

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JPWO2021061253A5
JPWO2021061253A5 JP2022514757A JP2022514757A JPWO2021061253A5 JP WO2021061253 A5 JPWO2021061253 A5 JP WO2021061253A5 JP 2022514757 A JP2022514757 A JP 2022514757A JP 2022514757 A JP2022514757 A JP 2022514757A JP WO2021061253 A5 JPWO2021061253 A5 JP WO2021061253A5
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pump
tank
cryogenic liquid
cryogenic
location
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Priority claimed from PCT/US2020/040292 external-priority patent/WO2021061253A1/en
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Claims (16)

極低温液体を貯蔵して搬送するための運搬船であって、
液化温度を有する極低温液体を貯蔵して搬送するように構成されたタンクと、
前記タンクを前記極低温液体で充填し、かつ、前記極低温液体の第１の部分の前記タンクを空にし、それによって該極低温液体の第２の部分を該タンクに残す、ように構成された第１のポンプと、
前記極低温液体の前記第２の部分を前記タンクの底部上の場所に集中させるタンク構造と、
前記場所に位置付けられ、かつ前記極低温液体の前記第２の部分の前記タンクを空にし、それによって該極低温液体の残留部分がそこに残されるように構成された第２のポンプと、
を含み、
さらに、前記場所に熱を送出するように構成された集中加熱構造であって、該熱が、前記残留部分の温度を前記液化温度よりも高く上昇させ、それによって該残留部分の全てを気化させるように構成される前記集中加熱構造、
を含む、運搬船。 A carrier for storing and transporting cryogenic liquids, comprising:
a tank configured to store and convey a cryogenic liquid having a liquefaction temperature;
configured to fill the tank with the cryogenic liquid and empty the tank of a first portion of the cryogenic liquid, thereby leaving a second portion of the cryogenic liquid in the tank; a first pump;
a tank structure for concentrating the second portion of the cryogenic liquid at a location on the bottom of the tank;
a second pump positioned at the location and configured to empty the tank of the second portion of the cryogenic liquid, thereby leaving a residual portion of the cryogenic liquid therein;
including
Further, a centralized heating structure configured to deliver heat to the location, the heat raising the temperature of the residual portion above the liquefying temperature, thereby vaporizing all of the residual portion. said centralized heating structure configured to:
including carriers. 前記タンク構造は、前記第２のポンプを取り囲むバッフルを含み、該バッフルは、前記タンクの前記底部に取り付けられる、請求項１に記載の運搬船。 2. The carrier of claim 1, wherein said tank structure includes a baffle surrounding said second pump, said baffle attached to said bottom of said tank. 前記第２のポンプを前記バッフル、バッフル上部、及び前記タンクの前記底部内に封入するバッフル上部を更に含む、請求項２に記載の運搬船。 3. The carrier of claim 2, further comprising a baffle top enclosing said second pump within said baffle, baffle top, and said bottom of said tank. 前記タンク構造は、前記タンクの前記底部にポンプウェルを含み、該ポンプウェルは、該タンクの該底部の陥凹部分を含み、前記陥凹部分の中に前記第２のポンプが位置付けられた、請求項１に記載の運搬船。 The tank structure includes a pump well in the bottom of the tank, the pump well including a recessed portion in the bottom of the tank, and the second pump positioned in the recessed portion. A carrier according to claim 1. 前記ポンプウェルを覆い、かつ前記第２のポンプを該ポンプウェルに封入するポンプウェル上部を更に含む、請求項４に記載の運搬船。 5. The carrier of claim 4, further comprising a pump well top covering said pump well and enclosing said second pump in said pump well. 前記集中加熱構造は、前記第２のポンプに隣接する出口を有するガス注入ラインを含み、該ガス注入ラインは、前記タンクの前記底部での前記場所にガスを導入するように構成され、該ガスは、前記液化温度よりも高い温度を有する、請求項１に記載の運搬船。 The centralized heating structure includes a gas injection line having an outlet adjacent to the second pump, the gas injection line configured to introduce gas to the location at the bottom of the tank, the gas has a temperature above said liquefying temperature. 前記第１のポンプ５に接続され、かつ前記極低温液体をタンク内に又はタンクから搬送するように構成された第１のポンプラインであって、前記ガス注入ラインが該第１のポンプライン内に配置される前記第１のポンプラインを更に含む、請求項６に記載の運搬船。 a first pump line connected to the first pump 5 and configured to convey the cryogenic liquid into or out of a tank, the gas injection line being in the first pump line; 7. The carrier according to claim 6, further comprising said first pumpline located in a . 前記集中加熱構造は、前記タンクの前記底部上の前記場所の下に配置された加熱要素を含み、
