CN102192401A - Floating LNG revaporization equipment - Google Patents
Floating LNG revaporization equipment Download PDFInfo
- Publication number
- CN102192401A CN102192401A CN2011100209418A CN201110020941A CN102192401A CN 102192401 A CN102192401 A CN 102192401A CN 2011100209418 A CN2011100209418 A CN 2011100209418A CN 201110020941 A CN201110020941 A CN 201110020941A CN 102192401 A CN102192401 A CN 102192401A
- Authority
- CN
- China
- Prior art keywords
- lng
- gas
- machine
- turbine generator
- floating type
- 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
Images
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F02—COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
- F02C—GAS-TURBINE PLANTS; AIR INTAKES FOR JET-PROPULSION PLANTS; CONTROLLING FUEL SUPPLY IN AIR-BREATHING JET-PROPULSION PLANTS
- F02C1/00—Gas-turbine plants characterised by the use of hot gases or unheated pressurised gases, as the working fluid
- F02C1/02—Gas-turbine plants characterised by the use of hot gases or unheated pressurised gases, as the working fluid the working fluid being an unheated pressurised gas
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F02—COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
- F02C—GAS-TURBINE PLANTS; AIR INTAKES FOR JET-PROPULSION PLANTS; CONTROLLING FUEL SUPPLY IN AIR-BREATHING JET-PROPULSION PLANTS
- F02C6/00—Plural gas-turbine plants; Combinations of gas-turbine plants with other apparatus; Adaptations of gas- turbine plants for special use
- F02C6/04—Gas-turbine plants providing heated or pressurised working fluid for other apparatus, e.g. without mechanical power output
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P80/00—Climate change mitigation technologies for sector-wide applications
- Y02P80/10—Efficient use of energy, e.g. using compressed air or pressurized fluid as energy carrier
- Y02P80/15—On-site combined power, heat or cool generation or distribution, e.g. combined heat and power [CHP] supply
Abstract
The present invention relates to flowing LNG revaporization equipment. The flowing LNG revaporization equipment comprises an LNG storage tank (10) and an LNG revaporizer (20), wherein the flowing LNG revaporization equipment further comprises power generation equipment which is capable of generating power, as well as generating gas through the LNG revaporizer (20). Accordingly, since a gas turbine generator which is a power generating equipment to generate power is additionally included in the revaporization equipment to revaporize LNG, more specifically, it is possible to supply gas and electricity at the same time. Also, since it is possible to drive the gas turbine generator with gas generated from the revaporization equipment, a compressor for processing gas is removed from the gas turbine generator, so that it is possible to reduce the cost for installing the gas turbine generator. In addition, after vapor is generated using exhaust gas which is generated from the gas turbine generator, the generated gas can be used as the driving power for the LNG revaporizer and a steam turbine generator which is additionally included to generate electricity. Thus, it is possible to minimize the energy required for the entire equipment according to waste heat recovery, so that it is possible to reduce the cost and to prevent oceanic pollution through the usage of waste heat.
Description
Technical field
The present invention relates to floating type liquefaction regasification equipment, relate in particular to and be used for the equipment for gasification again of lng regas, additional as can producing the gas turbine generator of the Electric Power Generating Equipment of electric power, thus supply gas and electric power simultaneously basically.And, utilize the gas that in equipment for gasification again, produces, drive gas turbine generator, thereby can remove compressor, and then reduce the expense that gas turbine generator is set for the gas compression of gas turbine generator.And, after the exhausting air that produces generates steam, use it for the driving power of steam turbin generator in utilizing gas turbine generator, described steam turbin generator is for lng regas machine and generating and additional.Thereby by reclaiming used heat, the required energy of integral device is minimized, help the minimizing of expense, by using heat extraction, can also prevent the floating type liquefaction regasification equipment of marine pollution simultaneously.
Background technique
Usually, LNG Liquefied natural gas floating drum (LNG Floater; Floating type storage of LNG and equipment for gasification again) refer on the unsteady thing of barge form, to have the offshore set-up of the equipment of production LNG Liquefied natural gas (LNG) or rock gas (Natural Gas).
