WO2016097461A1 - Lng tank - Google Patents

Lng tank Download PDF

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Publication number
WO2016097461A1
WO2016097461A1 PCT/FI2014/051012 FI2014051012W WO2016097461A1 WO 2016097461 A1 WO2016097461 A1 WO 2016097461A1 FI 2014051012 W FI2014051012 W FI 2014051012W WO 2016097461 A1 WO2016097461 A1 WO 2016097461A1
Authority
WO
WIPO (PCT)
Prior art keywords
lng tank
metal shell
lng
tank
vacuum
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Ceased
Application number
PCT/FI2014/051012
Other languages
French (fr)
Inventor
Viktor BERGMAN
Mathias Jansson
Martin RÅHOLM
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.)
Wartsila Finland Oy
Original Assignee
Wartsila Finland Oy
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 Wartsila Finland Oy filed Critical Wartsila Finland Oy
Priority to PCT/FI2014/051012 priority Critical patent/WO2016097461A1/en
Publication of WO2016097461A1 publication Critical patent/WO2016097461A1/en
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

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Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS 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
    • F17C3/00Vessels not under pressure
    • F17C3/02Vessels not under pressure with provision for thermal insulation
    • F17C3/025Bulk storage in barges or on ships
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS 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
    • F17C3/00Vessels not under pressure
    • F17C3/02Vessels not under pressure with provision for thermal insulation
    • F17C3/04Vessels not under pressure with provision for thermal insulation by insulating layers
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS 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
    • F17C2201/00Vessel construction, in particular geometry, arrangement or size
    • F17C2201/01Shape
    • F17C2201/0104Shape cylindrical
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS 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
    • F17C2201/00Vessel construction, in particular geometry, arrangement or size
    • F17C2201/03Orientation
    • F17C2201/035Orientation with substantially horizontal main axis
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS 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
    • F17C2201/00Vessel construction, in particular geometry, arrangement or size
    • F17C2201/05Size
    • F17C2201/054Size medium (>1 m3)
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS 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
    • F17C2203/00Vessel construction, in particular walls or details thereof
    • F17C2203/03Thermal insulations
    • F17C2203/0304Thermal insulations by solid means
    • F17C2203/0329Foam
    • F17C2203/0333Polyurethane
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS 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
    • F17C2203/00Vessel construction, in particular walls or details thereof
    • F17C2203/03Thermal insulations
    • F17C2203/0304Thermal insulations by solid means
    • F17C2203/0337Granular
    • F17C2203/0341Perlite
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS 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
    • F17C2203/00Vessel construction, in particular walls or details thereof
    • F17C2203/03Thermal insulations
    • F17C2203/0391Thermal insulations by vacuum
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS 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
    • F17C2203/00Vessel construction, in particular walls or details thereof
    • F17C2203/06Materials for walls or layers thereof; Properties or structures of walls or their materials
    • F17C2203/0602Wall structures; Special features thereof
    • F17C2203/0607Coatings
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS 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
    • F17C2203/00Vessel construction, in particular walls or details thereof
