EP2643629A2 - Installations pour stockage flottant de gaz naturel liquéfié au large comprenant une unité de regazéification de jetée - Google Patents

Installations pour stockage flottant de gaz naturel liquéfié au large comprenant une unité de regazéification de jetée

Info

Publication number
EP2643629A2
EP2643629A2 EP11852293.7A EP11852293A EP2643629A2 EP 2643629 A2 EP2643629 A2 EP 2643629A2 EP 11852293 A EP11852293 A EP 11852293A EP 2643629 A2 EP2643629 A2 EP 2643629A2
Authority
EP
European Patent Office
Prior art keywords
unit
lng
jetty
regasification
facilities
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
EP11852293.7A
Other languages
German (de)
English (en)
Other versions
EP2643629B1 (fr
EP2643629A4 (fr
Inventor
Ki Ho Moon
Kwang Ho Wi
Jae Young Ahn
Ho Joon Shin
Jae In Lee
In Soo Kim
Young Jae Yoo
Hyuk Jin Kwon
Doo Hyeong Lee
Chang Soo Kim
Sung Uk Lee
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.)
Samsung C&T Corp
Original Assignee
Samsung C&T Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Samsung C&T Corp filed Critical Samsung C&T Corp
Priority to PL11852293T priority Critical patent/PL2643629T3/pl
Publication of EP2643629A2 publication Critical patent/EP2643629A2/fr
Publication of EP2643629A4 publication Critical patent/EP2643629A4/fr
Application granted granted Critical
Publication of EP2643629B1 publication Critical patent/EP2643629B1/fr
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

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
    • F17C5/00—Methods or apparatus for filling containers with liquefied, solidified, or compressed gases under pressures
    • F17C5/06—Methods or apparatus for filling containers with liquefied, solidified, or compressed gases under pressures for filling with compressed gases
    • 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
    • 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
    • F17C2223/0161—Liquefied gas, e.g. LPG, GPL cryogenic, e.g. LNG, GNL, 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
    • F17C2223/03—Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel characterised by the pressure level
    • F17C2223/033—Small pressure, e.g. for liquefied gas
    • 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
    • F17C2225/00—Handled fluid after transfer, i.e. state of fluid after transfer from the vessel
    • F17C2225/03—Handled fluid after transfer, i.e. state of fluid after transfer from the vessel characterised by the pressure level
    • F17C2225/035—High pressure, i.e. between 10 and 80 bars
    • 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
    • F17C2227/03—Heat exchange with the fluid
    • F17C2227/0302—Heat exchange with the fluid by heating
    • F17C2227/0309—Heat exchange with the fluid by heating using another fluid
    • F17C2227/0316—Water heating
    • F17C2227/0318—Water heating using seawater
    • 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
    • F17C2227/03—Heat exchange with the fluid
    • F17C2227/0367—Localisation of heat exchange
    • F17C2227/0388—Localisation of heat exchange separate
    • F17C2227/0393—Localisation of heat exchange separate using a vaporiser
    • 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
    • F17C2265/05—Regasification
    • 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
    • F17C2270/0118—Offshore
    • F17C2270/0121—Platforms
    • 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
    • F17C2270/0118—Offshore
    • F17C2270/0123—Terminals

