LNG tank and unloading of LNG from the tank
View Patent ↗Disclosed is a liquefied natural gas storage apparatus. The apparatus includes a heat insulated tank and liquefied natural gas contained in the tank. The tank has heat insulation sufficient to maintain liquefied natural gas therein such that most of the liquefied natural gas stays in liquid. The contained liquefied natural gas has a vapor pressure from about 0.3 bar to about 2 bar. The apparatus further includes a safety valve configured to release a part of liquefied natural gas contained in the tank when a vapor pressure of liquefied natural gas within the tank becomes higher than a cut-off pressure. The cut-off pressure is from about 0.3 bar to about 2 bar.
1. A method of receiving LNG from an LNG tank containing LNG, the method comprising:
providing a receiving tank;
connecting between the receiving tank and an LNG tank containing LNG such that a fluid communication between the receiving tank and the LNG tank is established; and
receiving at least part of the LNG into the receiving tank from the LNG tank, in which the LNG has a vapor pressure from about 0.3 bar to about 2 bar,
wherein the LNG tank is integrated with a ship, the ship comprising:
the LNG tank configured to contain LNG in both liquid and gaseous phases therein, wherein the LNG tank has a volume;
a primary engine of the ship for generating power to move the ship, wherein the engine is designed to use a fuel other than LNG such that the engine does not use LNG to reduce vapor pressure of the LNG within the LNG tank; and
at least one liquefier configured to convert at least a portion of gaseous phase LNG to liquid phase LNG, wherein the at least one liquefier has a processing capacity, which is the maximum amount of gaseous phase LNG to be processed by the at least one liquefier for one hour, wherein a ratio of the processing capacity to the volume is smaller than about 0.015 kg/m 3 .
2. The method of claim 1 , wherein the vapor pressure within the LNG tank is from about 0.4 bar to about 1.5 bar.
3. The method of claim 1 , wherein the vapor pressure within the LNG tank is from about 0.5 bar to about 1 bar.
4. The method of claim 1 , wherein the vapor pressure, within the LNG tank is from about 0.65 bar to about 0.75 bar.
5. The method of claim 1 , wherein the vapor pressure within the LNG tank is greater than that within the receiving tank.
6. The method of claim 1 , wherein the receiving tank is located on a shore.
7. The method of claim 1 , wherein the receiving tank is located inland substantially away from a shore.
8. The method of claim 1 , further comprising:
providing an additional receiving tank;
connecting between the additional receiving tank and the LNG tank such that a fluid communication between the additional receiving tank and the LNG tank is established; and
receiving at least part of the LNG into the additional receiving tank from the LNG tank, wherein receiving into the additional receiving tank is simultaneously performed with receiving into the receiving tank for at least some time.
9. The method of claim 1 , wherein the LNG tank comprises:
an interior wall defining an interior space configured to contain LNG;
an exterior wall substantially surrounding the interior wall; and
a heat insulation interposed between the interior wall and the exterior wall.
10. A method of unloading LNG from an LNG tank containing LNG to a receiving tank, the method comprising:
providing an LNG tank comprising LNG, which has a vapor pressure from about 0.3 bar to about 2 bar;
connecting between the LNG tank and a receiving tank such that a fluid communication between the receiving tank and the LNG tank is established; and
unloading at least part of the LNG from the LNG tank to the receiving tank;
wherein the LNG tank is integrated with a ship, the ship comprising:
the LNG tank configured to contain LNG in both liquid and gaseous phases therein, wherein the LNG tank has a volume;
a primary engine of the ship for generating power to move the ship, wherein the engine is designed to use a fuel other than LNG such that the engine does not use LNG to reduce vapor pressure of the LNG within the LNG tank; and
at least one liquefier configured to convert at least a portion of gaseous phase LNG to liquid phase LNG, wherein the at least one liquefier has a processing capacity, which is the maximum amount of gaseous phase LNG to be processed by the at least one liquefier for one hour, wherein a ratio of the processing capacity to the volume is smaller than about 0.015 kg/m 3 .
11. The method of claim 10 , wherein the vapor pressure within the LNG tank is from about 0.4 bar to about 1.5 bar.
12. The method of claim 10 , wherein the vapor pressure within the LNG tank is from about 0.5 bar to about 1 bar.
13. The method of claim 10 , wherein the vapor pressure within the LNG tank is from about 0.65 bar to about 0.75 bar.
14. The method of claim 10 , wherein the vapor pressure of the LNG tank is greater than that within the receiving tank.
15. The method of claim 10 , wherein the receiving tank is located on a shore.
16. The method of claim 10 , wherein the receiving tank is located inland substantially away from a shore.
17. The method of claim 10 , further comprising:
connecting between the LNG tank and an additional receiving tank such that a fluid communication between the additional receiving tank and the LNG tank is established; and
unloading at least part of the LNG from the LNG tank to the additional receiving tank, wherein unloading to the additional receiving tank is simultaneously performed with unloading to the receiving tank for at least some time.
18. The method of claim 10 , wherein the LNG tank comprises:
an interior wall defining an interior space configured to contain LNG;
an exterior wall substantially surrounding the interior wall; and
a heat insulation interposed between the interior wall and the exterior wall.