前記加熱要素は、前記極低温液体の前記残留部分を前記液化温度よりも高く加熱するように構成される、
請求項１に記載の運搬船。 the centralized heating structure includes a heating element positioned below the location on the bottom of the tank;
the heating element is configured to heat the remaining portion of the cryogenic liquid above the liquefaction temperature;
A carrier according to claim 1. 液化極低温液体を運搬船で搬送する方法であって、
両用極低温貯蔵タンク内で液化温度を有する極低温液体を貯蔵して搬送する段階と、
第１のポンプを使用して前記極低温液体の第１の部分の前記極低温貯蔵タンクを空にし、それによって該極低温液体の第２の部分を前記極低温貯蔵タンクに残す段階と、
前記極低温貯蔵タンクの底部上の場所に前記極低温液体の前記第２の部分を集中させる段階と、
前記場所に位置付けられた第２のポンプを使用して前記極低温液体の前記第２の部分の前記極低温貯蔵タンクを空にし、それによって該極低温液体の残留部分がそこに残される段階と、
を含み、
さらに、集中加熱構造を使用して前記場所にのみ熱を送出する段階と、
前記集中加熱構造を使用して前記残留部分の温度を前記液化温度よりも高く上昇させ、それによって該残留部分の全てを気化させる段階と、
を含む、方法。 A method of transporting a liquefied cryogenic liquid in a carrier vessel, comprising:
storing and conveying a cryogenic liquid having a liquefaction temperature in a dual-purpose cryogenic storage tank;
emptying the cryogenic storage tank of a first portion of the cryogenic liquid using a first pump, thereby leaving a second portion of the cryogenic liquid in the cryogenic storage tank;
concentrating the second portion of the cryogenic liquid at a location on the bottom of the cryogenic storage tank;
emptying the cryogenic storage tank of the second portion of the cryogenic liquid using a second pump positioned at the location, thereby leaving a residual portion of the cryogenic liquid therein; ,
including
further delivering heat only to said location using a centralized heating structure;
raising the temperature of the residual portion above the liquefying temperature using the centralized heating structure, thereby vaporizing all of the residual portion;
A method, including 前記極低温液体の前記第２の部分は、前記第２のポンプを取り囲むバッフルを使用して集中させられ、該バッフルは、前記極低温貯蔵タンクの前記底部に取り付けられる、請求項９に記載の方法。 10. The method of claim 9, wherein said second portion of said cryogenic liquid is concentrated using a baffle surrounding said second pump, said baffle attached to said bottom of said cryogenic storage tank. Method. 前記第２のポンプを前記バッフルと、バッフル上部と、前記極低温貯蔵タンクの前記底部との間に封入するバッフル上部を更に含む、請求項１０に記載の方法。 11. The method of claim 10, further comprising a baffle top enclosing said second pump between said baffle, baffle top and said bottom of said cryogenic storage tank. 前記極低温液体の前記第２の部分は、前記極低温貯蔵タンクの前記底部でポンプウェルを使用して集中させられ、該ポンプウェルは、前記第２のポンプがその中に位置付けられた該極低温貯蔵タンクの該底部の陥凹部分を含む、請求項９に記載の方法。 The second portion of the cryogenic liquid is concentrated using a pump well at the bottom of the cryogenic storage tank, the pump well being the pole in which the second pump is positioned. 10. The method of claim 9, including a recessed portion of said bottom of a cryogenic storage tank. 前記ポンプウェルを覆い、かつ該ポンプウェルに前記第２のポンプを封入するポンプウェル上部を更に含む、請求項１２に記載の方法。 13. The method of claim 12, further comprising a pump well top covering the pump well and enclosing the second pump in the pump well. 前記集中加熱構造は、前記第２のポンプに隣接する出口を有するガス注入ラインを含み、
