JP2015506454A5 - - Google Patents

Download PDF

Info

Publication number
JP2015506454A5
JP2015506454A5 JP2014548840A JP2014548840A JP2015506454A5 JP 2015506454 A5 JP2015506454 A5 JP 2015506454A5 JP 2014548840 A JP2014548840 A JP 2014548840A JP 2014548840 A JP2014548840 A JP 2014548840A JP 2015506454 A5 JP2015506454 A5 JP 2015506454A5
Authority
JP
Japan
Prior art keywords
stream
heat exchanger
external heat
refrigerant stream
separation vessel
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.)
Ceased
Application number
JP2014548840A
Other languages
Japanese (ja)
Other versions
JP2015506454A (en
Filing date
Publication date
Application filed filed Critical
Priority claimed from PCT/US2012/070647 external-priority patent/WO2013096464A1/en
Publication of JP2015506454A publication Critical patent/JP2015506454A/en
Publication of JP2015506454A5 publication Critical patent/JP2015506454A5/ja
Ceased legal-status Critical Current

Links

Claims (15)

動き環境下でプロセスガスを冷却または液化するためのシステムであって、
a.分離容器、ここで該分離容器は、冷媒流を分離しそれにより気体冷媒流と液体冷媒流を生成するものであり、
b.前記液体冷媒流を前記分離容器から外部の熱交換器コアに送達するための気液冷媒パイプ、
c.少なくとも1つの外部熱交換器コア、ここで前記液体冷媒流およびより暖かいプロセス流が前記外部熱交換器コアにおいて間接的な熱交換を受け、それにより、冷却されたプロセス流および気化した冷媒流を生成し、
d.前記部分気化冷媒を前記外部熱交換器コアから前記分離容器に送達するための部分気化冷媒パイプ、
を含む該システム。
A system for cooling or liquefying process gas in a moving environment,
a. A separation vessel, wherein the separation vessel separates the refrigerant stream and thereby generates a gaseous refrigerant stream and a liquid refrigerant stream;
b. A gas-liquid refrigerant pipe for delivering the liquid refrigerant stream from the separation vessel to an external heat exchanger core;
c. At least one external heat exchanger core, wherein the liquid refrigerant stream and warmer process stream undergo indirect heat exchange in the external heat exchanger core, thereby reducing the cooled process stream and the vaporized refrigerant stream. Generate
d. A partially vaporized refrigerant pipe for delivering the partially vaporized refrigerant from the external heat exchanger core to the separation vessel;
Including the system.
前記冷媒流が、高圧液体冷媒として前記分離容器に送達される請求項に記載のシステム。 The system of claim 1 , wherein the refrigerant stream is delivered to the separation vessel as a high pressure liquid refrigerant. 前記分離容器が、複数の動き抑制バッフルを含む請求項に記載のシステム。 The system of claim 1 , wherein the separation vessel includes a plurality of motion restraining baffles. 前記複数の動き抑制バッフルが、水平に配置されている、垂直に配置されているまたは水平および垂直に配置されている請求項に記載のシステム。 The system of claim 3 , wherein the plurality of motion suppression baffles are arranged horizontally, arranged vertically, or arranged horizontally and vertically . 前記部分気化冷媒パイプが、最小の圧力降下を提供する請求項に記載のシステム。 The system of claim 1 , wherein the partially vaporized refrigerant pipe provides a minimum pressure drop. 前記部分気化冷媒パイプが、熱サイフォン効果が維持されることを確保する請求項に記載のシステム。 The system of claim 1 , wherein the partially vaporized refrigerant pipe ensures that the thermosyphon effect is maintained. 前記冷却されたプロセス流が、前記外部熱交換器コアの外部の場所に送達される請求項に記載のシステム。 The system of claim 1 , wherein the cooled process stream is delivered to a location external to the external heat exchanger core. 前記外部熱交換器コアが、ケトルの外部にある請求項1に記載のプロセス。  The process of claim 1, wherein the external heat exchanger core is external to a kettle. 動き環境下で天然ガスを液化するための方法であって、
a.分離容器に冷(refrigeration)を導入し、それにより気体冷媒流と液体冷媒流を生成すること、
b.前記液体冷媒流を外部熱交換器コアの底近傍に導入すること、
c.より暖かいプロセス流を前記液体冷媒流の上部の位置で前記外部熱交換器コアに導入すること、
d.前記より暖かいプロセス流を前記外部熱交換器コアにおいて前記液体冷媒流との間接的熱交換により冷却し、それにより冷却されたプロセス流と部分気化冷媒流とを生成すること、
e.前記冷却されたプロセス流と前記部分気化冷媒流とを前記外部熱交換器から取り出すこと、
を含む該方法。
A method for liquefying natural gas in a moving environment,
a. Introducing refrigeration into the separation vessel, thereby producing a gas refrigerant stream and a liquid refrigerant stream;
b. Introducing the liquid refrigerant stream near the bottom of the external heat exchanger core;
c. Introducing a warmer process stream into the external heat exchanger core at a position above the liquid refrigerant stream;
d. Cooling the warmer process stream by indirect heat exchange with the liquid refrigerant stream in the external heat exchanger core, thereby producing a cooled process stream and a partially vaporized refrigerant stream;
e. Removing the cooled process stream and the partially vaporized refrigerant stream from the external heat exchanger;