This LNG Liquefied natural gas floating drum (LNG Floater) is also different according to the configuration of its top equipment of shape of the cargo hold that stores LNG Liquefied natural gas.For example, when cargo hold is spherical cargo hold (MOSS), owing to the problem of rocking that does not have LNG Liquefied natural gas is considered to safe.But produce the restriction on the space when being transformed into LNG FPSO and require area more than the demand at the FPSO (floating type crude oil production storage device) that makes the production LNG Liquefied natural gas or with operating liquefied natural gas (LNG) carrier.
In addition, when cargo hold is film type cargo hold (Membrane), because there are a lot of restrictions during as the cargo hold of LNG Liquefied natural gas floating drum in the problems of rocking etc., particularly need to strengthen greatly the intensity of the insulated part of cargo hold, and the part that will change cargo hold when transforming is replaced by the heavy insulation material.
In addition, when cargo hold is self-support square cargo hold (SPB), estimate not exist problem, therefore use, but need more operating cost compared with film type cargo hold (Membrane) as the LNG Liquefied natural gas floating drum to rocking.
So, utilize multiple liquefied natural gas (LNG) regasification facilities according to the cargo hold shape, thus can be at sea, with seawater face quick condition process gas.
As an example, below be floating type liquefaction regasification equipment according to prior art.
As shown in Figure 1, be in the floating type liquefaction regasification equipment of the prior art of marine quick condition, it comprises: liquified natural gas tank 10, and it stores LNG Liquefied natural gas respectively; Low pressure pump 81, it is expelled to the outside with the LNG Liquefied natural gas in the described liquified natural gas tank 10; Knock out drum 82, it is arranged on the outside, thereby is used for the LNG Liquefied natural gas that disposable mitigation is discharged from liquified natural gas tank 10; High-pressure service pump 83, its LNG Liquefied natural gas with described knock out drum 82 is expelled to the outside; Flow control valve 84, the flow of its control LNG Liquefied natural gas is supplied with; And, lng regas machine 20, it is used for the gasification again of LNG Liquefied natural gas.
By the prior art of formation like this, obtain the supply of LNG Liquefied natural gas from liquified natural gas tank 10, thus process gas after LNG Liquefied natural gas is gasified again.
Summary of the invention
But the liquefied natural gas (LNG) regasification facilities of a this prior art process gas needs to use seawater in order to gasify, so the environment of ocean is produced harmful effect again.And when summer that gas consumption reduces, LNG Liquefied natural gas is elongated between the storage life, thereby will be passed on the gas that produces to force incineration or be discarded to atmosphere by heat, thereby causes the waste of the energy.And, when the generator that uses for the construction of supporting coastal facility, exist because of using existing fuel to cause the problem of marine pollution etc.
The present invention proposes in order to solve described problem, its purpose is, a kind of floating type liquefaction regasification equipment is provided, it is being used for the additional gas turbine generator that can produce the Electric Power Generating Equipment of electric power on the equipment for gasification again of lng regas, thereby basically can while supply gas and electric power.
And, can utilize the gas-powered gas turbine generator that in equipment for gasification again, produces, thereby remove the compressor of the gas compression that is used for gas turbine generator, and then reduce the expense that gas turbine generator is set.
And, the exhausting air that in utilizing gas turbine generator, produces and after generating steam, used as for lng regas machine and generating and the driving power of the steam turbin generator that appends, thereby by reclaiming used heat, the energy that integral device is required minimizes, when helping reducing expense,, can also prevent marine pollution by using used heat.
The of the present invention floating type liquefaction regasification equipment that proposes in order to realize described purpose, it comprises liquefied natural gas storage tanks and lng regas machine.It also comprises, Electric Power Generating Equipment, and it can also produce electric power by described lng regas machine process gas the time.
And, in floating type liquefaction regasification equipment according to the present invention, preferably, described Electric Power Generating Equipment is produced electric power by gas turbine generator, and described gas turbine generator relies on the gasifying gas again of lng regas machine production to carry out work.
And, according to floating type liquefaction regasification equipment of the present invention, also comprising the exhausting air heat exchanger, it utilizes the exhausting air of described gas turbine generator generation and produces high-temperature steam.
And according to floating type liquefaction regasification equipment of the present invention, described lng regas machine uses the steam that described exhausting air heat exchanger 40 generates as the energy that makes lng regas.