方法が、
前記ガス注入ラインを使用して、前記液化温度よりも高い温度を有するガスを前記極低温貯蔵タンクの前記底部で前記場所に導入する段階、
を更に含む、
請求項９に記載の方法。 the centralized heating structure includes a gas injection line having an outlet adjacent to the second pump;
the method is
introducing a gas having a temperature above the liquefaction temperature to the location at the bottom of the cryogenic storage tank using the gas injection line;
further comprising
10. The method of claim 9. 前記第１のポンプに接続された第１のポンプラインを使用して前記極低温液体を前記極低温貯蔵タンク内に又はそこから外に搬送する段階と、
前記ガス注入ラインを前記第１のポンプライン内に配置する段階と、
を更に含む、請求項１４に記載の方法。 conveying the cryogenic liquid into or out of the cryogenic storage tank using a first pump line connected to the first pump;
positioning the gas injection line within the first pump line;
15. The method of claim 14, further comprising: 前記集中加熱構造は、前記タンクの前記底部上の前記場所の下に配置された加熱要素を含み、
方法が、
前記加熱要素を使用して前記極低温液体の前記残留部分を前記液化温度よりも高く加熱する段階、
を更に含む、
請求項９に記載の方法。 the centralized heating structure includes a heating element positioned below the location on the bottom of the tank;
the method is
heating the remaining portion of the cryogenic liquid above the liquefaction temperature using the heating element;
further comprising
10. The method of claim 9.
JP2022514757A 2019-09-24 2020-06-30 Cargo stripping capabilities for dual-purpose cryogenic tanks on ships or floating storage units for LNG and liquid nitrogen Pending JP2022548529A (en)

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US201962904966P 2019-09-24 2019-09-24
US62/904,966 2019-09-24
PCT/US2020/040292 WO2021061253A1 (en) 2019-09-24 2020-06-30 Cargo stripping features for dual-purpose cryogenic tanks on ships or floating storage units for lng and liquid nitrogen

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JP2022548529A JP2022548529A (en) 2022-11-21
JPWO2021061253A5 true JPWO2021061253A5 (en) 2023-06-28

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FR3126119A1 (en) * 2021-08-16 2023-02-17 Gaztransport Et Technigaz Liquid gas storage and/or transport tank intended for a ship

Family Cites Families (152)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3103427A (en) 1963-09-10 Carbon dioxide freezeout system
US2011550A (en) 1930-12-26 1935-08-13 Carbonic Dev Corp Manufacture of solid carbon dioxide
US1914337A (en) 1931-01-17 1933-06-13 Joseph S Belt Process of producing solid carbon dioxide
US1974145A (en) 1932-06-30 1934-09-18 Standard Oil Co Air conditioning
US2007271A (en) 1932-09-23 1935-07-09 American Oxythermic Corp Process for the separation of constituents of a gaseous mixture
US2321262A (en) 1939-11-01 1943-06-08 William H Taylor Space heat transfer apparatus
US2361865A (en) * 1941-01-18 1944-10-31 Bastian Biessing Co Liquefied petroleum gas system
US2475255A (en) 1944-03-17 1949-07-05 Standard Oil Dev Co Method of drying gases
US2537045A (en) 1949-02-08 1951-01-09 Hydrocarbon Research Inc Cooling gases containing condensable material
US2975604A (en) 1956-05-07 1961-03-21 Little Inc A Method of distribution of condensable gases
US2900797A (en) 1956-05-25 1959-08-25 Kurata Fred Separation of normally gaseous acidic components and methane
US2986010A (en) 1958-07-07 1961-05-30 Conch Int Methane Ltd Purge means for storage tank