    • F17C2203/06Materials for walls or layers thereof; Properties or structures of walls or their materials
    • F17C2203/0602Wall structures; Special features thereof
    • F17C2203/0612Wall structures
    • F17C2203/0626Multiple walls
    • F17C2203/0629Two walls
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS 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
    • F17C2203/00Vessel construction, in particular walls or details thereof
    • F17C2203/06Materials for walls or layers thereof; Properties or structures of walls or their materials
    • F17C2203/0634Materials for walls or layers thereof
    • F17C2203/0636Metals
    • F17C2203/0639Steels
    • F17C2203/0643Stainless steels
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS 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
    • F17C2205/00Vessel construction, in particular mounting arrangements, attachments or identifications means
    • F17C2205/01Mounting arrangements
    • F17C2205/0153Details of mounting arrangements
    • F17C2205/018Supporting feet
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS 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
    • F17C2209/00Vessel construction, in particular methods of manufacturing
    • F17C2209/22Assembling processes
    • F17C2209/225Spraying
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS 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
    • F17C2209/00Vessel construction, in particular methods of manufacturing
    • F17C2209/22Assembling processes
    • F17C2209/227Assembling processes by adhesive means
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS 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
    • F17C2221/00Handled fluid, in particular type of fluid
    • F17C2221/03Mixtures
    • F17C2221/032Hydrocarbons
    • F17C2221/033Methane, e.g. natural gas, CNG, LNG, GNL, GNC, PLNG
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS 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
    • F17C2221/00Handled fluid, in particular type of fluid
    • F17C2221/03Mixtures
    • F17C2221/032Hydrocarbons
    • F17C2221/035Propane butane, e.g. LPG, GPL
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS 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
    • F17C2223/00Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel
    • F17C2223/01Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel characterised by the phase
    • F17C2223/0146Two-phase
    • F17C2223/0153Liquefied gas, e.g. LPG, GPL
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS 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
    • F17C2223/00Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel
    • F17C2223/01Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel characterised by the phase
    • F17C2223/0146Two-phase
    • F17C2223/0153Liquefied gas, e.g. LPG, GPL
    • F17C2223/0161Liquefied gas, e.g. LPG, GPL cryogenic, e.g. LNG, GNL, PLNG
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS 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
    • F17C2223/00Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel
    • F17C2223/03Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel characterised by the pressure level
    • F17C2223/033Small pressure, e.g. for liquefied gas
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS 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
    • F17C2260/00Purposes of gas storage and gas handling
    • F17C2260/03Dealing with losses
    • F17C2260/031Dealing with losses due to heat transfer
    • F17C2260/033Dealing with losses due to heat transfer by enhancing insulation
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS 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
    • F17C2270/00Applications
    • F17C2270/01Applications for fluid transport or storage
    • F17C2270/0102Applications for fluid transport or storage on or in the water
    • F17C2270/0105Ships