And according to floating type liquefaction regasification equipment of the present invention, the steam shift by described lng regas machine is a water, thereby re-uses as the water of condensation that generates steam at the exhausting air heat exchanger again.
And, according to floating type liquefaction regasification equipment of the present invention, also comprise heat exchanger, thereby it heats the water of condensation that is transformed to high temperature to the water of discharging at described lng regas machine.
And, according to floating type liquefaction regasification equipment of the present invention, described heat exchanger utilizes the water of the cooling that the lng regas machine discharges, and the high-temperature cooling water of the discharges such as air-conditioning system on described gas turbine generator or the equipment for gasification is more in addition cooled off.
And, according to floating type liquefaction regasification equipment of the present invention, also comprising steam turbin generator, it utilizes the steam that produces and generates electricity in described exhausting air heat exchanger.
And according to floating type liquefaction regasification equipment of the present invention, the water of discharging from described steam turbin generator mixes with the water of lng regas machine discharge and supplies to heat exchanger.
And, according to floating type liquefaction regasification equipment of the present invention, also comprising the supply stream, it is used for supplying to the lng regas machine in the exhausting air that described exhausting air heat exchanger produces.
As mentioned above, floating type liquefaction regasification equipment according to an embodiment of the invention, be used for the equipment for gasification again of lng regas, additional conduct can be produced the gas turbine generator of the Electric Power Generating Equipment of electric power, thereby basically can while supply gas and electric power.
And, utilize the gas that produces at equipment for gasification again and drive gas turbine generator, thereby remove the compressor of the gas compression that is used for gas turbine generator, and then reduce the expense that gas turbine generator is set.
And, the exhausting air that utilization produces at gas turbine generator and after generating steam, be used for for lng regas machine and generating and the driving power of additional steam turbin generator, thereby by reclaiming used heat, the required energy of integral device is minimized, help the minimizing of expense, and by using used heat, can also obtain preventing the effect of marine pollution etc.
Description of drawings
Fig. 1 represents the synoptic diagram according to the floating type liquefaction regasification equipment of prior art.
Fig. 2 represents also to comprise on the floating type liquefaction regasification equipment according to an embodiment of the invention the synoptic diagram of the state of Electric Power Generating Equipment.
Embodiment
The following accompanying drawing of reference further describes has the present invention who as above constitutes.
As shown in Figure 2, floating type according to an embodiment of the invention liquefaction regasification equipment, it comprises: liquefied natural gas (LNG) tank 10; Lng regas machine 20; And, Electric Power Generating Equipment, it can produce electric power.
At this, described Electric Power Generating Equipment is produced electric power by gas turbine generator 30, and gas turbine generator is the work of gasifying gas again of producing according to lng regas machine 20.
And, also comprise exhausting air heat exchanger 40, the exhausting air that it utilizes described gas turbine generator 30 to produce, thus produce high-temperature steam.
At this, described lng regas machine 20 uses the steam that described exhausting air heat exchanger 40 generates as the energy that makes lng regas.
And making the steam shift by described lng regas machine 20 is water, thereby re-uses as the water of condensation that generates steam in exhausting air heat exchanger 40 again.
And, also comprising heat exchanger 50, the water that it utilizes lng regas machine 20 to discharge cools off the cooling water of the high temperature that air-conditioning system on described gas turbine generator 30 or the equipment for gasification more in addition etc. discharges.
At this, the heat that the heat exchange by described heat exchanger 50 produces also comprises the effect that water that lng regas machine 20 is discharged heats.
And, also comprising steam turbin generator 60, it is as Electric Power Generating Equipment of the present invention, utilizes the steam that produces at described exhausting air heat exchanger 40 and generates electricity.
Also have, the water that described steam turbine 60 is discharged mixes with the water that lng regas machine 20 is discharged, and supplies to heat exchanger 50.
In addition, comprise also and supply with stream 70 that it supplies to lng regas machine 20 for the exhausting air that described exhausting air heat exchanger 40 is produced.
Low pressure pump in the undeclared label 81 expression liquified natural gas tanks, label 82 expression knock out drums, label 83 expression high-pressure service pumps, label 84 expression flow control valves.
And, undeclared label 85 expression gas flowmeters, label 86 expression dispensers, label 87 expression transformation machines, label 88 expression recycle pumps.