US3018632A (en) 1959-05-11 1962-01-30 Hydrocarbon Research Inc Cyclic process for transporting methane
US3014082A (en) 1959-12-23 1961-12-19 Pure Oil Co Method and apparatus for purifying and dehydrating natural gas streams
US3180709A (en) 1961-06-29 1965-04-27 Union Carbide Corp Process for liquefaction of lowboiling gases
US3347055A (en) 1965-03-26 1967-10-17 Air Reduction Method for recuperating refrigeration
US3376709A (en) 1965-07-14 1968-04-09 Frank H. Dickey Separation of acid gases from natural gas by solidification
US3370435A (en) 1965-07-29 1968-02-27 Air Prod & Chem Process for separating gaseous mixtures
DE1501730A1 (en) 1966-05-27 1969-10-30 Linde Ag Method and device for liquefying natural gas
US3400512A (en) 1966-07-05 1968-09-10 Phillips Petroleum Co Method for removing water and hydrocarbons from gaseous hci
US3398544A (en) 1966-07-27 1968-08-27 Continental Oil Co Solidification of acidic components in natural gas
US3400547A (en) 1966-11-02 1968-09-10 Williams Process for liquefaction of natural gas and transportation by marine vessel
DE1960515B1 (en) 1969-12-02 1971-05-27 Linde Ag Method and device for liquefying a gas
US3724225A (en) 1970-02-25 1973-04-03 Exxon Research Engineering Co Separation of carbon dioxide from a natural gas stream
US3878689A (en) 1970-07-27 1975-04-22 Carl A Grenci Liquefaction of natural gas by liquid nitrogen in a dual-compartmented dewar
FR2131985B1 (en) 1971-03-30 1974-06-28 Snam Progetti
US3724226A (en) 1971-04-20 1973-04-03 Gulf Research Development Co Lng expander cycle process employing integrated cryogenic purification
US3877240A (en) * 1973-04-27 1975-04-15 Lummus Co Process and apparatus for the storage and transportation of liquefied gases
US3850001A (en) 1973-06-15 1974-11-26 Chicago Bridge & Iron Co Lng ship tank inert gas generation system
DE2354726A1 (en) 1973-11-02 1975-05-07 Messer Griesheim Gmbh Liquefaction and conditioning of methane liquid nitrogen - for transport or storage in small amounts
JPS5357575U (en) 1976-10-18 1978-05-17
GB1596330A (en) 1978-05-26 1981-08-26 British Petroleum Co Gas liquefaction
JPS5755848Y2 (en) 1978-06-30 1982-12-02
US4281518A (en) 1979-01-23 1981-08-04 Messerschmitt-Bolkow-Blohm Gmbh Method and apparatus for separating particular components of a gas mixture
US4609388A (en) 1979-04-18 1986-09-02 Cng Research Company Gas separation process
JPH0143098Y2 (en) 1980-06-11 1989-12-14
DE3149847A1 (en) 1981-12-16 1983-07-21 Linde Ag, 6200 Wiesbaden Process for removing hydrocarbons and other impurities from a gas
US4415345A (en) 1982-03-26 1983-11-15 Union Carbide Corporation Process to separate nitrogen from natural gas
FR2535113B1 (en) 1982-10-22 1986-05-16 Thomson Csf PROCESS FOR MANUFACTURING A PIEZO- OR PYROELECTRIC POLYMER MATERIAL COMPRISING A CROSSLINKING STAGE
JPS59216785A (en) 1983-05-26 1984-12-06 Mitsubishi Heavy Ind Ltd Transportation system for lng
US4533372A (en) 1983-12-23 1985-08-06 Exxon Production Research Co. Method and apparatus for separating carbon dioxide and other acid gases from methane by the use of distillation and a controlled freezing zone
FR2561751B1 (en) 1984-03-23 1988-11-10 Air Liquide TANK PURGE AND INERTAGE PROCESS AND INSTALLATION
GB8505930D0 (en) 1985-03-07 1985-04-11 Ncl Consulting Engineers Gas handling