Definitions

  • the invention is in general related to the field of storing liquid fuel, in particular liquefied natural gas (LNG), as a marine fuel in one or more engines of a ship or of a corresponding sea-going vessel.
  • LNG liquefied natural gas
  • the invention is related to LNG tanks and connecting pipes to an LNG tank. More particularly the invention relates to the LNG tank according to the preamble of the independent LNG tank claim.
  • Liquid fuels that are used as marine fuels are typically liquefied natural gas, liquefied petroleum gas or liquid petroleum gas (LPG), methanol, ethylene.
  • Natural gas is in gaseous form in room temperature. In ships that use natural gas as fuel, the natural gas is typically stored onboard in liquid form, and thus this marine fuel is commonly called by its acronym LNG (Liquefied Natural Gas). Natural gas can be kept in liquid form by maintaining its temperature be- low a boiling point, which is approximately -163 °C.
  • LNG system onboard comprises typically a bunkering station, which is the ship's connection with a LNG terminal on shore or with an LNG bunkering barge, insulated pipes for leading LNG to an LNG tank, which is for storage of LNG and a tank connection space where LNG is controllably evaporated and its distribution to the en- gine(s) is arranged.
  • LNG tank is a cylindrical, double-walled or single- walled, insulated stainless steel tank.
  • the LNG tank is usually the most expensive item in the LNG fuel handling system, taking up even 50-60% of the total cost of the system.
  • double-walled structure is typically used, with a vacuum generated between the shells for heat insulation with possible perlite insulation.
  • the inner wall is stainless steel and the outer wall can be either stainless steel or carbon steel.
  • a tank room or a tank connection space is associated with a storage tank and contains the equipment to convert the liquid into a gas for safe delivery to the engines.
  • the tank room is also considered a 'secondary barrier' in case there should be leakage of the LNG, since liquid pipes and valves are inside it.
  • an LNG tank having an inner shell of stainless steel and an outer shell spaced at a distance from the inner shell, the said inner and outer shells defining an isolation space there between.
  • the tank consists of a stainless steel inner shell, which is de- signed for an internal pressure, and an outer shell that acts as a secondary barrier.
  • the outer shell can be made of either stainless steel or nickel steel.
  • the tank is insulated with perlite/vacuum.
  • Natural gas is a safe fuel when the right precautions are taken. Neither is LNG in a liquid state explosive, corrosive or toxic. Thus, possible spillages will not cause any lasting contamination, as the liquid will evaporate as gas.
  • a marine vessel refers to a ship, or other floating structure, such as an off-shore structure.
  • One important problem to be solved relates to the scenario of loss of vacuum in double shelled storage tanks.
  • loss of vacuum the insulation properties will be significantly reduced, which causes the temperature of the outer shell to drastically decrease.
  • a reduced temperature on the outer shell will conduct coldness to the surrounding walls of a tank hold space and to other surrounding structures of the marine vessel.
  • a tank hold refers to a compartment inside the marine vessel hull that surrounds the LNG tank and the tank connection space.
  • the surrounding structures are not constructed of a cold resistant material such as stainless steel, which is expensive, the problem is to be solved so that the temperature of the surrounding structures will not reach the temperature limitations of the material.
  • the leakage scenario shall be calculated with a -163°C outer shell temperature.
  • Another object of the invention is to prevent any leakage and cold temperatures related problems in connection with an LNG tank.
  • Another object of the invention is to create a double-shell LNG tank with more LNG space within a certain space.
  • the LNG tank located in a tank hold space of a marine vessel comprises a inner metal shell, an outer metal shell and an isolation space between the shells containing vacuum, where in the LNG tank further comprises an insulation material adhered on the outer surface of the outer metal shell.
  • the insulation material adhered on the outer surface of the outer metal shell substantially covers the outer surface of the outer shell of the LNG tank.
  • the insulation material adhered on the outer surface of the outer metal shell is polyurethane (PUR) or other corresponding onto the outer surface of the outer shell of the LNG tank sprayed insulating foam.
  • thermal conductivity (NPT) of the PUR is: below 0.2 W/m * k and density is 1 10- 130 kg/m3.
  • the insulation material adhered on the outer surface of the outer metal shell is formed of at least one insulation panel, advantageously several insulation panels, substantially covering the outer surface of the outer shell of the LNG tank.
  • the insulation material adhered on the outer surface of the outer metal shell is formed of several insulation panels forming a substantially continuous insulation material layer onto the outer surface of the outer shell of the LNG tank.
  • the insulation material adhered on the outer surface of the outer metal shell comprises at least one insulation panel and polyurethane (PUR) or other corresponding onto the outer surface of the outer shell of the LNG tank sprayed insulating foam.
  • PUR polyurethane
  • the isolation space between the inner metal shell and the outer metal shell containing vacuum is perlite filled.