Definitions

  • the present invention relates to facilities for offshore liquefied natural gas (LNG) floating storage with jetty regasification unit, and more particularly, to offshore facilities that have floating storage and regasification unit installed on jetty unit.
  • LNG offshore liquefied natural gas
  • this concept have been found to reduce installation, operating costs and construction time, and moreover increases stability of regasification performance of LNG.
  • the regasification facilities are used for regasification of LNG, i.e., to turn LNG back into natural gas.
  • LNG storage and regasification units are installed onshore
  • offshore facilities include a floating LNG storage unit, usually an LNG carrier or a gravity based structure (GBS), and a regasification unit installed on the floating structure, a shuttle regasification vessel (SRV) or a LNG regasification vessel (RV).
  • GGS gravity based structure
  • SRV shuttle regasification vessel
  • RV LNG regasification vessel
  • the SRV or the LNG RV is special purposed vessels that can navigate with regasification facilities.
  • the procedure starts by loading LNG from where it is produced and transports to an unloading location where then it is moored by submerged turret loading (STL) in offshore.
  • STL submerged turret loading
  • FSRU or SRV is moored to a jetty structure to withstand offshore weather and conditions.
  • LNG is supplied to FSRU from LNC carrier (LNGC) through a loading arm installed on a jetty where both FSRU and LNGC are moored side by side.
  • LNC carrier LNC carrier
  • high pressured natural gas (usually between 40 and 90 atm) is supplied to onshore through high pressure gas arm.
  • the loading arm and the high pressure gas arm have a large number of components which can absorb impact from the motions.
  • the present invention facilities for offshore LNG floating storage with jetty regasification unit, is designed for reduction of a construction time and cost, and enhances the stability for operation when compared to a newly constructed or converted FSRU and LNG RV.
  • a facilities for offshore liquefied natural gas (LNG) floating storage with jetty regasification unit comprising: a jetty unit of a steel structure or an iron concrete structure installed in offshore; a storage unit moored at the jetty unit providing a space for storing LNG; a regasification unit as a module which regasifies the LNG supplied from the storage unit, installed on a top portion of the jetty unit and is separable from the jetty unit; a utility unit comprising a power source and a sea water pump to supply power and sea water to the regasification unit; and a piping unit comprising unloading pipe for connecting the regasification unit and the storage unit and supplying pipe for carrying natural gas gasified by the regasification unit.
  • LNG offshore liquefied natural gas
  • the utility unit may be implemented as a module to be separable from the jetty unit.
  • the regasification unit may be used an open rack vaporizer (ORV) using sea water for heat exchanger.
  • ORV open rack vaporizer
  • the sea water pump of the utility unit and a ballast water pump disposed in the storage unit may be simultaneously used to supply sea water to the regasification unit.
  • a power facility, a steam generator, and a ballast water pump disposed in the storage unit may be used to supply power, steam, and sea water, respectively, which are necessary for the regasification unit.
  • the storage unit may be fixed to the jetty unit, loads LNG from a movable LNG carrier or a floating storage unit (FSU), and carries the LNG to the regasification unit.
  • FSU floating storage unit
  • the storage unit may be separable from the jetty unit and movable to load LNG.
  • the storage unit may be the LNG carrier or an FSU.
  • the present invention of offshore LNG floating storage with jetty regasification unit can provide a solution that can dramatically reduce the possibilities of high pressured natural gas leak into the atmosphere when compared to regasification on a floating structure.
  • FIG. 1 is a schematic diagram of a liquefied natural gas (LNG) regasification unit according to an embodiment of the present invention.
  • LNG liquefied natural gas
  • FIG. 1 is a schematic diagram of a liquefied natural gas (LNG) regasification unit according to an embodiment of the present invention.
  • LNG liquefied natural gas
  • the LNG regasification unit is used to regasify LNG in offshore and supply the regasified LNG, to gas users onshore.
  • this invention includes the jetty unit 10, a storage unit 20, a regasification unit 30, a piping unit 40, and a utility unit 50.
  • the jetty unit 10 is a fixed structure installed in sea bed with its legs, made of steel or iron concrete.
  • the term ‘jetty’ has various meanings, for example, a structure like a breakwater which distinguishes an inland and the sea, or a facility which is for anchoring vessels.
  • a site with certain depth of water, higher than a predetermined depth is required.
  • the jetty can be used for berthing in the way of stretching steeled structure from onshore to offshore or constructing a container terminal after dredging.
  • the jetty unit 10 is a semi-permanent structure that is installed to maintain a constant altitude above the sea level to withstand the changes of the wave by tidal current.
  • the shape of jetty unit 10 is not limited, it can be changed according to the locations and conditions thereof as long as the storage unit 20 can be anchored at.
  • a structure for anchoring the storage unit 20, such as a mooring dolphin or a fender, may be installed around the jetty unit 10, and is not shown in FIG. 1 for illustrative convenience (all the constituents are quite simply illustrated in FIG. 1).
  • the storage unit 20 provides a space for storing LNG once moored at the jetty unit 10.
  • the storage unit 20 can be converted from a second-handed LNG carrier or an existing LNG floating storage unit (FSU). Meanwhile, the storage unit 20 may be fixedly moored at the jetty unit 10 and separated from the jetty unit 10 on occasional demands.
  • Conventional operation involves supplying the LNG to the regasification unit 30 after receiving LNG from another LNG carrier.
  • the storage unit 20 may move to a location where LNG is produced or another FSU by itself, then receives LNG therefrom and supply the LNG to the regasification unit 30 again after being moored at the jetty unit 10.
  • another LNG carrier may supply LNG to the regasification unit 30, at the opposite side of the jetty unit 10.
  • Fixed or movable type of the storage unit 20 is determined according to circumstances or economical efficiency. For example, when a converted LNG carrier is used for the storage unit 20, storage type can be decided depending on the situation, as its mobility is already obtained.
  • the conversion process may require the vessel to operation both LNG loading pipe 21 and LNG unloading pipe 42 simultaneously, as general LNG carrier is designed not to proceed loading and unloading at the same time. Furthermore, if the storage unit 20 is expected to move, an appropriate facility for separating the unloading pipe 42 from the storage unit 20 is required as well.
  • the storage unit 20 includes a utility facility 22, such as a power facility, a steam generator, a ballast water pump P2, etc. which general LNG carriers and FSU are already equipped, thus no additional facility is needed when the second-handed LNG carrier or the FSU is converted.
  • a utility facility 22 such as a power facility, a steam generator, a ballast water pump P2, etc. which general LNG carriers and FSU are already equipped, thus no additional facility is needed when the second-handed LNG carrier or the FSU is converted.
  • the regasification unit 30 is a module for regasifying LNG which is supplied from the storage unit 20.
  • the regasification unit 30 is also separable from the jetty unit 10. Installment of the regasification unit 30 on the jetty unit 10, which is fixed on the sea bed, allows LNG to be regasified in offshore without the problems which commonly occurs in operation of conventional FSRU of LNG RV, a danger of leakage of natural gas due to an automatic piping separation in the operation or abrupt disconnection of a high pressure gas arm on the jetty unit 10 under the various offshore conditions. Since regasification work is performed on the hull 11 of the jetty unit 10, LNG can be transferred through the pipe between the storage unit 20 and the regasification unit 30. The stability of the hull 11 allows more safe transfer of LNG, regardless of the storage unit 20 movement due to the waves and tidal current.
  • a heat exchanger of the regasification unit 30 in the present invention is an open rack vaporizer (ORV) that utilizes sea water as a heat source. By contacting the heat exchanger, sea water absorbs the heat and vaporizes LNG into gas. ORV is strongly recommended due to its low investment and operating cost. However, if sea water is not uniformly coated on the vaporizer, the heat exchanger freezes and deteriorates its structure. That is why the ORV cannot be installed on FSRU of LNG RV. For the present invention, fixed structure of the jetty unit 10 guarantees safe operation of the ORV, which is a relatively inexpensive heat exchange system.
  • a sea water pump P1 in the utility unit 50 and the ballast water pump P2 of the utility facility 22 in the storage unit 20 are used to supply sea water to the ORV.
  • the sea water pump P1 and the ballast water pump P2 are designed to operate simultaneous as depicted in FIG1, it is not necessary to use both of them.
  • the sea water pump P1 acts as a main pump and the ballast water pump P2 as an auxiliary pump. Or, only the sea water pump P1 may be operated if the storage unit 20 is disconnected. How to supply the sea water to the ORV are subject to circumstances.
  • the piping unit 40 connecting the regasification unit 30 and the storage unit 20, includes unloading pipe 41 for supplying LNG from the storage unit 20 to the regasification unit 30 and supply pipe 42 for supplying gasified LNG from the regasification unit 30 to the end users in onshore. If required part of the piping unit 40 may be installed below a sea level.
  • the utility unit 50 (module) includes a power source, the sea water pump P1, and the steam generator for supplying power, sea water, and steam, respectively, to the regasification unit 30. Similar with the regasification unit 30, it is installed on the jetty unit 10, but also separable.
  • the utility unit 50 and the regasification unit 30 are connected by a power cable 51, sea water pipe 52, and steam pipe 53. They are respectively connected to the utility facilities in the storage unit 20 to be used simultaneously or complementarily in the present invention. Unlike shown in FIG.1, only the utility unit 50 may operate independently.
  • the piping unit 40, the power cable 51, the sea water pipe 52, and the steam pipe 53 are quite simply illustrated in FIG.1 for illustrative convenience, but the actual design is considerably complicated. Nevertheless, for the purpose of illustration, such simple diagram will be understood by those who have knowledge of this technology.
  • LNG stored in the storage unit 20 is supplied to the regasification unit 30 through the unloading pipe 41. Once regasified through the unit 30, regasified LNG is carried to the end users’ pipe line onshore through the supplying pipe 42.
  • the storage unit 20 can be fixed to the jetty unit 10 to load LNG from an LNG carrier (supplied through the loading pipe 21) or can be moved by itself to receive LNG from a neighboring FSU or a location where LNG is produced. If the storage unit 20 moves to different site, designated replacement should substitute for the previous storage unit 20, in order to supply LNG continuously.

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Filling Or Discharging Of Gas Storage Vessels (AREA)

Abstract

L'invention concerne des installations pour stockage flottant de gaz naturel liquéfié (GNL) au large comprenant une unité de regazéification de jetée, qui comportent : une unité de jetée composée d'une structure en acier ou en béton armé montée au large; une unité de stockage amarrée à l'unité de jetée fournissant un espace pour stocker du GNL; une unité de regazéification en tant que module qui regazéifie le GNL amené depuis l'unité de stockage, montée sur une partie supérieure de l'unité de jetée et pouvant être séparée de cette dernière; une unité de service comprenant une source d'alimentation et une pompe d'eau de mer pour fournir une alimentation et de l'eau de mer à l'unité de regazéification; et une unité de conduite qui comprend une conduite de décharge à connecter à l'unité de regazéification et à l'unité de stockage et une conduite d'amenée pour transporter le gaz naturel gazéifié par l'unité de regazéification.
EP11852293.7A 2010-12-30 2011-12-19 Installations pour stockage flottant de gaz naturel liquéfié au large comprenant une unité de regazéification de jetée Active EP2643629B1 (fr)

Priority Applications (1)

Application Number Priority Date Filing Date Title
PL11852293T PL2643629T3 (pl) 2010-12-30 2011-12-19 Urządzenia dla pływającego magazynu skroplonego gazu ziemnego na morzu z jednostką pomostową do regazyfikacji

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
KR1020100139360A KR101018741B1 (ko) 2010-12-30 2010-12-30 해상 제티 구조물을 이용한 엘엔지 재기화 설비
PCT/KR2011/009773 WO2012091337A2 (fr) 2010-12-30 2011-12-19 Installations pour stockage flottant de gaz naturel liquéfié au large comprenant une unité de regazéification de jetée

Publications (3)

Publication Number Publication Date
EP2643629A2 true EP2643629A2 (fr) 2013-10-02
EP2643629A4 EP2643629A4 (fr) 2017-04-19
EP2643629B1 EP2643629B1 (fr) 2019-12-11

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EP11852293.7A Active EP2643629B1 (fr) 2010-12-30 2011-12-19 Installations pour stockage flottant de gaz naturel liquéfié au large comprenant une unité de regazéification de jetée

Country Status (9)

Country Link
EP (1) EP2643629B1 (fr)
JP (1) JP5597773B2 (fr)
KR (1) KR101018741B1 (fr)
CN (1) CN103328879B (fr)
BR (1) BR112013016676B1 (fr)
CL (1) CL2013001923A1 (fr)
PL (1) PL2643629T3 (fr)
UY (1) UY33848A (fr)
WO (1) WO2012091337A2 (fr)

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KR20150026674A (ko) * 2013-08-29 2015-03-11 대우조선해양 주식회사 부유 저장식 가스 발전플랜트의 배치구조
KR101715061B1 (ko) 2015-07-02 2017-03-13 주식회사 가스이즈 선택 부유형 레그드 플랫폼 설비와 이의 건조방법 및 운용방법
CN107228275A (zh) * 2017-05-26 2017-10-03 惠生（南通）重工有限公司 一种可灵活组合且无人值守的浮式lng储存系统
WO2020115805A1 (fr) * 2018-12-03 2020-06-11 日揮グローバル株式会社 Installation flottante

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WO2012091337A2 (fr) 2012-07-05
EP2643629B1 (fr) 2019-12-11
KR101018741B1 (ko) 2011-03-04
CN103328879A (zh) 2013-09-25
BR112013016676B1 (pt) 2020-10-20
CL2013001923A1 (es) 2014-04-11
PL2643629T3 (pl) 2020-06-15
BR112013016676A2 (pt) 2016-10-04
EP2643629A4 (fr) 2017-04-19
WO2012091337A3 (fr) 2012-09-27
JP5597773B2 (ja) 2014-10-01
CN103328879B (zh) 2014-12-17
UY33848A (es) 2012-06-29
JP2014505842A (ja) 2014-03-06

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