DE3622145A1 (en) 1986-07-02 1988-01-07 Messer Griesheim Gmbh Device for removing condensable components from gases
US4669277A (en) 1986-08-19 1987-06-02 Sunwell Engineering Company Ltd. Corrugated plate heat exchanger
US4769054A (en) 1987-10-21 1988-09-06 Union Carbide Corporation Abatement of vapors from gas streams by solidification
US4923493A (en) 1988-08-19 1990-05-08 Exxon Production Research Company Method and apparatus for cryogenic separation of carbon dioxide and other acid gases from methane
EP0394187B1 (en) 1989-04-17 1992-07-15 GebràœDer Sulzer Aktiengesellschaft Method for the recovery of nlg
JP2530859Y2 (en) 1989-04-21 1997-04-02 セイコーエプソン株式会社 Data imprinting device for camera
US5062270A (en) 1990-08-31 1991-11-05 Exxon Production Research Company Method and apparatus to start-up controlled freezing zone process and purify the product stream
US5120338A (en) 1991-03-14 1992-06-09 Exxon Production Research Company Method for separating a multi-component feed stream using distillation and controlled freezing zone
US5141543A (en) 1991-04-26 1992-08-25 Air Products And Chemicals, Inc. Use of liquefied natural gas (LNG) coupled with a cold expander to produce liquid nitrogen
US5139547A (en) 1991-04-26 1992-08-18 Air Products And Chemicals, Inc. Production of liquid nitrogen using liquefied natural gas as sole refrigerant
US5137558A (en) 1991-04-26 1992-08-11 Air Products And Chemicals, Inc. Liquefied natural gas refrigeration transfer to a cryogenics air separation unit using high presure nitrogen stream
NO179986C (en) 1994-12-08 1997-01-22 Norske Stats Oljeselskap Process and system for producing liquefied natural gas at sea
US5638698A (en) 1996-08-22 1997-06-17 Praxair Technology, Inc. Cryogenic system for producing nitrogen
US5865605A (en) * 1997-03-20 1999-02-02 Chicago Bridge & Iron Company Method and apparatus for removing a high pressure in-tank pump using a low pressure tube
DZ2533A1 (en) 1997-06-20 2003-03-08 Exxon Production Research Co Advanced component refrigeration process for liquefying natural gas.
CA2294742C (en) 1997-07-01 2005-04-05 Exxon Production Research Company Process for separating a multi-component gas stream containing at least one freezable component
GB2333148A (en) 1998-01-08 1999-07-14 Winter Christopher Leslie Liquifaction of gases
FR2756368B1 (en) 1998-01-13 1999-06-18 Air Liquide METHOD AND INSTALLATION FOR SUPPLYING AN AIR SEPARATION APPARATUS
US6082133A (en) 1999-02-05 2000-07-04 Cryo Fuel Systems, Inc Apparatus and method for purifying natural gas via cryogenic separation
DE19906602A1 (en) 1999-02-17 2000-08-24 Linde Ag Production of pure methane comprises rectifying liquefied methane from a natural gas storage tank
US6237347B1 (en) 1999-03-31 2001-05-29 Exxonmobil Upstream Research Company Method for loading pressurized liquefied natural gas into containers
CN1119195C (en) 1999-07-12 2003-08-27 吕应中 Gas dehydration method and device
US6298688B1 (en) 1999-10-12 2001-10-09 Air Products And Chemicals, Inc. Process for nitrogen liquefaction
US6308531B1 (en) 1999-10-12 2001-10-30 Air Products And Chemicals, Inc. Hybrid cycle for the production of liquefied natural gas
GB0006265D0 (en) 2000-03-15 2000-05-03 Statoil Natural gas liquefaction process
US6295838B1 (en) 2000-08-16 2001-10-02 Praxair Technology, Inc. Cryogenic air separation and gas turbine integration using heated nitrogen