  • the inner metal shell is stainless steel and the outer metal shell is stainless steel.
  • the insulation panels are vacuum insulated panels (VIP) comprising vacuum inside a reflective layer.
  • VI Ps vacuum insulated panels
  • the VI Ps can be of different shapes and are mounted on the outside of the outer shell.
  • Advantageously thermal conductivity (NPT) of the VIPS is: below 0.0023 W/m * k and density is 270 - 290 kg/m3.
  • NPT thermal conductivity
  • the isolation space between the tank shells is 250 - 350 mm thick, and comprises vacuum filled with perlite.
  • the insulation thickness of the insulation material formed of vacuum insulated panels adhered on the outer surface of the outer shell of the LNG tank is 30-70 mm.
  • surrounding structures of the LNG tank comprise at least one wall or floor of a tank connection space i.e. a tank room and the material of the surrounding structure is DNV grade A steel (NV A steel).
  • a marine vessel comprises an LNG tank according to the invention.
  • the LNG tank comprises the insulation of the outer shell surface, in the case of loss or reduction of vacuum from the isolation space between the shells of the LNG tank, the insulation prevents the reduced temperature on the outer shell to conduct coldness to the surrounding structures and thus the temperatures of the surrounding structures remain within the temperature limi- tations of the material even in the worst case scenario with a -163°C outer shell temperature of the LNG tank.
  • the insulation of the outer shell surface of the LNG tank also reduces the requirement of the distance between the shells as the outer insulation decreases capacity needed of the isolation space between the shells.
  • the insulation of the outer shell surface of the LNG tank also makes it possible to reduce the distance from the outer surface of the tank to the walls of the tank room due to the improved insulation achieved by the insulation of the outer shell surface.
  • Fig. 1 shows schematically a prior art LNG fuel distribution architecture and Figs 2 - 3 show schematically an advantageous example of the invention.
  • Fig. 1 illustrates schematically the architecture of a known system onboard an LNG-fuelled ship.
  • An LNG bunkering station 101 is located on the deck and used to fill up the system with LNG.
  • the LNG fuel storage system comprises one or more thermally insulated gas tanks 102 for storing the LNG in liquid form, and the so-called tank room 103 where the LNG is controllably evapo- rated and its distribution to the engine(s) is arranged.
  • the LNG tank 102 and the tank room 103 are located in a tank hold space 16 of a marine vessel.
  • Evaporation means a phase change from liquid to gaseous phase, for which reason all subsequent stages should leave the L for liquefied out of the acronym and use only NG (Natural Gas) instead.
  • the engine 104 or engines of the ship are located in an engine room 105. Each engine has its respective engine-specific fuel input subsystem 106, which in the case of gaseous fuel is in some sources referred to as the GVU (Gas Valve Unit).
  • the tank room 103 of fig. 1 comprises two evaporators, of which the first evaporator 107 is the so-called PBU (Pressure Build-Up) evapo- rator used to maintain a sufficient pressure inside the gas tank 102.
  • PBU Pressure Build-Up
  • Hydrostatic pressure at the inlet of a main supply line 108 inside the gas tank 102 is the driving force that makes the LNG flow into the second evaporator 109, which is the MGE or Main Gas Evaporator from which the fuel is distributed in gaseous form towards the engines.
  • the PBU system maintains the internal pressure of the gas tank 102 at or close to a predetermined value, which is typically between 5 and 7 bars.
  • the engine 104 comprises one or more cooling circuits. Schematically shown in fig. 1 is an external loop 1 10 of the so-called low temperature (LT) cooling circuit, which may be used for example to cool lubricating oil.
  • LT low temperature
  • the so-called LT water that circulates in the external loop 1 10 may have a temperature around 50 degrees centigrade when it goes through a heat exchanger 1 1 1 , in which it donates heat to a mixture of glycol and water that in turn transfers heat to the evaporators 107 and 109.
  • the glycol / water mixture circuit comprises a circulation pump 1 12 and an expansion tank 1 13. Glycol is needed in the mixture to prevent it from freezing when it comes into contact with the extremely cold LNG inlet parts of the evaporators 107 and 109.
  • the LNG tank 10 is a double-shell LNG tank and comprises an inner shell 1 1 defining the tank space for the LNG and an outer shell 12.
  • the level of the LNG is denoted by reference sign L.
  • the isolation space 13 is located between the inner shell 1 1 and the outer shell 12 .
  • insulation material 15 is adhered on the outer surface 14 of the outer shell 12 .
  • the insulation material 15 is advanta- geously VIP (vacuum insulated panels) and/or PUR (polyurethane).
  • the insulation material 15 adhered on the outer surface 14 of the outer metal shell 12 substantially covers the outer surface 14 of the outer shell 12 of the LNG tank 10.
  • the isolation space 13 between the inner metal shell 1 1 and the outer metal shell 12 advantageously contains vacuum.
  • the isolation space 13 is ad- vantageously perlite filled and it comprises 250 - 350 mm perlite.
  • the insula- tion thickness of the insulation material 15 in case formed of vacuum insulated panels adhered on the outer surface 14 of the outer shell 12 of the LNG tank 10 is 30-70 mm.
  • the deck 18 below the LNG tank 10 located in a tank connection space i.e. a tank room is typically DNV grade A steel (NV A steel).