Floating type liquefaction regasification equipment according to described formation as one embodiment of the present of invention, basically receive the supply of LNG Liquefied natural gas by low pressure pump 81, knock out drum 82 and high-pressure service pump 83 from liquefied natural gas storage tanks 10, thereby make at liquid gas gasifying machine 20 process gas again, append at this and Electric Power Generating Equipment is set and produces electric power.
Below the power production process by described Electric Power Generating Equipment is understood, at first, be provided with gas turbine generator 30, drive gas turbine generator 30 by the gasifying gas of producing at lng regas machine 20 again and produce electric power as Electric Power Generating Equipment.
At this, the exhausting air that described gas turbine generator 30 produces in exhausting air heat exchanger 40, generate steam with water of condensation by heat exchange after, it is expelled in the atmosphere.
And the high-temperature steam that produces by described heat exchange uses as the energy of the lng regas of described lng regas machine 20.
That is, begin this moment, and lng regas machine 20 does not use the diesel oil as starting fluid, and utilize the steam that generates at exhausting air heat exchanger 40 to operate.
And making the steam shift by described lng regas machine 20 is water, thereby in exhausting air heat exchanger 40, again as the water of condensation that generates steam.
At this moment, making the steam shift by described lng regas machine 20 is that water (about 20 ℃) supplies to heat exchanger 50, then, in this heat exchanger 50, by with gas turbine generator 30 or equipment for gasification more in addition on the cooling water of high temperature (about 60 ℃) of discharges such as air-conditioning system carry out heat exchange, make the cooling water of this high temperature be transformed to the cooling water of low temperature (about 30 ℃), thus again as described gas turbine generator 30 or again air-conditioning system on the equipment for gasification etc. cooling water and re-use.
In addition, will supply to the steam turbin generator 60 that can generate electricity at a part of steam that described exhausting air heat exchanger 40 produces and produce electric power.
And the water of discharging from this steam turbine mixes with the water from 20 discharges of lng regas machine and supplies to heat exchanger 50.
At this moment, the water that carries out heat exchange in heat exchanger 50 will reach about 45～50 ℃, by recycle pump 88, supply to exhausting air heat exchanger 40 as water of condensation.
In addition, the exhausting air from described exhausting air heat exchanger 40 is discharged can also supply to lng regas machine 20 again by independent supply stream 70.
So, the present invention utilizes this gas-powered gas turbine generator 30 that gasifies again and generates electricity by lng regas machine 20 process gas time.And, utilize the exhausting air of this gas turbine generator 30 and make steam, it is used for the driving raw material of lng regas machine 20 and steam turbin generator 60, thereby when using the energy effectively, can also obtain preventing multiple effects such as marine pollution.
Describe by the preferred embodiments of the present invention above, but, not only merely make up and among the embodiment that is suitable at described embodiment and existing known technology, simultaneously in claim scope of the present invention and detailed explanation, those skilled in the art in the invention merely are out of shape the present invention, thereby available technology should be included in technical scope of the present invention.
Claims (10)
1. a floating type liquefaction regasification equipment comprises liquefied natural gas storage tanks 10 and lng regas machine 20, it is characterized in that, also comprise: Electric Power Generating Equipment, it in process gas, can also produce electric power by described lng regas machine 20.
2. floating type liquefaction regasification equipment according to claim 1 is characterized in that:
Described Electric Power Generating Equipment is produced electric power by gas turbine generator 30, and the gasifying gas again that described gas turbine generator 30 relies on lng regas machine 20 to produce carries out work.
3. floating type liquefaction regasification equipment according to claim 2 is characterized in that, also comprises:
Exhausting air heat exchanger 40, it utilizes the exhausting air of described gas turbine generator 30 generations and produces high-temperature steam.
4. floating type liquefaction regasification equipment according to claim 3 is characterized in that:
Described lng regas machine 20 uses the steam that described exhausting air heat exchanger 40 generates as the energy that makes lng regas.
5. floating type liquefaction regasification equipment according to claim 4 is characterized in that:
Steam shift by described lng regas machine 20 is a water, thereby re-uses as the water of condensation that generates steam in exhausting air heat exchanger 40 again.
6. floating type liquefaction regasification equipment according to claim 5 is characterized in that, also comprises:
Heat exchanger 50, thus it heats the water of condensation that is transformed to high temperature to the water of discharging at described lng regas machine 20.