The method comprising.
(f)前記部分気化冷媒流を、前記分離容器に送達することをさらに含む請求項に記載の方法。 10. The method of claim 9 , further comprising (f) delivering the partially vaporized refrigerant stream to the separation vessel. (g)前記冷却されたプロセス流を、前記外部熱交換器コアの外部の場所に送達することをさらに含む請求項に記載の方法。 The method of claim 9 , further comprising: (g) delivering the cooled process stream to a location external to the external heat exchanger core. 前記分離容器が、複数の動き抑制バッフルを含む請求項に記載のシステム。 The system of claim 9 , wherein the separation vessel includes a plurality of motion restraining baffles. 前記複数の動き抑制バッフルが、垂直に配置されている、水平に配置されているまたは水平および垂直に配置されている請求項12に記載のシステム。 The system of claim 12 , wherein the plurality of motion suppression baffles are arranged vertically, arranged horizontally, or arranged horizontally and vertically . 動き環境下でプロセスガスを冷却または液化するためのシステムであって、
a.分離容器、ここで該分離容器は複数の動き抑制バッフルを含み、該分離容器は、高圧冷媒流を分離しそれにより気体冷媒流と液体冷媒流を生成するものであり、
b.前記液体冷媒流を前記分離容器から外部の熱交換器コアに送達するための気液冷媒パイプ、
c.少なくとも1つの外部熱交換器コア、ここで該外部熱交換器コアは、ケトルの外部にあり、前記液体冷媒流およびより暖かいプロセス流が前記外部熱交換器コアにおいて間接的な熱交換を受け、それにより、冷却されたプロセス流および気化した冷媒流を生成し、前記冷却されたプロセス流は、前記外部熱交換器コアの外部の位置に送達されるものであり、
d.前記部分気化冷媒を前記外部熱交換器コアから前記分離容器に送達するための部分気化冷媒パイプ、ここで前記部分気化冷媒パイプは最小の圧力降下を提供し、前記部分気化冷媒パイプは、熱サイフォン効果が維持されるのを保証するものである、
を含む該システム。
A system for cooling or liquefying process gas in a moving environment,
a. A separation vessel, wherein the separation vessel includes a plurality of motion-suppressing baffles, the separation vessel separating a high-pressure refrigerant stream and thereby generating a gaseous refrigerant stream and a liquid refrigerant stream;
b. A gas-liquid refrigerant pipe for delivering the liquid refrigerant stream from the separation vessel to an external heat exchanger core;
c. At least one external heat exchanger core, wherein the external heat exchanger core is external to the kettle, and the liquid refrigerant stream and warmer process stream undergo indirect heat exchange in the external heat exchanger core; Thereby producing a cooled process stream and a vaporized refrigerant stream, wherein the cooled process stream is delivered to a location external to the external heat exchanger core;
d. A partially vaporized refrigerant pipe for delivering the partially vaporized refrigerant from the external heat exchanger core to the separation vessel, wherein the partially vaporized refrigerant pipe provides a minimum pressure drop, and the partially vaporized refrigerant pipe is a thermosyphon Guarantees that the effect is maintained,
Including the system.
動き環境下で天然ガスを液化するための方法であって、
a.冷(refrigeration)を分離容器に導入し、それにより気体冷媒流と液体冷媒流を生成すること、ここで、前記分離容器は、複数の動き抑制バッフルを含み、
b.前記液体冷媒流を外部熱交換器コアの底近傍に導入すること、
c.より暖かいプロセス流を前記液体冷媒流の上部の位置で前記外部熱交換器コアに導入すること、
d.前記より暖かいプロセス流を前記液体冷媒流との間接的熱交換により冷却し、それにより冷却されたプロセス流と部分気化冷媒流とを生成すること、
e.前記冷却されたプロセス流と部分気化冷媒流とを前記外部熱交換器から取り出すこと、
f.前記部分気化冷媒流を前記分離容器に送達すること、
g.前記冷却されたプロセス流を前記外部熱交換器の外部の位置に送達すること、
を含む該方法。
A method for liquefying natural gas in a moving environment,
a. Introducing refrigeration into the separation vessel, thereby producing a gaseous refrigerant stream and a liquid refrigerant stream, wherein the separation vessel comprises a plurality of motion-reducing baffles;
b. Introducing the liquid refrigerant stream near the bottom of the external heat exchanger core;
c. Introducing a warmer process stream into the external heat exchanger core at a position above the liquid refrigerant stream;
d. Cooling the warmer process stream by indirect heat exchange with the liquid refrigerant stream, thereby producing a cooled process stream and a partially vaporized refrigerant stream;
e. Removing the cooled process stream and the partially vaporized refrigerant stream from the external heat exchanger;
f. Delivering the partially vaporized refrigerant stream to the separation vessel;
g. Delivering the cooled process stream to a location external to the external heat exchanger;
The method comprising.
JP2014548840A 2011-12-20 2012-12-19 Natural gas liquefaction in a moving environment Ceased JP2015506454A (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
US201161578085P 2011-12-20 2011-12-20
US61/578,085 2011-12-20
PCT/US2012/070647 WO2013096464A1 (en) 2011-12-20 2012-12-19 Liquefying natural gas in a motion environment