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

Abstract

The invention relates to an LNG tank (10) located in a tank hold space (16) of a marine vessel comprising an inner metal shell (11), an outer metal shell (12) and an isolation space (13) between the shells (11, 12) advantageously con- taining vacuum, which LNG tank (10) further comprises an insulation material (15) adhered on outer surface (14) of the outer metal shell (12).

Description

LNG tank
The invention is in general related to the field of storing liquid fuel, in particular liquefied natural gas (LNG), as a marine fuel in one or more engines of a ship or of a corresponding sea-going vessel. In particular the invention is related to LNG tanks and connecting pipes to an LNG tank. More particularly the invention relates to the LNG tank according to the preamble of the independent LNG tank claim.
Liquid fuels that are used as marine fuels are typically liquefied natural gas, liquefied petroleum gas or liquid petroleum gas (LPG), methanol, ethylene. Natural gas is in gaseous form in room temperature. In ships that use natural gas as fuel, the natural gas is typically stored onboard in liquid form, and thus this marine fuel is commonly called by its acronym LNG (Liquefied Natural Gas). Natural gas can be kept in liquid form by maintaining its temperature be- low a boiling point, which is approximately -163 °C. LNG system onboard comprises typically a bunkering station, which is the ship's connection with a LNG terminal on shore or with an LNG bunkering barge, insulated pipes for leading LNG to an LNG tank, which is for storage of LNG and a tank connection space where LNG is controllably evaporated and its distribution to the en- gine(s) is arranged. Typically LNG tank is a cylindrical, double-walled or single- walled, insulated stainless steel tank.
The LNG tank is usually the most expensive item in the LNG fuel handling system, taking up even 50-60% of the total cost of the system. For smaller tank sizes (below 300 m2) double-walled structure is typically used, with a vacuum generated between the shells for heat insulation with possible perlite insulation. In double shell tanks the inner wall is stainless steel and the outer wall can be either stainless steel or carbon steel.
The natural gas is delivered to the engines as a gas but stored as a liquid. A tank room or a tank connection space is associated with a storage tank and contains the equipment to convert the liquid into a gas for safe delivery to the engines. The tank room is also considered a 'secondary barrier' in case there should be leakage of the LNG, since liquid pipes and valves are inside it. In patent application publication WO 2013/128063 is disclosed an LNG tank having an inner shell of stainless steel and an outer shell spaced at a distance from the inner shell, the said inner and outer shells defining an isolation space there between. The tank consists of a stainless steel inner shell, which is de- signed for an internal pressure, and an outer shell that acts as a secondary barrier. The outer shell can be made of either stainless steel or nickel steel. The tank is insulated with perlite/vacuum.
Natural gas is a safe fuel when the right precautions are taken. Neither is LNG in a liquid state explosive, corrosive or toxic. Thus, possible spillages will not cause any lasting contamination, as the liquid will evaporate as gas.
The low temperature, however, is an issue when considering normal marine vessel steels as too low temperatures may cause defects such as cracks to the steel. For example for some commonly used marine vessel structure steels the temperature is not allowed to drop below -5°C. A marine vessel refers to a ship, or other floating structure, such as an off-shore structure.
One important problem to be solved relates to the scenario of loss of vacuum in double shelled storage tanks. In case of loss of vacuum the insulation properties will be significantly reduced, which causes the temperature of the outer shell to drastically decrease. A reduced temperature on the outer shell will conduct coldness to the surrounding walls of a tank hold space and to other surrounding structures of the marine vessel. A tank hold refers to a compartment inside the marine vessel hull that surrounds the LNG tank and the tank connection space. In case the surrounding structures are not constructed of a cold resistant material such as stainless steel, which is expensive, the problem is to be solved so that the temperature of the surrounding structures will not reach the temperature limitations of the material. According to the worst case scenario the leakage scenario shall be calculated with a -163°C outer shell temperature. These problems enhance especially in cases where the LNG tank is located in a tank hold space of a marine vessel. An object of the present invention is to provide an improved LNG tank, in which the problems described above are eliminated or at least minimized.
Another object of the invention is to prevent any leakage and cold temperatures related problems in connection with an LNG tank. Another object of the invention is to create a double-shell LNG tank with more LNG space within a certain space.
