LNG tank and operation of the same
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 operating an LNG tank ship, the method comprising:
providing an LNG tank ship comprising:
a membrane-type LNG tank comprising a thermal insulation wall and a membrane,
LNG and boil-off gas of the LNG contained in the membrane-type LNG tank, and
a safety valve connected to the membrane-type LNG tank for releasing LNG boil-off gas therefrom when vapor pressure inside the membrane-type LNG tank exceeds a cut-off pressure of the safety valve ranging between 0.4 bar (gauge pressure) and 1 bar (gauge pressure),
wherein the LNG tank ship does not comprises an LNG-consuming boiler for consuming LNG boil-off gas from the membrane-type LNG tank,
wherein the LNG tank ship does not comprises an LNG-consuming turbine for consuming LNG boil-off gas from the membrane-type LNG tank,
wherein the LNG tank ship does not comprises an LNG-consuming propulsion engine for consuming LNG boil-off gas from the membrane-type LNG tank,
loading LNG to the membrane-type LNG tank at a loading pressure;
subsequent to loading, letting the vapor pressure inside the membrane-type LNG tank increase to an increased pressure ranging between 0.25 bar (gauge pressure) and the cut-off pressure; and
subsequently, unloading the LNG from the membrane-type LNG tank to an LNG-receiving tank that is located outside the LNG tank ship and requires a receiving pressure higher than the increased pressure,
wherein unloading the LNG comprises increasing the LNG's pressure to higher than the increased pressure such that the LNG unloaded to the LNG receiving tank matches the higher pressure requirement.
2. The method of claim 1 , wherein the LNG-receiving tank is located at a receiving place that is not equipped with an LNG re-condenser for processing the unloaded LNG.
3. The method of claim 1 , wherein the LNG tank ship does not comprises an LNG combustion unit for burning LNG boil-off gas from the membrane-type LNG tank.
4. The method of claim 1 , wherein the increased pressure inside the membrane tank ranges between 0.3 bar (gauge pressure) and 1 bar (gauge pressure).
5. The LNG tank ship of claim 1 , wherein the LNG tank ship comprises at least one LNG liquefaction plant configured to re-liquefy LNG boil-off gas.
6. The method of claim 2 , wherein the LNG tank ship does not comprises an LNG combustion unit for burning LNG boil-off gas from the membrane-type LNG tank.
7. The method of claim 2 , wherein the increased pressure inside the membrane tank ranges between 0.3 bar (gauge pressure) and 1 bar (gauge pressure).
8. The LNG tank ship of claim 2 , wherein the LNG tank ship comprises at least one LNG liquefaction plant configured to re-liquefy LNG boil-off gas.
9. The method of claim 3 , wherein the increased pressure inside the membrane tank ranges between 0.3 bar (gauge pressure) and 1 bar (gauge pressure).
10. The LNG tank ship of claim 3 , wherein the LNG tank ship comprises at least one LNG liquefaction plant configured to re-liquefy LNG boil-off gas.
11. The LNG tank ship of claim 4 , wherein the LNG tank ship comprises at least one LNG liquefaction plant configured to re-liquefy LNG boil-off gas.