EP3685094A1 - Lng wiedervergasung - Google Patents
Lng wiedervergasungInfo
- Publication number
- EP3685094A1 EP3685094A1 EP18769104.3A EP18769104A EP3685094A1 EP 3685094 A1 EP3685094 A1 EP 3685094A1 EP 18769104 A EP18769104 A EP 18769104A EP 3685094 A1 EP3685094 A1 EP 3685094A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- heat exchanger
- heat
- fluid
- heated
- liquefied gas
- 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
- 239000012530 fluid Substances 0.000 claims abstract description 55
- 239000007789 gas Substances 0.000 claims abstract description 51
- 238000000034 method Methods 0.000 claims abstract description 24
- 239000002918 waste heat Substances 0.000 claims abstract description 11
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 22
- 239000003949 liquefied natural gas Substances 0.000 claims description 19
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims description 14
- 229910052757 nitrogen Inorganic materials 0.000 claims description 11
- 238000001704 evaporation Methods 0.000 claims description 7
- 239000003345 natural gas Substances 0.000 claims description 7
- 230000008020 evaporation Effects 0.000 claims description 6
- 238000004172 nitrogen cycle Methods 0.000 claims description 4
- 238000002485 combustion reaction Methods 0.000 claims description 3
- 108090000623 proteins and genes Proteins 0.000 claims 1
- 238000011084 recovery Methods 0.000 abstract description 6
- 239000000446 fuel Substances 0.000 description 6
- 238000001816 cooling Methods 0.000 description 4
- 239000003570 air Substances 0.000 description 3
- 239000013535 sea water Substances 0.000 description 3
- 241000196324 Embryophyta Species 0.000 description 2
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 2
- 239000012080 ambient air Substances 0.000 description 2
- 239000000498 cooling water Substances 0.000 description 2
- 230000008016 vaporization Effects 0.000 description 2
- 235000008694 Humulus lupulus Nutrition 0.000 description 1
- 244000025221 Humulus lupulus Species 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 230000008878 coupling Effects 0.000 description 1
- 238000010168 coupling process Methods 0.000 description 1
- 238000005859 coupling reaction Methods 0.000 description 1
- 238000006073 displacement reaction Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000008014 freezing Effects 0.000 description 1
- 238000007710 freezing Methods 0.000 description 1
- 239000002737 fuel gas Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- WGCNASOHLSPBMP-UHFFFAOYSA-N hydroxyacetaldehyde Natural products OCC=O WGCNASOHLSPBMP-UHFFFAOYSA-N 0.000 description 1
- 230000010354 integration Effects 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 230000008092 positive effect Effects 0.000 description 1
- 238000010248 power generation Methods 0.000 description 1
- 238000005057 refrigeration Methods 0.000 description 1
- 230000008023 solidification Effects 0.000 description 1
- 238000007711 solidification Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000011144 upstream manufacturing Methods 0.000 description 1
- 238000009834 vaporization Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
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
- 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
- F17C9/04—Recovery of thermal energy
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
- F25J3/02—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
- F25J3/0204—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream characterised by the feed stream
- F25J3/0209—Natural gas or substitute natural gas
- F25J3/0214—Liquefied natural 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
- F17C2221/00—Handled fluid, in particular type of fluid
- F17C2221/01—Pure fluids
- F17C2221/011—Oxygen
-
- 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
- F17C2227/00—Transfer of fluids, i.e. method or means for transferring the fluid; Heat exchange with the fluid
- F17C2227/01—Propulsion of the fluid
- F17C2227/0128—Propulsion of the fluid with pumps or compressors
- F17C2227/0135—Pumps
-
- 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
- F17C2227/01—Propulsion of the fluid
- F17C2227/0128—Propulsion of the fluid with pumps or compressors
- F17C2227/0157—Compressors
-
- 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
- F17C2227/0337—Heat exchange with the fluid by cooling
- F17C2227/0341—Heat exchange with the fluid by cooling using another fluid
- F17C2227/0355—Heat exchange with the fluid by cooling using another fluid in a closed loop
-
- 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
- F17C2265/00—Effects achieved by gas storage or gas handling
- F17C2265/07—Generating electrical power as side effect
-
- 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
- F17C2270/05—Applications for industrial use
- F17C2270/0581—Power plants
Definitions
- the liquefied natural gas is regasified before being discharged into a gas network.
- the liquid natural gas is typically evaporated with ambient heat (air / seawater) or chemical heat.