7. floating type liquefaction regasification equipment according to claim 6 is characterized in that:
Described heat exchanger 50 utilizes the cooling water of discharging from lng regas machine 20, and the high-temperature cooling water of the discharges such as air-conditioning system on described gas turbine generator 30 or the equipment for gasification is more in addition cooled off.
8. floating type liquefaction regasification equipment according to claim 3 is characterized in that, also comprises:
Steam turbin generator 60, it utilizes from the steam of described exhausting air heat exchanger 40 generations and generates electricity.
9. floating type liquefaction regasification equipment according to claim 8 is characterized in that:
The water of discharging from described steam turbin generator 60 mixes with the water from 20 discharges of lng regas machine and supplies to heat exchanger 50.
10. floating type liquefaction regasification equipment according to claim 3 is characterized in that, also comprises:
Supply with stream 70, be used for the exhausting air that described exhausting air heat exchanger 40 produces is offered lng regas machine 20.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| KR1020100007662A KR101121721B1 (en) | 2010-01-28 | 2010-01-28 | Floating type LNG regasification unit |
| KR10-2010-0007662 | 2010-01-28 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN102192401A true CN102192401A (en) | 2011-09-21 |
| CN102192401B CN102192401B (en) | 2014-07-09 |
Family
ID=44319944
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201110020941.8A Expired - Fee Related CN102192401B (en) | 2010-01-28 | 2011-01-18 | Floating LNG revaporization equipment |
Country Status (7)
| Country | Link |
|---|---|
| JP (1) | JP5183756B2 (en) |
| KR (1) | KR101121721B1 (en) |
| CN (1) | CN102192401B (en) |
| BR (1) | BRPI1100658A2 (en) |
| NO (1) | NO20110059A1 (en) |
| SG (1) | SG173272A1 (en) |
| WO (1) | WO2011093591A2 (en) |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103225740A (en) * | 2013-04-22 | 2013-07-31 | 中国海洋石油总公司 | BOG processing system utilizing pressure energy of LNG receiving station |
| CN103225739A (en) * | 2013-04-22 | 2013-07-31 | 中国海洋石油总公司 | Energy-saving processing system for vapor of LNG receiving station |
| CN104315339A (en) * | 2014-10-27 | 2015-01-28 | 中国海洋石油总公司 | LNG stepped regasification system applied to marine floating type LNG regasification device and regasification method |
| CN109424341A (en) * | 2017-09-05 | 2019-03-05 | 斗山重工业建设有限公司 | Use the system of the carbon dioxide in the exhaust gas by the cold and hot collection of liquefied natural gas |
| CN109578806A (en) * | 2018-12-07 | 2019-04-05 | 江苏中圣压力容器装备制造有限公司 | A kind of process unit of LNG flash steam (BOG) pressurization condensing recovery |
| CN109760783A (en) * | 2019-01-25 | 2019-05-17 | 太平洋海洋工程（舟山）有限公司 | A kind of ventilative mast suitable for FSRU |
| CN113022792A (en) * | 2016-04-07 | 2021-06-25 | 现代重工业株式会社 | Ship with gas regasification system |
Families Citing this family (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR101419009B1 (en) * | 2012-04-17 | 2014-07-15 | 에스티엑스조선해양 주식회사 | Lng regasification apparatus having combined cycle power plant |
| KR101665328B1 (en) * | 2012-05-25 | 2016-10-24 | 대우조선해양 주식회사 | Marine Electricity Generation Module Using Waste Heat In Cooling Water Of Condenser |
| KR101260993B1 (en) * | 2012-10-29 | 2013-05-06 | 주식회사 디섹 | Floating facility mounted power plant |
| KR101260992B1 (en) * | 2012-10-29 | 2013-05-06 | 주식회사 디섹 | Floating facility mounted power plant |
| KR101260994B1 (en) * | 2012-10-29 | 2013-05-06 | 주식회사 디섹 | Floating facility mounted power plant |
| KR101814446B1 (en) * | 2016-05-24 | 2018-01-05 | 삼성중공업 주식회사 | Fuel gas supply system |