Publications (2)

Publication Number Publication Date
JP2015506454A JP2015506454A (en) 2015-03-02
JP2015506454A5 true JP2015506454A5 (en) 2015-11-12

Family

ID=48653241

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2014548840A Ceased JP2015506454A (en) 2011-12-20 2012-12-19 Natural gas liquefaction in a moving environment

Country Status (8)

Country Link
US (1) US20130160487A1 (en)
EP (1) EP2795214A4 (en)
JP (1) JP2015506454A (en)
CN (1) CN104011487B (en)
AP (1) AP2014007703A0 (en)
AU (1) AU2012359032A1 (en)
RU (1) RU2620310C2 (en)
WO (1) WO2013096464A1 (en)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
AU2015225689B2 (en) * 2014-03-07 2019-01-03 Conocophillips Company Heat exchanger system with mono-cyclone inline separator
AU2015252986B2 (en) 2014-05-01 2019-07-11 Conocophillips Company Liquid drains in core-in-shell heat exchanger
CN106024074A (en) * 2016-05-11 2016-10-12 中广核研究院有限公司 Nuclear power plant voltage stabilizer for inhibiting liquid level sloshing
CN105957565B (en) * 2016-06-23 2018-05-29 中广核研究院有限公司 Constrain pond and the containment with the constrain pond
CN114777412B (en) * 2022-04-01 2023-03-24 中国科学院理化技术研究所 Hydrogen liquefying plant with thermal siphon type hydrogen subcooler