- US 2009/0211263 A1 discloses an apparatus and method in which a liquid natural gas stream is vaporized.
- the object of the invention is to provide an energetically and comparatively cost-effective evaporation process for a cryogenic liquefied gas. Furthermore, it is an object of the invention to provide a correspondingly improved device.
- the invention solves the task directed to a device by providing that in such a device for generating electrical energy and for vaporizing a cryogenic liquefied gas comprising a line for the cryogenic liquefied gas, a pump disposed in the line, a heat engine , as well as one of the thermal power
- the branching line branches off into the heat engine and the device further comprises a fluid circuit in which the following components are arranged one behind the other in the direction of flow of the fluid:
- a first heat exchanger which is also connected in the flow direction of the cryogenic liquefied gas behind the pump in the line,
- Refrigerated liquefied gas means that the gas has been liquefied by cooling down.
- the temperatures are in the relevant to the invention gases in the order of -140 ° C and below.
- the fluid circuit should be operated as a 1-pressure process to optimize the efficiency of the device. For this purpose, in addition to a certain temperature, a match of the pressure provided by the compressor is required.
- the fluid is heated by means of ambient heat.
- a gas turbine is used as the heat engine, a possible application would be the gas turbine intake air cooling, which results in a power increase of the gas turbine.
- other heat sources can be used ver, such as heated cooling water, sea water, ambient air is also in question.
- the third heat exchanger cleverly displaces heat within the fluid circuit.
- the fluid heated in the waste heat utilization system can be relaxed in a work-free manner.
- a generator is coupled to the expansion machine.
- a fourth heat exchanger with a first side in the fluid circuit arranged.
- This fourth heat exchanger is fer ner with a second side in the flow direction of the fluid to the second side of the third heat exchanger in the fluid circuit arranged.
- the fluid supplied to the waste heat recovery system should not fall below a certain temperature. Preheating by the fourth heat exchanger would ensure this.
- a waiver of the fourth heat exchanger and the Hinneh men a comparatively early repair of the cold part of Abhitze verseungssystems could also better use of the heat in Abhitze contractsssystem cause.
- a fifth heat exchanger in the branch line and in the fluid circuit is arranged in front of the second side of the third heat exchanger to preheat the fuel for combustion in the heat engine.
- a sixth heat exchanger is arranged in the line before a branch of the branch line.
- this sixth heat exchanger heat from the environment is to be used to further heat the regasified gas. It makes sense, if this is not the case after the branch happens, but before that in the actual fuel gas preheating in the fifth heat exchanger less heat the system, ie the fluid circuit, must be removed to achieve a desired temperature level.
- the claimed device can be used for various cryogenic liquefied gases.
- the cryogenic liquefied gas is natural gas, alone in Hin look at its usability in the heat engine, but also in terms of the choice of fluid in the fluid circuit and the efficiency of the overall system.
- An alternative to natural gas is, for example, hydrogen.
- the fluid circuit is a nitrogen cycle.
- the use of nitrogen is advantageous.
- nitrogen with a critical point of -147 ° C / 34 bara is excellently suited for supercritical heat exchange with the LNG.
- the supercritical state prevents the formation of an isothermal condensation plateau.
- the exergetic losses in the heat transfer mini mized Furthermore, the solidification temperature of -210 ° C is well below the LNG temperature of -162 ° C, so that a freezing of the fluid is not possible.
- the object directed to a method is achieved by a method for generating electrical energy and Ver evaporation of a cryogenic liquefied gas in which a cryogenic liquefied gas is compressed and heated in a first heat exchanger with a fluid stream and evaporated, the fluid flow in a circle is, wherein it is compressed after the first heat exchanger, in a second heat exchanger absorbs heat, is divided into a first and a second partial flow, the first partial flow is heated at least in a Abhitze dividedungssystem with Abga sen a heat engine and the second partial flow in a third Heat exchanger is heated and first and second partial flow are brought together again, the merged fluid is expanded and then heated in the third heat exchanger, the second partial flow before it heats the cryogenic liquefied gas in the first heat exchanger.
- the first partial flow, before it is heated in the heat utilization system from Ab, in a fourth heat exchanger through the fluid is heated after this has heated the second partial flow in the third heat exchanger.
- the connection of the second sides of third and four heat exchangers to one another compared to a common preheating of the entire fluid flow makes sense, since the first partial flow is in any case supplied to a comparatively strong heating in the waste heat utilization system and too much "preheating" of the fluid occurs would have an overall negative impact on the efficiency of the entire system, if due to a relatively high inlet temperature of the fluid in the area of entry into the Abhitze stressedungssystem a comparatively large amount of heat would have to be discharged unused into the environment.
- the previously deeply cold ver liquid gas is at least partially supplied to a gas network and part of the heat engine.
- the heat engine supplied, formerly cryogenic liquefied gas through the fluid id, before it heats the second partial flow in the third heat exchanger, is preheated in a fifth heat exchanger for a combus- tion.
- the fluid circuit is a supercritically operated circuit.
- the heat of vaporization no longer plays a role, which has a positive effect on efficient heat transfer.
- liquefied natural gas is used as the cryogenic liquefied gas.
- the regasification preferably LNG
- the recycle process preferably nitrogen
- the LNG be set at the terminal point to the gas network to the ge desired pressure and temperature level.
- the design of the fluid circuit is optimally adapted to the requirements of the subsystems (e.g., the internal heat displacement allows both the final LNG temperature and a minimum nitrogen temperature at the entrance to the waste heat recovery system downstream of the gas turbine).
- FIG. 1 shows a device for generating electrical energy and for the evaporation of liquefied natural gas according to the inven tion.
- FIG. 1 shows schematically and by way of example a device 1 according to the invention. It comprises a line 2 for the cryogenic liquefied gas, such as natural gas, and ei ne arranged in the line 2 pump 3. Further, the device 1 of Figure 1 comprises a gas turbine engine as 4 Wärekraftma, as well as a heat engine 4 downstream Abhitzecesssystem 5 similar to one Heat recovery steam generator for gas and steam turbine plants. However, the invention does not provide for a water-steam cycle.
- the fluid circuit 6 could be, for example, a nitrogen cycle and comprises in the embodiment of Figure 1 in the flow direction of the fluid behind the following components:
- a first heat exchanger 7 which is also connected in the flow direction of the cryogenic liquefied gas behind the pump 3 in the line 2; in the first heat exchanger 7, heat is transferred, for example, from nitrogen to the liquefied natural gas, whereby the liquefied natural gas heats up and evaporates, a compressor 8 with which the fluid / nitrogen can be brought into the supercritical pressure range for optimum heat exchange,
- a second heat exchanger 9 in which ambient heat (for example from a gas turbine intake air cooling, seawater, ambient air, warmed-up cooling water) is used to heat the fluid,
- ambient heat for example from a gas turbine intake air cooling, seawater, ambient air, warmed-up cooling water
- a portion of the expanded natural gas is in the embodiment of Figure 1 a gas network 24 and another part of Gastur bine (heat engine 4) supplied.
- a gas network 24 and another part of Gastur bine (heat engine 4) supplied For this purpose branches off at branch 21, a branch line 18 from the line 2 from.
- the branch line 18 opens into the gas turbine (heat engine 4).
- a sixth heat exchanger 20 is further arranged in the line 2 in front of a branch 21 of the branch line 18.
- the turbine 13, in which nitrogen is expanded in the embodiment of FIG. 1, has leaks. These can be sucked off at least partially and then into the fluid circuit 6 are recycled. Generally, a feed 26 of nitrogen into the fluid circuit 6 is provided.
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Filling Or Discharging Of Gas Storage Vessels (AREA)
- Engine Equipment That Uses Special Cycles (AREA)
Abstract
Description
Claims
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP18157209.0A EP3527869A1 (de) | 2018-02-16 | 2018-02-16 | Lng wiedervergasung |
PCT/EP2018/073712 WO2019158230A1 (de) | 2018-02-16 | 2018-09-04 | Lng wiedervergasung |
Publications (2)
Publication Number | Publication Date |
---|---|
EP3685094A1 true EP3685094A1 (de) | 2020-07-29 |
EP3685094B1 EP3685094B1 (de) | 2021-10-27 |
Family
ID=61244410
Family Applications (2)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP18157209.0A Withdrawn EP3527869A1 (de) | 2018-02-16 | 2018-02-16 | Lng wiedervergasung |
EP18769104.3A Active EP3685094B1 (de) | 2018-02-16 | 2018-09-04 | Lng wiedervergasung |
Family Applications Before (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP18157209.0A Withdrawn EP3527869A1 (de) | 2018-02-16 | 2018-02-16 | Lng wiedervergasung |
Country Status (7)
Country | Link |
---|---|
US (1) | US11274795B2 (de) |
EP (2) | EP3527869A1 (de) |
JP (1) | JP7080324B2 (de) |
KR (1) | KR102405754B1 (de) |
CN (1) | CN111727342A (de) |
ES (1) | ES2902937T3 (de) |
WO (1) | WO2019158230A1 (de) |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US11493175B2 (en) * | 2019-12-31 | 2022-11-08 | L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude | Method for filling tanks of hydrogen-fueled vehicles |
EP3945239B1 (de) * | 2020-07-27 | 2022-09-14 | Efficiency for LNG Applications, S.L. | System und verfahren zur rückgewinnung von kälte aus einer regasifizierungsanlage für flüssigerdgas |
CN114659023A (zh) * | 2022-03-30 | 2022-06-24 | 成都天储动力设备集团有限公司 | 一种液化气体储能系统 |
Family Cites Families (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0009387A1 (de) * | 1978-09-18 | 1980-04-02 | Fluor Corporation | Verfahren zur Energiegewinnung während der Wiederverdampfung verflüssigter Gase |
DE4025023A1 (de) * | 1990-08-07 | 1992-02-13 | Linde Ag | Verfahren zum verdampfen von fluessigem erdgas |
JPH09138063A (ja) * | 1995-11-14 | 1997-05-27 | Osaka Gas Co Ltd | 液化天然ガス冷熱利用の空気分離方法および設備 |
JPH10288047A (ja) | 1997-04-16 | 1998-10-27 | Osaka Gas Co Ltd | 液化天然ガス気化発電装置 |
JP2003056312A (ja) * | 2001-08-09 | 2003-02-26 | Kobe Steel Ltd | 閉サイクルガスタービンおよび同ガスタービンを用いた発電システム |
US7028481B1 (en) * | 2003-10-14 | 2006-04-18 | Sandia Corporation | High efficiency Brayton cycles using LNG |
US20080178611A1 (en) * | 2007-01-30 | 2008-07-31 | Foster Wheeler Usa Corporation | Ecological Liquefied Natural Gas (LNG) Vaporizer System |
US8973398B2 (en) * | 2008-02-27 | 2015-03-10 | Kellogg Brown & Root Llc | Apparatus and method for regasification of liquefied natural gas |
JP2009203860A (ja) * | 2008-02-27 | 2009-09-10 | Takeo Tomota | 原動機システム |
US8950196B2 (en) * | 2008-07-17 | 2015-02-10 | Fluor Technologies Corporation | Configurations and methods for waste heat recovery and ambient air vaporizers in LNG regasification |
US8132411B2 (en) * | 2008-11-06 | 2012-03-13 | Air Products And Chemicals, Inc. | Rankine cycle for LNG vaporization/power generation process |
US20110289941A1 (en) * | 2010-05-28 | 2011-12-01 | General Electric Company | Brayton cycle regasification of liquiefied natural gas |
JP2014218922A (ja) | 2013-05-07 | 2014-11-20 | 日立造船株式会社 | 原動機システム |
-
2018
- 2018-02-16 EP EP18157209.0A patent/EP3527869A1/de not_active Withdrawn
- 2018-09-04 KR KR1020207026295A patent/KR102405754B1/ko active IP Right Grant
- 2018-09-04 ES ES18769104T patent/ES2902937T3/es active Active
- 2018-09-04 EP EP18769104.3A patent/EP3685094B1/de active Active
- 2018-09-04 JP JP2020531757A patent/JP7080324B2/ja active Active
- 2018-09-04 CN CN201880089284.2A patent/CN111727342A/zh active Pending
- 2018-09-04 WO PCT/EP2018/073712 patent/WO2019158230A1/de unknown
- 2018-09-04 US US16/767,622 patent/US11274795B2/en active Active
Also Published As
Publication number | Publication date |
---|---|
EP3527869A1 (de) | 2019-08-21 |
KR102405754B1 (ko) | 2022-06-08 |
ES2902937T3 (es) | 2022-03-30 |
US11274795B2 (en) | 2022-03-15 |
JP2021509940A (ja) | 2021-04-08 |
BR112020010611A2 (pt) | 2020-11-10 |
BR112020010611A8 (pt) | 2022-10-04 |
US20200393085A1 (en) | 2020-12-17 |
JP7080324B2 (ja) | 2022-06-03 |
CN111727342A (zh) | 2020-09-29 |
WO2019158230A1 (de) | 2019-08-22 |
EP3685094B1 (de) | 2021-10-27 |
KR20200120940A (ko) | 2020-10-22 |
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