In order to achieve the above objects and those that will come apparent later the LNG tank according to the invention is characterized by the features of in- dependent LNG tank claim. Advantageous embodiments and features are defined in dependent claims.
According to the invention the LNG tank located in a tank hold space of a marine vessel comprises a inner metal shell, an outer metal shell and an isolation space between the shells containing vacuum, where in the LNG tank further comprises an insulation material adhered on the outer surface of the outer metal shell.
According to an advantageous feature the insulation material adhered on the outer surface of the outer metal shell substantially covers the outer surface of the outer shell of the LNG tank. According to an advantageous aspect the insulation material adhered on the outer surface of the outer metal shell is polyurethane (PUR) or other corresponding onto the outer surface of the outer shell of the LNG tank sprayed insulating foam. Advantageously thermal conductivity (NPT) of the PUR is: below 0.2 W/m * k and density is 1 10- 130 kg/m3. According to another advantageous aspect the insulation material adhered on the outer surface of the outer metal shell is formed of at least one insulation panel, advantageously several insulation panels, substantially covering the outer surface of the outer shell of the LNG tank. Advantageously the insulation material adhered on the outer surface of the outer metal shell is formed of several insulation panels forming a substantially continuous insulation material layer onto the outer surface of the outer shell of the LNG tank.
According to another advantageous aspect the insulation material adhered on the outer surface of the outer metal shell comprises at least one insulation panel and polyurethane (PUR) or other corresponding onto the outer surface of the outer shell of the LNG tank sprayed insulating foam.
According to an advantageous feature the isolation space between the inner metal shell and the outer metal shell containing vacuum is perlite filled. According to an advantageous feature the inner metal shell is stainless steel and the outer metal shell is stainless steel.
According to an advantageous feature the insulation panels are vacuum insulated panels (VIP) comprising vacuum inside a reflective layer. By the vacuum an effective form of insulation is achieved and thus the required insulation thickness can be minimized with the use of VI Ps. The VI Ps can be of different shapes and are mounted on the outside of the outer shell. Advantageously thermal conductivity (NPT) of the VIPS is: below 0.0023 W/m * k and density is 270 - 290 kg/m3. According to an advantageous feature the isolation space between the tank shells is 250 - 350 mm thick, and comprises vacuum filled with perlite. The insulation thickness of the insulation material formed of vacuum insulated panels adhered on the outer surface of the outer shell of the LNG tank is 30-70 mm.
According to an advantageous feature surrounding structures of the LNG tank comprise at least one wall or floor of a tank connection space i.e. a tank room and the material of the surrounding structure is DNV grade A steel (NV A steel).
According to an advantageous aspect a marine vessel comprises an LNG tank according to the invention. As the LNG tank comprises the insulation of the outer shell surface, in the case of loss or reduction of vacuum from the isolation space between the shells of the LNG tank, the insulation prevents the reduced temperature on the outer shell to conduct coldness to the surrounding structures and thus the temperatures of the surrounding structures remain within the temperature limi- tations of the material even in the worst case scenario with a -163°C outer shell temperature of the LNG tank.
The insulation of the outer shell surface of the LNG tank also reduces the requirement of the distance between the shells as the outer insulation decreases capacity needed of the isolation space between the shells. The insulation of the outer shell surface of the LNG tank also makes it possible to reduce the distance from the outer surface of the tank to the walls of the tank room due to the improved insulation achieved by the insulation of the outer shell surface.
As the problem relating to cold convection in case of loss or significant loss of vacuum of the isolation space between the shells of the LNG tank is solved by insulation of the outer surface of the outer shell of the LNG tank also a clear advantage in respect of space requirements is achieved. In ships and other marine application the space is extremely limited the solution according to the advantageous feature of the invention to use as the insulation material the vacuum insulation panes is very advantageous as the vacuum insulation pan- els are space effective.
In the following the invention is described in more detail by reference to the accompanying drawing in which
Fig. 1 shows schematically a prior art LNG fuel distribution architecture and Figs 2 - 3 show schematically an advantageous example of the invention. Fig. 1 illustrates schematically the architecture of a known system onboard an LNG-fuelled ship. An LNG bunkering station 101 is located on the deck and used to fill up the system with LNG. The LNG fuel storage system comprises one or more thermally insulated gas tanks 102 for storing the LNG in liquid form, and the so-called tank room 103 where the LNG is controllably evapo- rated and its distribution to the engine(s) is arranged. The LNG tank 102 and the tank room 103 are located in a tank hold space 16 of a marine vessel. Evaporation means a phase change from liquid to gaseous phase, for which reason all subsequent stages should leave the L for liquefied out of the acronym and use only NG (Natural Gas) instead. The engine 104 or engines of the ship are located in an engine room 105. Each engine has its respective engine-specific fuel input subsystem 106, which in the case of gaseous fuel is in some sources referred to as the GVU (Gas Valve Unit). The tank room 103 of fig. 1 comprises two evaporators, of which the first evaporator 107 is the so-called PBU (Pressure Build-Up) evapo- rator used to maintain a sufficient pressure inside the gas tank 102. Hydrostatic pressure at the inlet of a main supply line 108 inside the gas tank 102 is the driving force that makes the LNG flow into the second evaporator 109, which is the MGE or Main Gas Evaporator from which the fuel is distributed in gaseous form towards the engines. In order to ensure that evaporated gas flows to the GVU(s) and further to the engine(s) at sufficiently high pressure, the PBU system maintains the internal pressure of the gas tank 102 at or close to a predetermined value, which is typically between 5 and 7 bars. The engine 104 comprises one or more cooling circuits. Schematically shown in fig. 1 is an external loop 1 10 of the so-called low temperature (LT) cooling circuit, which may be used for example to cool lubricating oil. The so-called LT water that circulates in the external loop 1 10 may have a temperature around 50 degrees centigrade when it goes through a heat exchanger 1 1 1 , in which it donates heat to a mixture of glycol and water that in turn transfers heat to the evaporators 107 and 109. The glycol / water mixture circuit comprises a circulation pump 1 12 and an expansion tank 1 13. Glycol is needed in the mixture to prevent it from freezing when it comes into contact with the extremely cold LNG inlet parts of the evaporators 107 and 109. During the course of the following description of figures 2 - 3 corresponding reference numbers and signs will be used to identify corresponding elements, parts and part components unless otherwise mentioned. In the following the examples are described mainly by reference to an LNG tank of a ship or a corresponding marine vessel in view of simplifying the disclosure but it should be noted that instead of this example any type of a tank for correspond liquid fuel tanks with similar problems for example cryogenic liquid tanks can have similar features and properties in accordance with the invention.
In the example of figures 2-3 schematic cross-sections of an LNG tank 10 located inside a tank hold space 16 of a marine vessel are shown. The LNG tank 10 is a double-shell LNG tank and comprises an inner shell 1 1 defining the tank space for the LNG and an outer shell 12. In the figure the level of the LNG is denoted by reference sign L. Between the inner shell 1 1 and the outer shell 12 the isolation space 13 is located. On the outer surface 14 of the outer shell 12 insulation material 15 is adhered. The insulation material 15 is advanta- geously VIP (vacuum insulated panels) and/or PUR (polyurethane). The insulation material 15 adhered on the outer surface 14 of the outer metal shell 12 substantially covers the outer surface 14 of the outer shell 12 of the LNG tank 10. The isolation space 13 between the inner metal shell 1 1 and the outer metal shell 12 advantageously contains vacuum. The isolation space 13 is ad- vantageously perlite filled and it comprises 250 - 350 mm perlite. The insula- tion thickness of the insulation material 15 in case formed of vacuum insulated panels adhered on the outer surface 14 of the outer shell 12 of the LNG tank 10 is 30-70 mm. The deck 18 below the LNG tank 10 located in a tank connection space i.e. a tank room is typically DNV grade A steel (NV A steel). Above only some advantageous examples of the invention have been described to which the invention is not to be narrowly limited. It is clear to one skilled in the art that many modifications and variations are possible within the invention as defined in the following claims.
Reference signs used in figure 1
101 LNG bunkering station
102 tank
103 tank room
104 engine
105 engine room
106 fuel input subsystem
107 first evaporator
08 main supply line
109 second evaporator
1 10 external loop of the so-called low temperature (LT) cooling circuit
1 1 1 heat exchanger
1 12 circulation pump
1 13 expansion tank
1 14 tank hold space
Reference signs used in figures 2 - 3
10 LNG tank
1 1 inner shell
12 outer shell
13 isolation space
14 outer surface of the outer shell
5 insulation material 16 tank hold space
17 foot of LNG tank
18 deck
L level of LNG
LNG liquefied natural gas

