CN102101520A - Twin-hulled lng floater - Google Patents
Twin-hulled lng floater Download PDFInfo
- Publication number
- CN102101520A CN102101520A CN2010105958714A CN201010595871A CN102101520A CN 102101520 A CN102101520 A CN 102101520A CN 2010105958714 A CN2010105958714 A CN 2010105958714A CN 201010595871 A CN201010595871 A CN 201010595871A CN 102101520 A CN102101520 A CN 102101520A
- Authority
- CN
- China
- Prior art keywords
- natural gas
- liquefied natural
- buoyancy body
- hull
- twin
- 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
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 37
- 239000003949 liquefied natural gas Substances 0.000 claims description 80
- 230000001105 regulatory effect Effects 0.000 claims description 4
- 239000013535 sea water Substances 0.000 claims description 4
- 238000009434 installation Methods 0.000 abstract 1
- 238000004519 manufacturing process Methods 0.000 description 5
- 238000005516 engineering process Methods 0.000 description 4
- 239000000446 fuel Substances 0.000 description 4
- 230000001131 transforming effect Effects 0.000 description 4
- 239000012528 membrane Substances 0.000 description 3
- 239000007789 gas Substances 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 238000003860 storage Methods 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000010779 crude oil Substances 0.000 description 1
- 238000005520 cutting process Methods 0.000 description 1
- 230000006837 decompression Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 239000012774 insulation material Substances 0.000 description 1
- 239000003345 natural gas Substances 0.000 description 1
- 238000005192 partition Methods 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
- 239000003643 water by type Substances 0.000 description 1
- 238000003466 welding Methods 0.000 description 1
Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B63—SHIPS OR OTHER WATERBORNE VESSELS; RELATED EQUIPMENT
- B63B—SHIPS OR OTHER WATERBORNE VESSELS; EQUIPMENT FOR SHIPPING
- B63B11/00—Interior subdivision of hulls
- B63B11/02—Arrangement of bulkheads, e.g. defining cargo spaces
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B63—SHIPS OR OTHER WATERBORNE VESSELS; RELATED EQUIPMENT
- B63B—SHIPS OR OTHER WATERBORNE VESSELS; EQUIPMENT FOR SHIPPING
- B63B25/00—Load-accommodating arrangements, e.g. stowing, trimming; Vessels characterised thereby
- B63B25/02—Load-accommodating arrangements, e.g. stowing, trimming; Vessels characterised thereby for bulk goods
- B63B25/08—Load-accommodating arrangements, e.g. stowing, trimming; Vessels characterised thereby for bulk goods fluid
- B63B25/12—Load-accommodating arrangements, e.g. stowing, trimming; Vessels characterised thereby for bulk goods fluid closed
- B63B25/16—Load-accommodating arrangements, e.g. stowing, trimming; Vessels characterised thereby for bulk goods fluid closed heat-insulated
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B63—SHIPS OR OTHER WATERBORNE VESSELS; RELATED EQUIPMENT
- B63B—SHIPS OR OTHER WATERBORNE VESSELS; EQUIPMENT FOR SHIPPING
- B63B1/00—Hydrodynamic or hydrostatic features of hulls or of hydrofoils
- B63B1/02—Hydrodynamic or hydrostatic features of hulls or of hydrofoils deriving lift mainly from water displacement
- B63B1/10—Hydrodynamic or hydrostatic features of hulls or of hydrofoils deriving lift mainly from water displacement with multiple hulls
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B63—SHIPS OR OTHER WATERBORNE VESSELS; RELATED EQUIPMENT
- B63B—SHIPS OR OTHER WATERBORNE VESSELS; EQUIPMENT FOR SHIPPING
- B63B13/00—Conduits for emptying or ballasting; Self-bailing equipment; Scuppers
-
- 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
- F17C2260/00—Purposes of gas storage and gas handling
- F17C2260/01—Improving mechanical properties or manufacturing
- F17C2260/016—Preventing slosh
-
- 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
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- Ocean & Marine Engineering (AREA)
- Physics & Mathematics (AREA)
- Fluid Mechanics (AREA)
- Filling Or Discharging Of Gas Storage Vessels (AREA)
Abstract
The present invention relates to a twin-hulled LNG floater, comprising: an LNG hull body (10) having a first ballast tank (11) where ballast water is held; a floatation body (20) which floats on the surface of the sea to the side adjacent but with a predetermined spacing from the LNG hull body (10), and which is provided with a second ballast tank (21) where ballast water is held; and liquefaction equipment (30) of which one end is supported connected to the LNG hull body (10) and the other end is supported connected to the floatation body (20). Consequently, the floatation body is provided to the side adjacent to the LNG hull body in such a way that the liquefaction equipment is supported connected to these bodies while at the same time the liquefaction equipment can be kept horizontal and can also be supported in a stable fashion by means of a water-level adjusting means on the floatation body, and hence the present invention basically gives advantageous effects such as that it improves the stability of the LNG floater as a whole through the twin-hulled arrangement employing the LNG hull body and the floatation body and, additionally, it allows for easy and rapid installation of liquefaction equipment without remodelling existing LNG vessels.
Description
Technical field
The present invention relates to a kind of twin-hull ship type liquefied natural gas floating drum, relate in particular to buoyancy body being set and connecting liquefaction device thereon it is supported at the liquefied natural gas hull in abutting connection with sidepiece, obtain stable support when the water level control apparatus by buoyancy body makes that liquefaction device is kept level simultaneously, thereby basically to utilize the catamaran mode of liquefied natural gas carrier body and buoyancy body, make liquefied natural gas floating drum single-piece stability improve, the while also can make being provided with easily of liquefaction device and promptly carry out under the situation of not transforming existing liquefied natural gas carrier.
Background technology
Usually, liquefied natural gas floating drum (LNG Floater; Floating type storage of LNG and production facilities) refer to have in the unsteady thing of barge form the offshore set-up of the equipment of producing liquefied natural gas or natural fuels.
This liquefied natural gas floating drum is also different according to the configuration of its top equipment of cargo hold shape that stores liquefied natural gas (LNG), for example, when cargo hold is spherical cargo hold (MOSS), owing to (Sloshing) problem of rocking that does not have liquefied natural gas is considered to safe, but at the FPSO (floating type crude oil production storage device) that make to produce liquefied natural gas thus or produce restriction on the space when operating liquefied natural gas carrier is transformed into LNG FPSO and require area more than the demand.
In addition, when cargo hold is film-type cargo hold (Membrane), owing to there are a lot of restrictions during the feasible cargo hold of using it for the liquefied natural gas floating drum such as the problem of rocking.Especially need to strengthen greatly the intensity of the insulated part of cargo hold, and the part of change cargo hold need be replaced when transforming by the heavy insulation material.
In addition, when cargo hold is prismatic cabin (SPB), estimate not exist the problem of rocking, therefore it is used as the liquefied natural gas floating drum, but need more cost of production compared with film-type cargo hold (Membrane).
In addition,, transform under the situation of existing liquefied natural gas carrier or new liquid making natural gas boat, have following problem according to each cargo hold shape in order to make the liquefied natural gas floating drum.
At first, when adopting film-type cargo hold (Membrane), because the problem of rocking need be provided with partition wall therebetween and use special chest, described chest is the insulated case that intensity increases.
In addition, when transforming the liquefied natural gas carrier making floating drum of navigation, has following problem: need to change cargo hold in-to-in insulated case it is strengthened, therefore do not utilize the liquefied natural gas carrier transformation but utilize LNG RV (Regasification Vessel) to transform.Therefore at this moment, need liquefaction device be set, in the middle of cutting off and when welding again, the insulated case (Insulation Box) of goods (Cargo) cargo hold damage be taken place and need carry out operation to cargo hold again with LNG RV separated into two parts and in the centre.
In addition, under the situation of spherical cargo hold (MOSS) type, have following problem: no matter be newly to make or transform, the narrow space of liquefaction device be set and because the height height of heat exchanger and column (Column), therefore can be very not enough for the space that is provided with.
Now, in order to develop middle-size and small-size gas field, need to have the liquefied natural gas floating drum of medium size liquefaction device on the market.
Therefore, because the expense of new liquid making natural fuels floating drum is more, attempting on the market to transform does not have the liquefied natural gas carrier of transportation planning to use.