Family Cites Families (31)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US436003A (en) * 1890-09-09 Process of circulating liquefied refrigerating agents
NL300398A (en) * 1962-11-22
DE2438443C2 (en) * 1974-08-09 1984-01-26 Linde Ag, 6200 Wiesbaden Process for liquefying natural gas
JPS5733298A (en) * 1980-07-31 1982-02-23 Mitsubishi Heavy Ind Ltd Liquefaction/recovery device for evaporated gas in ship's tank
US4445916A (en) * 1982-08-30 1984-05-01 Newton Charles L Process for liquefying methane
FR2545589B1 (en) * 1983-05-06 1985-08-30 Technip Cie METHOD AND APPARATUS FOR COOLING AND LIQUEFACTING AT LEAST ONE GAS WITH LOW BOILING POINT, SUCH AS NATURAL GAS
JPH0133985Y2 (en) * 1984-09-25 1989-10-16
JPH06299174A (en) * 1992-07-24 1994-10-25 Chiyoda Corp Cooling system using propane coolant in natural gas liquefaction process
JPH06159928A (en) * 1992-11-20 1994-06-07 Chiyoda Corp Liquefying method for natural gas
JP3320934B2 (en) * 1994-12-09 2002-09-03 株式会社神戸製鋼所 Gas liquefaction method
EP0723125B1 (en) * 1994-12-09 2001-10-24 Kabushiki Kaisha Kobe Seiko Sho Gas liquefying method and plant
MY117899A (en) * 1995-06-23 2004-08-30 Shell Int Research Method of liquefying and treating a natural gas.
JPH11244671A (en) * 1998-02-27 1999-09-14 Mitsubishi Rayon Co Ltd Hollow-fiber membrane module for treating crude oil, treatment of crude oil using the module and crude oil treating device
TW421704B (en) * 1998-11-18 2001-02-11 Shell Internattonale Res Mij B Plant for liquefying natural gas
MY122625A (en) * 1999-12-17 2006-04-29 Exxonmobil Upstream Res Co Process for making pressurized liquefied natural gas from pressured natural gas using expansion cooling
US6220287B1 (en) * 2000-02-03 2001-04-24 The Boeing Company Baffle for suppressing slosh in a tank and a tank for incorporating same
WO2001088447A1 (en) * 2000-05-18 2001-11-22 Phillips Petroleum Company Enhanced ngl recovery utilizing refrigeration and reflux from lng plants
US6564580B2 (en) * 2001-06-29 2003-05-20 Exxonmobil Upstream Research Company Process for recovering ethane and heavier hydrocarbons from methane-rich pressurized liquid mixture
CN100504262C (en) * 2004-06-23 2009-06-24 埃克森美孚上游研究公司 Mixed refrigerant liquefaction process
US7469651B2 (en) * 2004-07-02 2008-12-30 Exxonmobil Upstream Research Company Lng sloshing impact reduction system
KR101259192B1 (en) * 2004-08-06 2013-04-29 비피 코포레이션 노쓰 아메리카 인코포레이티드 Natural gas liquefaction process
RU2459652C2 (en) * 2006-11-22 2012-08-27 Шелл Интернэшнл Рисерч Маатсхаппий Б.В. Method and device for making homogeneous vapor and liquid phases in two or more flows and method of cooling hydrocarbon flow
US20100293996A1 (en) * 2007-11-16 2010-11-25 Michiel Gijsbert Van Aken Method and apparatus for liquefying a hydrocarbon stream and floating vessel or offshore platform comprising the same
CN101883715B (en) * 2007-12-04 2013-04-17 三星重工业株式会社 Anti-sloshing structure for LNG cargo tank
US20090139263A1 (en) * 2007-12-04 2009-06-04 Air Products And Chemicals, Inc. Thermosyphon reboiler for the denitrogenation of liquid natural gas
US10780955B2 (en) * 2008-06-20 2020-09-22 Seaone Holdings, Llc Comprehensive system for the storage and transportation of natural gas in a light hydrocarbon liquid medium
RU2382301C1 (en) * 2008-10-20 2010-02-20 Открытое акционерное общество "Научно-исследовательский и проектный институт по переработке газа" ОАО "НИПИгазпереработка" Unit for low-temperature separation of hydrocarbon gas
FR2943683B1 (en) * 2009-03-25 2012-12-14 Technip France PROCESS FOR TREATING A NATURAL LOAD GAS TO OBTAIN TREATED NATURAL GAS AND C5 + HYDROCARBON CUTTING, AND ASSOCIATED PLANT
FR2944523B1 (en) * 2009-04-21 2011-08-26 Technip France PROCESS FOR PRODUCING METHANE-RICH CURRENT AND CUTTING RICH IN C2 + HYDROCARBONS FROM A NATURAL LOAD GAS CURRENT, AND ASSOCIATED PLANT
US20100281915A1 (en) * 2009-05-05 2010-11-11 Air Products And Chemicals, Inc. Pre-Cooled Liquefaction Process
US9829246B2 (en) * 2010-07-30 2017-11-28 Exxonmobil Upstream Research Company Cryogenic systems for removing acid gases from a hydrocarbon gas stream using co-current separation devices

Similar Documents

Publication Publication Date Title
JP2015506454A5 (en)
JP2016505793A5 (en)
JP2011094145A5 (en)
PH12017502172A1 (en) Boil-off gas re-liquefying system
MY174487A (en) Integrated pre-cooled mixed refrigerant system and method
RU2014140213A (en) ORDERED NOZZLE
JP2013510286A5 (en)
JP2010537151A5 (en)
EP2478312A4 (en) Auto-refrigerated gas separation system for carbon dioxide capture and compression
WO2014053297A3 (en) Process for the separation of air by cryogenic distillation
MX2013000563A (en) Energy efficient production of co2 using single stage expansion and pumps for elevated evaporation.
AU2015212280A8 (en) Liquefied gas producing facility and liquefied gas producing method
JP2013505423A5 (en)
RU2014129588A (en) NATURAL GAS LIQUIDATION IN A MOVING ENVIRONMENT
WO2015140197A3 (en) A method for liquefaction of a pre-processed natural gas
IN2014KN03003A (en)
RU2018101475A (en) METHOD OF MODERNIZATION OF AMMONIA SYNTHESIS INSTALLATION
WO2015060930A3 (en) Air separation method and apparatus
WO2015095040A3 (en) An apparatus for producing liquid nitrogen
GB201305641D0 (en) Method and apparatus for cooling in liquefaction process
WO2015104510A3 (en) Method and device for the liquefaction of a gaseous co2 stream
WO2012140369A3 (en) Method and apparatus for liquefying a gas or cooling a feed gas at supercritical pressure
WO2010069910A3 (en) Method for cooling a hydrocarbon stream and a floating vessel therefor
RU2009117466A (en) METHOD AND DEVICE FOR COOLING A HYDROCARBON FLOW
EP2503265A3 (en) Method for operating a cooling system