| KR20190008790A (en) * | 2017-07-17 | 2019-01-25 | 현대중공업 주식회사 | A Engine cooling water expansion tank and Cooling water treatment system and Vessel having the same |
| CN110107368B (en) * | 2019-06-11 | 2024-04-19 | 赫普科技发展（北京）有限公司 | Steam condensing method, steam condensing system and power generation system |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5833594A (en) * | 1981-08-20 | 1983-02-26 | Mitsubishi Heavy Ind Ltd | Compound energy conservation type equipment for liquefied-gas ship |
| JPH05113108A (en) * | 1991-10-23 | 1993-05-07 | Osaka Gas Co Ltd | Cold heat power generator utilizing liquefied natural gas |
| WO2005091932A2 (en) * | 2004-03-04 | 2005-10-06 | Single Buoy Moorings, Inc. | Floating power generation system |
| CN1852832A (en) * | 2003-09-19 | 2006-10-25 | 信号系泊浮筒公司 | Gas offloading system |
| CN101057101A (en) * | 2004-11-08 | 2007-10-17 | 国际壳牌研究有限公司 | Liquefied natural gas floating storage regasification unit |
| CN101305238A (en) * | 2005-12-22 | 2008-11-12 | 单浮筒系泊公司 | Enhanced lng regas |
Family Cites Families (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH10267197A (en) * | 1997-03-25 | 1998-10-09 | Ishikawajima Harima Heavy Ind Co Ltd | Storing facilities for low temperature liquefied gas |
| KR100489804B1 (en) * | 2002-11-28 | 2005-05-16 | 대우조선해양 주식회사 | A system of management for B.O.G in LNG carrier |
| JP2004330831A (en) * | 2003-05-02 | 2004-11-25 | Nobuhiko Hatakeyama | Ship with refrigeration storage means |
| FR2879720B1 (en) * | 2004-12-17 | 2007-04-06 | Snecma Moteurs Sa | COMPRESSION-EVAPORATION SYSTEM FOR LIQUEFIED GAS |
| US8196413B2 (en) * | 2005-03-30 | 2012-06-12 | Fluor Technologies Corporation | Configurations and methods for thermal integration of LNG regasification and power plants |
-
2010
- 2010-01-28 KR KR1020100007662A patent/KR101121721B1/en active IP Right Grant
- 2010-12-20 WO PCT/KR2010/009102 patent/WO2011093591A2/en active Application Filing
-
2011
- 2011-01-11 JP JP2011002717A patent/JP5183756B2/en not_active Expired - Fee Related
- 2011-01-13 NO NO20110059A patent/NO20110059A1/en not_active Application Discontinuation
- 2011-01-14 SG SG2011002540A patent/SG173272A1/en unknown
- 2011-01-18 CN CN201110020941.8A patent/CN102192401B/en not_active Expired - Fee Related
- 2011-01-27 BR BRPI1100658-7A patent/BRPI1100658A2/en not_active IP Right Cessation
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5833594A (en) * | 1981-08-20 | 1983-02-26 | Mitsubishi Heavy Ind Ltd | Compound energy conservation type equipment for liquefied-gas ship |
| JPH05113108A (en) * | 1991-10-23 | 1993-05-07 | Osaka Gas Co Ltd | Cold heat power generator utilizing liquefied natural gas |
| CN1852832A (en) * | 2003-09-19 | 2006-10-25 | 信号系泊浮筒公司 | Gas offloading system |
| WO2005091932A2 (en) * | 2004-03-04 | 2005-10-06 | Single Buoy Moorings, Inc. | Floating power generation system |
| CN101057101A (en) * | 2004-11-08 | 2007-10-17 | 国际壳牌研究有限公司 | Liquefied natural gas floating storage regasification unit |
| CN101305238A (en) * | 2005-12-22 | 2008-11-12 | 单浮筒系泊公司 | Enhanced lng regas |
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103225740A (en) * | 2013-04-22 | 2013-07-31 | 中国海洋石油总公司 | BOG processing system utilizing pressure energy of LNG receiving station |
| CN103225739A (en) * | 2013-04-22 | 2013-07-31 | 中国海洋石油总公司 | Energy-saving processing system for vapor of LNG receiving station |
| CN103225739B (en) * | 2013-04-22 | 2015-09-09 | 中国海洋石油总公司 | A kind of LNG receiving station boil-off gas energy-efficient treatment system |
| CN103225740B (en) * | 2013-04-22 | 2015-09-09 | 中国海洋石油总公司 | A kind of LNG receiving station utilizes the BOG processing system of pressure energy |