Summary of the invention
The present invention makes in order to solve described problem, its purpose is, provide a kind of twin-hull ship type liquefied natural gas floating drum: in abutting connection with sidepiece buoyancy body is set at the liquefied natural gas hull, and the connection liquefaction device is supported it on these buoyancy body, water level control apparatus by buoyancy body simultaneously, when keeping the liquefaction device level, make it obtain stable support, thereby basically to utilize the catamaran mode of liquefied natural gas carrier body and buoyancy body, liquefied natural gas floating drum single-piece stability is improved, do not transform existing liquefied natural gas carrier simultaneously and also can make being provided with easily of liquefaction device and promptly carry out.
In order to realize described purpose, twin-hull ship type liquefied natural gas floating drum of the present invention comprises: the liquefied natural gas hull, and it has first ballast tank that stores ballast water; Buoyancy body, its have float separate with described liquefied natural gas hull certain distance on the seawater face of sidepiece and store ballast water power second ballast tank; And, liquefaction device, the one end is connected in described liquefied natural gas hull, is supported thereby its other end is connected in buoyancy body.
And,, preferably, share ballast water mutually thereby second ballast tank of first ballast tank of described liquefied natural gas hull and buoyancy body is communicated with by independent connection comb according to twin-hull ship type liquefied natural gas floating drum of the present invention.
And, according to twin-hull ship type liquefied natural gas floating drum of the present invention, preferably, also have water level control apparatus, be used to regulate the water level of the ballast water in second ballast tank of described buoyancy body.
And, according to twin-hull ship type liquefied natural gas floating drum of the present invention, described water level control apparatus comprises: air compressor, it supplies with pressurized air to described buoyancy body, makes the interior ballast water of second ballast tank of this buoyancy body be pushed and flow into first ballast tank of liquefied natural gas hull; Supply with comb, the one end is connected with described air compressor, and the other end is communicated with upper end one side of buoyancy body, thereby the pressurized air of described air compressor is fed to buoyancy body; And, discharge comb, it is configured in the adjacency section of described supply comb, thereby buoyancy body in-to-in air exhaustion is extremely outside.
And, according to twin-hull ship type liquefied natural gas floating drum of the present invention, preferably, on described supply comb, also having the supply control cock, it is used to regulate the delivery volume from air compressor compressed and supplied air.
And, according to twin-hull ship type liquefied natural gas floating drum of the present invention, preferably, on described discharge comb, also having the discharge control cock, its pressurized air that is used to regulate buoyancy body is expelled to exterior discharge rate.
Beneficial effect of the present invention is: according to the twin-hull ship type liquefied natural gas floating drum of one embodiment of the invention buoyancy body being set and connecting liquefaction device thereon in abutting connection with sidepiece it is supported at the liquefied natural gas hull, water level control apparatus by buoyancy body makes liquefaction device keep balance and obtains stable support simultaneously, thereby basically to utilize the catamaran mode of liquefied natural gas carrier body and buoyancy body, make liquefied natural gas floating drum single-piece stability improve, not transforming existing liquefied natural gas carrier simultaneously also can be easily and liquefaction device promptly is set.
Description of drawings
Fig. 1 is the skeleton diagram of expression according to the twin-hull ship type liquefied natural gas floating drum of one embodiment of the invention.
The specific embodiment
Further describe the present invention with reference to accompanying drawing.
As shown in Figure 1, twin-hull ship type liquefied natural gas floating drum according to an embodiment of the invention comprises: liquefied natural gas hull 10, and it has first ballast tank 11 that stores ballast water; Buoyancy body 20, its have float separate with described liquefied natural gas hull 10 certain distance on the seawater face of sidepiece and store second ballast tank 21 of ballast water; And, liquefaction device 30, the one end is connected in described liquefied natural gas hull 10, is supported thereby its other end is connected in buoyancy body 20.
And, also having water level control apparatus, it is used to regulate the water level of the ballast water in second ballast tank 21 of described buoyancy body 20.
At this, described water level control apparatus comprises: air compressor 50, and it supplies with pressurized air to described buoyancy body 20, makes second ballast tank, the 21 interior ballast waters of this buoyancy body 20 be pushed into and flow into first ballast tank 11 of liquefied natural gas hull 10; Supply with comb 60, the one end is connected with described air compressor 50, and the other end is communicated with upper end one side of buoyancy body 20, thereby the pressurized air of described air compressor 50 is fed to buoyancy body 20; And, discharge comb 70, it is configured in the adjacency section of described supply comb 60, thereby buoyancy body 20 in-to-in air exhaustion are extremely outside.