Claims

Claims
LNG tank (10) located in a tank hold space (16) of a marine vessel comprising an inner metal shell (1 1 ), an outer metal shell (12) and an isolation space (13) between the shells (1 1 , 12) advantageously containing vacuum, characterized in that the LNG tank (10) further comprises an insulation material (15) adhered on outer surface (14) of the outer metal shell (12).
LNG tank according to claim 1 , characterized in that the insulation material (15) adhered on the outer surface (14) of the outer metal shell (12) substantially covers the outer surface (14) of the outer shell (12) of the LNG tank (10).
LNG tank according to claim 1 or 2, characterized in that the insulation material (15) adhered on the outer surface (14) of the outer metal shell (12) is polyurethane (PUR) or other corresponding onto the outer surface (14) of the outer shell (12) of the LNG tank (10) sprayed insulating foam.
LNG tank according to claims 1 or 2, characterized in that the insulation material (15) adhered on the outer surface (14) of the outer metal shell (12) is formed of at least one insulation panel containing vacuum, in particular formed of at least one vacuum insulation panel (VIP).
LNG tank according to claims 1 or 2, characterized in that the insulation material (15) adhered on the outer surface (14) of the outer metal shell (12) is formed of several vacuum insulation panels (VIP) forming a substantially continuous insulation material layer onto the outer surface (14) of the outer shell (12) of the LNG tank (10).
LNG tank according to any of previous claims, characterized in that the insulation material (15) adhered on the outer surface (14) of the outer metal shell (12) comprises at least one vacuum insulation panel (VIP) and polyurethane (PUR).
7. LNG tank according to any of previous claims, characterized in that the isolation space (13) between the inner metal shell (1 1 ) and the outer metal shell (12) contains vacuum and is perlite filled.
LNG tank according to any of previous claims, characterized in that the isolation space between the inner metal shell (1 1 ) and the outer metal shell (12) is 250 - 350 mm thick, and comprises vacuum filled with perlite and that the insulation thickness of the insulation material (15) formed of at least one vacuum insulated panel adhered on the outer surface of the outer shell of the LNG tank is 30-70 mm.
9. LNG tank according to any of previous claims, characterized in that surrounding structures of the LNG tank (10) comprise at least one wall or deck of a tank connection space i.e. a tank room and that material of the surrounding structure is DNV grade A steel (NV A steel).
10. A marine vessel comprising an LNG tank according to any of the previous claims.
PCT/FI2014/051012 2014-12-16 2014-12-16 Lng tank Ceased WO2016097461A1 (en)

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP3287685A1 (en) * 2016-08-26 2018-02-28 ABH Ingenieur-Technik GmbH Insulated container for temperature-sensitive fluids
WO2018065658A1 (en) 2016-10-05 2018-04-12 Wärtsilä Finland Oy A fuel tank unit
JP2026502417A (en) * 2023-06-22 2026-01-23 シービーアンドアイ エスティーエス デラウェア エルエルシー Cryopumping-resistant LH2 storage container

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0440031A1 (en) * 1990-01-12 1991-08-07 Nisshinbo Industries, Inc. Vacuum heat-insulating container
FR2967130A1 (en) * 2010-11-04 2012-05-11 New Generation Natural Gas Liquefied natural gas isolation device for use in ship tank, has openings for replacement of natural gas with inert gas consisting mainly of argon, lighter gas such as methane, or nitrogen that is present in insulating spaces
WO2013128063A1 (en) 2012-02-29 2013-09-06 Wärtsilä Finland Oy Lng tank
WO2014127840A1 (en) * 2013-02-25 2014-08-28 Olaf Berghoff Tank for cryogenic fluids
WO2014203530A1 (en) * 2013-06-21 2014-12-24 川崎重工業株式会社 Liquefied gas-storing tank and liquefied gas transport vessel

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0440031A1 (en) * 1990-01-12 1991-08-07 Nisshinbo Industries, Inc. Vacuum heat-insulating container
FR2967130A1 (en) * 2010-11-04 2012-05-11 New Generation Natural Gas Liquefied natural gas isolation device for use in ship tank, has openings for replacement of natural gas with inert gas consisting mainly of argon, lighter gas such as methane, or nitrogen that is present in insulating spaces
WO2013128063A1 (en) 2012-02-29 2013-09-06 Wärtsilä Finland Oy Lng tank
WO2014127840A1 (en) * 2013-02-25 2014-08-28 Olaf Berghoff Tank for cryogenic fluids
WO2014203530A1 (en) * 2013-06-21 2014-12-24 川崎重工業株式会社 Liquefied gas-storing tank and liquefied gas transport vessel

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP3287685A1 (en) * 2016-08-26 2018-02-28 ABH Ingenieur-Technik GmbH Insulated container for temperature-sensitive fluids
WO2018065658A1 (en) 2016-10-05 2018-04-12 Wärtsilä Finland Oy A fuel tank unit
JP2026502417A (en) * 2023-06-22 2026-01-23 シービーアンドアイ エスティーエス デラウェア エルエルシー Cryopumping-resistant LH2 storage container

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