US6412302B1 (en) 2001-03-06 2002-07-02 Abb Lummus Global, Inc. - Randall Division LNG production using dual independent expander refrigeration cycles
US20060000615A1 (en) 2001-03-27 2006-01-05 Choi Michael S Infrastructure-independent deepwater oil field development concept
US7219512B1 (en) 2001-05-04 2007-05-22 Battelle Energy Alliance, Llc Apparatus for the liquefaction of natural gas and methods relating to same
NZ534723A (en) 2002-01-18 2004-10-29 Univ Curtin Tech Process and device for production of LNG by removal of freezable solids
US6889522B2 (en) 2002-06-06 2005-05-10 Abb Lummus Global, Randall Gas Technologies LNG floating production, storage, and offloading scheme
US7143606B2 (en) 2002-11-01 2006-12-05 L'air Liquide-Societe Anonyme A'directoire Et Conseil De Surveillance Pour L'etide Et L'exploitation Des Procedes Georges Claude Combined air separation natural gas liquefaction plant
US6662589B1 (en) 2003-04-16 2003-12-16 Air Products And Chemicals, Inc. Integrated high pressure NGL recovery in the production of liquefied natural gas
US7591487B2 (en) 2003-11-07 2009-09-22 Complete Cryogenic Services, Inc. Apparatus and method for draining reservoirs
US20050123425A1 (en) * 2003-11-07 2005-06-09 Smith Henry A.Iii Apparatus and method for draining reservoirs
US7278281B2 (en) 2003-11-13 2007-10-09 Foster Wheeler Usa Corporation Method and apparatus for reducing C2 and C3 at LNG receiving terminals
WO2005082493A1 (en) 2004-03-02 2005-09-09 The Chugoku Electric Power Co., Inc. Method and system for treating exhaust gas, and method and apparatus for separating carbon dioxide
CA2471969A1 (en) 2004-06-23 2005-12-23 Lionel Gerber Heat exchanger for use in an ice machine
EP1715267A1 (en) 2005-04-22 2006-10-25 Air Products And Chemicals, Inc. Dual stage nitrogen rejection from liquefied natural gas
FR2885679A1 (en) 2005-05-10 2006-11-17 Air Liquide METHOD AND INSTALLATION FOR SEPARATING LIQUEFIED NATURAL GAS
AU2006280426B2 (en) 2005-08-09 2010-09-02 Exxonmobil Upstream Research Company Natural gas liquefaction process for LNG
FR2894838B1 (en) 2005-12-21 2008-03-14 Gaz De France Sa METHOD AND SYSTEM FOR CAPTURING CARBON DIOXIDE IN FUMEES
US7712331B2 (en) 2006-06-30 2010-05-11 Air Products And Chemicals, Inc. System to increase capacity of LNG-based liquefier in air separation process
GB0614250D0 (en) 2006-07-18 2006-08-30 Ntnu Technology Transfer As Apparatus and Methods for Natural Gas Transportation and Processing
BRPI0719868A2 (en) 2006-10-13 2014-06-10 Exxonmobil Upstream Res Co Methods for lowering the temperature of a subsurface formation, and for forming a frozen wall into a subsurface formation
US8079321B2 (en) 2006-12-15 2011-12-20 Exxonmobil Upstream Research Company Long tank FSRU/FLSV/LNGC
EP1972875A1 (en) 2007-03-23 2008-09-24 L'AIR LIQUIDE, S.A. pour l'étude et l'exploitation des procédés Georges Claude Process and apparatus for the separation of air by cryogenic distillation
CN101668677B (en) 2007-04-26 2013-11-06 埃克森美孚上游研究公司 Independent corrugated LNG tank
BRPI0808909A2 (en) 2007-05-03 2014-08-19 Exxonmobil Upstream Res Co PROCESS FOR LIQUIDATING A METAN RICH GAS CURRENT.
BRPI0813965A2 (en) 2007-07-12 2015-01-06 Shell Int Research METHOD AND APPARATUS FOR LIQUIFYING A GAS HYDROCARBON CURRENT.
US8601833B2 (en) 2007-10-19 2013-12-10 Air Products And Chemicals, Inc. System to cold compress an air stream using natural gas refrigeration
EP2225516A2 (en) 2007-12-21 2010-09-08 Shell Internationale Research Maatschappij B.V. Method of producing a gasified hydrocarbon stream; method of liquefying a gaseous hydrocarbon stream; and a cyclic process wherein cooling and re-warming a nitrogen-based stream, and wherein liquefying and regasifying a hydrocarbon stream
ATE546349T1 (en) 2008-08-21 2012-03-15 Daewoo Shipbuilding & Marine LIQUID GAS STORAGE TANK AND VESSEL CONTAINING SUCH TANK
DE102008060699A1 (en) 2008-12-08 2010-06-10 Behr Gmbh & Co. Kg Evaporator for a refrigeration circuit
DE102009008229A1 (en) 2009-02-10 2010-08-12 Linde Ag Process for separating nitrogen
JP5357575B2 (en) * 2009-02-26 2013-12-04 三菱重工業株式会社 Ship
KR20100112708A (en) 2009-04-10 2010-10-20 대우조선해양 주식회사 Replacement method of a liquefied gas storage tank using nitrogen
GB2470062A (en) 2009-05-08 2010-11-10 Corac Group Plc Production and Distribution of Natural Gas
US10132561B2 (en) 2009-08-13 2018-11-20 Air Products And Chemicals, Inc. Refrigerant composition control
FR2949553B1 (en) 2009-09-02 2013-01-11 Air Liquide PROCESS FOR PRODUCING AT LEAST ONE POOR CO2 GAS AND ONE OR MORE CO2-RICH FLUIDS
US9016088B2 (en) 2009-10-29 2015-04-28 Butts Propertties, Ltd. System and method for producing LNG from contaminated gas streams
GB2462555B (en) 2009-11-30 2011-04-13 Costain Oil Gas & Process Ltd Process and apparatus for separation of Nitrogen from LNG
US20110126451A1 (en) 2009-11-30 2011-06-02 Chevron U.S.A., Inc. Integrated process for converting natural gas from an offshore field site to liquefied natural gas and liquid fuel
KR101145303B1 (en) 2010-01-04 2012-05-14 한국과학기술원 Natural gas liquefaction method and equipment for LNG FPSO
SG10201500515QA (en) 2010-01-22 2015-04-29 Exxonmobil Upstream Res Co Removal of acid gases from a gas stream, with co2 capture and sequestration
JP2013518716A (en) 2010-02-03 2013-05-23 エクソンモービル アップストリーム リサーチ カンパニー System and method for using cryogenic liquids to remove solidifying gas components from a process gas stream
EP3254948B1 (en) 2010-02-22 2019-03-27 Shell International Research Maatschappij B.V. Hydrocarbon processing vessel and method
US8464289B2 (en) 2010-03-06 2013-06-11 Yang Pan Delivering personalized media items to users of interactive television and personal mobile devices by using scrolling tickers
JP5518531B2 (en) 2010-03-11 2014-06-11 中国電力株式会社 Carbon dioxide recovery device
US20110259044A1 (en) 2010-04-22 2011-10-27 Baudat Ned P Method and apparatus for producing liquefied natural gas
WO2011140117A2 (en) 2010-05-03 2011-11-10 Battelle Memorial Institute Carbon dioxide capture from power or process plant gases
EP2426452A1 (en) 2010-09-06 2012-03-07 Shell Internationale Research Maatschappij B.V. Method and apparatus for cooling a gaseous hydrocarbon stream
DE102010044869A1 (en) 2010-09-09 2012-03-15 Linde Aktiengesellschaft Liquefied Natural gas
JP5660845B2 (en) 2010-10-13 2015-01-28 三菱重工業株式会社 Liquefaction method, liquefaction apparatus, and floating liquefied gas production facility equipped with the same
JP5611377B2 (en) * 2011-02-07 2014-10-22 三菱重工業株式会社 Liquid suction device
EP2866921A2 (en) 2011-05-26 2015-05-06 Sustainable Energy Solutions, LLC Systems and methods for separating condensable vapors from light gases or liquids by recuperative cryogenic processes
GB2486036B (en) 2011-06-15 2012-11-07 Anthony Dwight Maunder Process for liquefaction of natural gas
CA2841624C (en) 2011-08-10 2019-09-03 Conocophillips Company Liquefied natural gas plant with ethylene independent heavies recovery system
EP2620732A1 (en) 2012-01-26 2013-07-31 Linde Aktiengesellschaft Method and device for air separation and steam generation in a combined system
US9439077B2 (en) 2012-04-10 2016-09-06 Qualcomm Incorporated Method for malicious activity detection in a mobile station
CN102620523B (en) 2012-04-16 2014-10-15 上海交通大学 Mixed refrigerant circulation natural gas zone pressure liquefaction technology with sublimation removal of CO2
CN102628635B (en) 2012-04-16 2014-10-15 上海交通大学 Gas expansion natural gas pressurized liquefying technique with function of condensing and removing carbon dioxide (CO2)
WO2014011903A1 (en) 2012-07-11 2014-01-16 Fluor Technologies Corporation Configurations and methods of co2 capture from flue gas by cryogenic desublimation
ITMI20121625A1 (en) 2012-09-28 2014-03-29 Eni Spa REFRIGERANT CIRCUIT FOR THE LIQUEFATION OF NATURAL GAS
US20140130542A1 (en) 2012-11-13 2014-05-15 William George Brown Method And Apparatus for High Purity Liquefied Natural Gas
JP6338589B2 (en) 2012-11-16 2018-06-06 エクソンモービル アップストリーム リサーチ カンパニー Natural gas liquefaction
DE102013007208A1 (en) 2013-04-25 2014-10-30 Linde Aktiengesellschaft Process for recovering a methane-rich liquid fraction
JP5705271B2 (en) 2013-06-17 2015-04-22 大陽日酸株式会社 CO2 transportation method, disposal method and transportation method
JP6036605B2 (en) * 2013-08-23 2016-11-30 株式会社Ihi Above-ground cryogenic tank
WO2015110443A2 (en) 2014-01-22 2015-07-30 Global Lng Services Ltd. Coastal liquefaction
KR101591781B1 (en) * 2014-08-06 2016-02-04 한국가스공사 Pump tower of liquified gas storage tank
US20160109177A1 (en) 2014-10-16 2016-04-21 General Electric Company System and method for natural gas liquefaction
TWI641789B (en) 2015-07-10 2018-11-21 艾克頌美孚上游研究公司 System and methods for the production of liquefied nitrogen gas using liquefied natural gas
TWI606221B (en) 2015-07-15 2017-11-21 艾克頌美孚上游研究公司 Liquefied natural gas production system and method with greenhouse gas removal
TWI608206B (en) 2015-07-15 2017-12-11 艾克頌美孚上游研究公司 Increasing efficiency in an lng production system by pre-cooling a natural gas feed stream
GB2540425B (en) 2015-07-17 2017-07-05 Sage & Time Llp A gas conditioning system
FR3041603B1 (en) * 2015-09-29 2018-07-13 Gaztransport Et Technigaz SEALED AND INSULATED TANK DISPOSED IN A SHIP
ITUB20155049A1 (en) 2015-10-20 2017-04-20 Nuovo Pignone Tecnologie Srl INTEGRATED TRAIN OF POWER GENERATION AND COMPRESSION, AND METHOD
CN108369061B (en) 2015-12-14 2020-05-22 埃克森美孚上游研究公司 Method and system for separating nitrogen from liquefied natural gas using liquefied nitrogen
CN108291767B (en) 2015-12-14 2021-02-19 埃克森美孚上游研究公司 Method for liquefaction of natural gas on LNG carriers storing liquid nitrogen
AU2016372710B2 (en) 2015-12-14 2019-09-12 Exxonmobil Upstream Research Company Expander-based LNG production processes enhanced with liquid nitrogen
JP6800977B2 (en) 2015-12-14 2020-12-16 エクソンモービル アップストリーム リサーチ カンパニー Precooling of natural gas by high pressure compression and expansion
NL2017393B1 (en) 2016-08-30 2018-03-08 Koole Eng B V Method for assembling a transport tank in a vessel and a corresponding vessel
US20180231305A1 (en) 2017-02-13 2018-08-16 Fritz Pierre, JR. Increasing Efficiency in an LNG Production System by Pre-Cooling a Natural Gas Feed Stream
WO2018147973A1 (en) 2017-02-13 2018-08-16 Exxonmobil Upstream Research Company Pre-cooling of natural gas by high pressure compression and expansion
EP3586057B1 (en) 2017-02-24 2022-09-14 ExxonMobil Upstream Research Company Method of purging a dual purpose lng/lin storage tank
US11402151B2 (en) 2017-02-24 2022-08-02 Praxair Technology, Inc. Liquid natural gas liquefier utilizing mechanical and liquid nitrogen refrigeration
CA3056863C (en) 2017-03-30 2023-09-19 Exxonmobil Upstream Research Company Ship/floating storage unit with dual cryogenic cargo tank for lng and liquid nitrogen
FR3065941A1 (en) * 2017-05-05 2018-11-09 Gaztransport Et Technigaz METHOD FOR HANDLING LIQUEFIED GAS CARGO AND STORAGE PLANT

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