Also have, also have the control cock 61 of supply on supply comb 60, it is used to regulate the delivery volume from air compressor 50 compressed and supplied air.And, on described discharge comb 70, also having and discharge control cock 71, its pressurized air that is used to regulate buoyancy body is expelled to exterior discharge rate.
At this, preferably, described air compressor 50 uses the suction system of existing liquefied natural gas hull 10, thereby the pressurization/decompression of air is carried out repeatedly and then regulated the water level of the ballast water of buoyancy body 20.
Also have, when regulating described water level, preferably, inclination supervisory system (not shown) is used in interlock, controls with the inclination of consideration liquefied natural gas hull 10 and to it.
Twin-hull ship type liquefied natural gas floating drum according to described formation as one embodiment of the invention, after the buoyancy body 20 of floating on the seawater face of sidepiece of liquefied natural gas hull 10, be communicated with each ballast tank 11,21 of these liquefied natural gas hulls 10 and buoyancy body 20 by being communicated with comb 40, thereby make it share ballast water each other.
Afterwards, liquefaction device 30 is set, makes that irritating 11,21 tops at ballast connects the both sides of liquefaction device 30 respectively and be supported.
Also have, connect as the supply comb 60 of ballast water water level control apparatus and discharge comb 70, and air compressor 50 is set supplying with comb 60, thereby finish the making of twin-hull ship type liquefied natural gas floating drum of the present invention in buoyancy body 20.
Under the state that the liquefied natural gas floating drum of finishing thus floats, produce liquefied natural gas or natural fuels at sea by liquefaction device 30.
Also have, in the production of this liquefied natural gas or natural fuels, if the degree of dip that liquefaction device 30 takes place not to and be in an unsure state, thereby the ballast of then regulating buoyancy body 20 in view of the above makes liquefaction device 30 become stable status.
Promptly, because buoyancy body 20 is positioned at the position higher than liquefied natural gas hull 10, thereby cause liquefaction device 30 when 10 inclinations of liquefied natural gas hull are oblique, the state that owing to second ballast tank, the 21 in-to-in air pressure height of buoyancy body 20 and ballast water are less buoyancy body is in to float.Therefore, the discharge control cock 71 that comb 70 is discharged in operation is expelled to the outside with air pressure, thereby realizes buoyancy body 20 and liquefied natural gas hull 10 balances.
At this moment, the supply control cock 61 of supply comb 60 will keep the osed top state.
In contrast, buoyancy body 20 is positioned at than liquefied natural gas hull 10 low positions and makes liquefaction device 30 when buoyancy body 20 inclinations are oblique, because second ballast tank, the 21 in-to-in air pressure of buoyancy body 20 are low and ballast water is more, thereby makes buoyancy body be in the state of sinking.Therefore at this moment, need to start the supply control cock 61 of air compressor 50 and operation supply comb 70, make a part of ballast water flow into first ballast tank to second ballast tank, the 21 inner high pressure that inject, thereby buoyancy body is lightened, and then realize buoyancy body 20 and liquefied natural gas hull 10 balances.
At this moment, the discharge control cock 71 of discharge comb 70 will keep the osed top state.
So, water level control apparatus carries out work in real time, and continues to keep liquefaction device 30 to be in stabilized conditions, and carries out the gas production operation.
Though preferred embodiments of the present invention have been disclosed for illustrative in the above, but, should be appreciated that those skilled in the art in the invention are to simple the present invention of change described embodiment and the existing embodiment that knows that technology merely makes up and be suitable for and claims of the present invention and the detailed explanation and utilize the technology of degree should be contained in technology category of the present invention.
Claims (6)
1. twin-hull ship type liquefied natural gas floating drum, it comprises:
Liquefied natural gas hull (10), it has first ballast tank (11) that stores ballast water;
Buoyancy body (20), its have float separate with described liquefied natural gas hull (10) certain distance on the seawater face of sidepiece and store second ballast tank (21) of ballast water; And
Liquefaction device (30), one end are connected in described liquefied natural gas hull (10), and its other end is connected in buoyancy body (20) thereby is supported.
2. twin-hull ship type liquefied natural gas floating drum according to claim 1, wherein:
First ballast tank (11) of described liquefied natural gas hull (10) and second ballast tank (21) of buoyancy body (20) by independent connection comb (40) thus be communicated with and share ballast water mutually.
3. twin-hull ship type liquefied natural gas floating drum according to claim 2, wherein:
Also have water level control apparatus, be used to regulate the water level of the ballast water in second ballast tank (21) of described buoyancy body (20).
4. twin-hull ship type liquefied natural gas floating drum according to claim 3, wherein, described water level control apparatus comprises:
Air compressor (50), it supplies with pressurized air to described buoyancy body (20), makes the interior ballast water of second ballast tank (21) of this buoyancy body (20) be pushed into and flow into first ballast tank (11) of liquefied natural gas hull (10);
Supply with comb (60), the one end is connected with described air compressor (50), and the other end is communicated with upper end one side of buoyancy body (20), thereby the pressurized air of described air compressor (50) is fed to buoyancy body (20); And
Discharge comb (70), it is configured in the adjacency section of described supply comb (60), thereby buoyancy body (20) in-to-in air exhaustion is extremely outside.
5. twin-hull ship type liquefied natural gas floating drum according to claim 4, wherein:
Also have supply control cock (61) on the described supply comb (60), it is used for regulating the delivery volume from air compressor (50) compressed and supplied air.
6. twin-hull ship type liquefied natural gas floating drum according to claim 4, wherein:
Also have discharge control cock (71) on described discharge comb (70), its pressurized air that is used to regulate described buoyancy body is expelled to exterior discharge rate.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| KR10-2009-0126843 | 2009-12-18 | ||
| KR1020090126843A KR101122350B1 (en) | 2009-12-18 | 2009-12-18 | Catamaran type LNG floater |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN102101520A true CN102101520A (en) | 2011-06-22 |
| CN102101520B CN102101520B (en) | 2013-11-13 |
Family
ID=44154633
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2010105958714A Expired - Fee Related CN102101520B (en) | 2009-12-18 | 2010-12-20 | Twin-hulled lng floater |
Country Status (7)
| Country | Link |
|---|---|
| KR (1) | KR101122350B1 (en) |
| CN (1) | CN102101520B (en) |
| BR (1) | BRPI1011115A2 (en) |
| MY (1) | MY160175A (en) |
| RU (1) | RU2497711C1 (en) |
| SG (1) | SG172573A1 (en) |
| WO (1) | WO2011074926A2 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104302540A (en) * | 2012-04-20 | 2015-01-21 | Sbm斯希丹公司 | Floating LNG plant comprising first and second converted LNG carrier and method for obtaining floating LNG plant |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| RU2619670C1 (en) * | 2015-12-09 | 2017-05-17 | Федеральное Государственное Бюджетное Образовательное Учреждение Высшего Образования "Донской Государственный Аграрный Университет" (Фгбоу Во Дгау) | Gas-waterjet drive of wave power plant |
| KR101840649B1 (en) | 2017-11-20 | 2018-03-21 | 알렌 주식회사 | A buoyant system of floating electricity generation platform |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS59202988A (en) * | 1983-04-28 | 1984-11-16 | Tomio Ueda | Twin hulled modular boat |
| JPH01226488A (en) * | 1988-03-08 | 1989-09-11 | Kawasaki Heavy Ind Ltd | Ballast regulator for floating body such as vessel |
| JPH058789A (en) * | 1990-10-29 | 1993-01-19 | Furuno Electric Co Ltd | Mooring apparatus for vessel |
| US5233937A (en) * | 1991-10-21 | 1993-08-10 | Mitsubishi Jukogyo Kabushiki Kaisha | Ballast tank internal gas controlling type tanker |
| US6805598B2 (en) * | 2002-09-06 | 2004-10-19 | Dorob International Ltd. | Liquid natural gas transfer station |
| CN101061344A (en) * | 2004-11-22 | 2007-10-24 | 蓝水能源服务公司 | Apparatus for offshore transfer of fluid |
| WO2009119953A1 (en) * | 2008-03-28 | 2009-10-01 | Samsung Heavy Ind. Co., Ltd. | Lng carrier having an lng loading and unloading system |
| US20090293506A1 (en) * | 2008-05-30 | 2009-12-03 | Daewoo Shipbuilding & Marine Engineering Co., Ltd. | Semi-Submersible Offshore Structure Having Storage Tanks for Liquified Gas |
Family Cites Families (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3653354A (en) * | 1970-03-02 | 1972-04-04 | Flume Stabilization Syst | Catamaran stabilizer |
| JPH11285615A (en) * | 1998-04-03 | 1999-10-19 | Ishikawajima Harima Heavy Ind Co Ltd | Waste gas discharge treatment for floating body liquefaction and storage equipment and device therefor |
| RU2219091C2 (en) * | 2000-05-31 | 2003-12-20 | Абрамов Валентин Алексеевич | Natural gas field development complex |
| KR100503509B1 (en) * | 2002-06-12 | 2005-07-25 | 강도욱 | Offshore LNG regasfication method |
| JP2009184378A (en) | 2008-02-01 | 2009-08-20 | Mitsubishi Heavy Ind Ltd | Ship |
| BRPI0800985A2 (en) | 2008-04-10 | 2011-05-31 | Internat Finance Consultant Ltda | integrated process for obtaining gnl and gnc and their energy suitability, flexibly integrated system for carrying out said process and uses of gnc obtained by said process |
-
2009
- 2009-12-18 KR KR1020090126843A patent/KR101122350B1/en active IP Right Grant
-
2010
- 2010-12-17 SG SG2010093748A patent/SG172573A1/en unknown
- 2010-12-20 WO PCT/KR2010/009103 patent/WO2011074926A2/en active Application Filing
- 2010-12-20 BR BRPI1011115-8A2A patent/BRPI1011115A2/en not_active IP Right Cessation
- 2010-12-20 MY MYPI2012002718A patent/MY160175A/en unknown
- 2010-12-20 CN CN2010105958714A patent/CN102101520B/en not_active Expired - Fee Related
- 2010-12-20 RU RU2012130400/11A patent/RU2497711C1/en not_active IP Right Cessation
Patent Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS59202988A (en) * | 1983-04-28 | 1984-11-16 | Tomio Ueda | Twin hulled modular boat |
| JPH01226488A (en) * | 1988-03-08 | 1989-09-11 | Kawasaki Heavy Ind Ltd | Ballast regulator for floating body such as vessel |
| JPH058789A (en) * | 1990-10-29 | 1993-01-19 | Furuno Electric Co Ltd | Mooring apparatus for vessel |
| US5233937A (en) * | 1991-10-21 | 1993-08-10 | Mitsubishi Jukogyo Kabushiki Kaisha | Ballast tank internal gas controlling type tanker |
| US6805598B2 (en) * | 2002-09-06 | 2004-10-19 | Dorob International Ltd. | Liquid natural gas transfer station |
| CN101061344A (en) * | 2004-11-22 | 2007-10-24 | 蓝水能源服务公司 | Apparatus for offshore transfer of fluid |
| WO2009119953A1 (en) * | 2008-03-28 | 2009-10-01 | Samsung Heavy Ind. Co., Ltd. | Lng carrier having an lng loading and unloading system |
| US20090293506A1 (en) * | 2008-05-30 | 2009-12-03 | Daewoo Shipbuilding & Marine Engineering Co., Ltd. | Semi-Submersible Offshore Structure Having Storage Tanks for Liquified Gas |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104302540A (en) * | 2012-04-20 | 2015-01-21 | Sbm斯希丹公司 | Floating LNG plant comprising first and second converted LNG carrier and method for obtaining floating LNG plant |
| CN104302540B (en) * | 2012-04-20 | 2017-08-04 | Sbm斯希丹公司 | The method of floating LNG factories and acquisition floating LNG factories including the first repacking LNG ship and the second repacking LNG ship |
Also Published As
| Publication number | Publication date |
|---|---|
| CN102101520B (en) | 2013-11-13 |
| KR20110070133A (en) | 2011-06-24 |
| MY160175A (en) | 2017-02-28 |
| WO2011074926A3 (en) | 2011-10-27 |
| RU2497711C1 (en) | 2013-11-10 |
| KR101122350B1 (en) | 2012-03-23 |
| SG172573A1 (en) | 2011-07-28 |
| BRPI1011115A2 (en) | 2013-12-24 |
| WO2011074926A4 (en) | 2012-01-26 |
| WO2011074926A2 (en) | 2011-06-23 |
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