| CN104315339A (en) * | 2014-10-27 | 2015-01-28 | 中国海洋石油总公司 | LNG stepped regasification system applied to marine floating type LNG regasification device and regasification method |
| CN113022792A (en) * | 2016-04-07 | 2021-06-25 | 现代重工业株式会社 | Ship with gas regasification system |
| CN109424341A (en) * | 2017-09-05 | 2019-03-05 | 斗山重工业建设有限公司 | Use the system of the carbon dioxide in the exhaust gas by the cold and hot collection of liquefied natural gas |
| CN109578806A (en) * | 2018-12-07 | 2019-04-05 | 江苏中圣压力容器装备制造有限公司 | A kind of process unit of LNG flash steam (BOG) pressurization condensing recovery |
| CN109578806B (en) * | 2018-12-07 | 2024-01-23 | 江苏中圣压力容器装备制造有限公司 | LNG flash evaporation vapour (BOG) supercharging condensation recovery process device |
| CN109760783A (en) * | 2019-01-25 | 2019-05-17 | 太平洋海洋工程（舟山）有限公司 | A kind of ventilative mast suitable for FSRU |
Also Published As
| Publication number | Publication date |
|---|---|
| NO20110059A1 (en) | 2011-07-29 |
| SG173272A1 (en) | 2011-08-29 |
| BRPI1100658A2 (en) | 2013-04-30 |
| WO2011093591A3 (en) | 2011-11-10 |
| WO2011093591A2 (en) | 2011-08-04 |
| KR20110087970A (en) | 2011-08-03 |
| JP2011158089A (en) | 2011-08-18 |
| CN102192401B (en) | 2014-07-09 |
| KR101121721B1 (en) | 2012-02-28 |
| JP5183756B2 (en) | 2013-04-17 |
| WO2011093591A4 (en) | 2012-01-05 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN102192401B (en) | Floating LNG revaporization equipment | |
| CN102648123B (en) | For supplying the ship of liquefaction gas | |
| US6907735B2 (en) | Hydrogen fueled electrical generator system and method thereof | |
| KR102197284B1 (en) | Power generation system | |
| JP2009203860A (en) | Prime mover system | |
| KR101232311B1 (en) | Waster heat recovery system with the exhaust gas from the gas combustion unit | |
| KR101537274B1 (en) | Floating and storage gas power plant and high power apparatus of the power plant | |
| CN102428311A (en) | Plant for re-gasification of liquefied natural gas and liquefied petroleum gas in combination with production of electric power | |
| CN109026235A (en) | A kind of cold energy generation system for liquefied natural gas floating storage regasification plant | |
| KR101911119B1 (en) | Fuel Cell Combination Hybrid System | |
| KR101419009B1 (en) | Lng regasification apparatus having combined cycle power plant | |
| CN104359003B (en) | Liquefied natural gas self power generation open type gasification system | |
| KR20110130050A (en) | Eco regasification apparatus and method | |
| KR20160017730A (en) | Supercritical Carbon Dioxide Power Generation System | |
| KR102252653B1 (en) | Hydrogen Fuel Cell Complex Power Plant Equipped with the Floating LNG Power Plant and Hydrogen Generation System and Method for Thereof | |
| JP2020513513A (en) | A prime mover heat pump for low temperature use and cooling fluids | |
| KR20160017731A (en) | Supercritical Carbon Dioxide Power Generation System | |
| KR200435144Y1 (en) | Energy recovery apparatus in LNG supply system | |
| KR20160031662A (en) | Floating lng re-gasification power plant using boil off gas as fuel | |
| JP6651826B2 (en) | Hydrogen utilization system and method | |
| KR101371253B1 (en) | A combined system of lng regasification and power generation | |
| KR20230083997A (en) | floating installation for treating CO2 and CO2 treatment system having the same | |
| KR101259951B1 (en) | Waste heat supply system and ship with the system | |
| KR20140147073A (en) | Marine LNG storage and combined cycle power generating unit | |
| KR101744793B1 (en) | Power generating system using boil off gas |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20140709 Termination date: 20190118 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |