Method and system for the real-time calculation of the amount of energy transported in a non-refrigerated, pressurised, liquefied natural gas tank
AssigneeEngie
InventorsMichel Ben Belgacem-Strek, Gabrielle Menard, Frédéric Legrand
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Abstract
Some embodiments of the presently disclosed subject matter relate to a method and system for the real-time calculation of the amount of residual chemical energy in a non-refrigerated, pressurised tank containing liquefied natural gas, without a composition of the liquefied natural gas having to be determined.
Claims7
A method for real-time calculation of residual chemical energy E contained in a pressurised tank defined by its shape and its dimensions and containing a layer of liquefied natural gas, the layer of liquefied natural gas being defined at a given instant t, by its temperature T, its density ρ, and its level h in the tank,
- the method including an algorithm that, at a given instant t, comprises:
- acquiring the characteristic parameters of the layer of liquefied natural gas by measurement,
- of the level h of the layer of liquefied natural gas in the tank, using a level sensor,
- of the temperature T using a temperature sensor, and
- of the density ρ using a density sensor;
- and
- determining the total mass mt of the liquefied natural gas contained in the tank, wherein the algorithm, for each instant t, further comprises:
- calculating of the mass gross calorific value GCVmass of the liquefied natural gas using a function f taking as parameters the temperature and the density ρ of the liquid according to the formula:
- GCVmass=f(T,ρ);
- and
- calculating of the residual chemical energy E according to the formula:
- E=GCVmass*mt
- wherein the function f that connects the mass gross calorific value GCVmass to die parameters T and ρ is according to the formula:
- f(T,ρ)=A(T)+B*p
- where,
- A is a constant value for a given temperature, and
- B is a constant independent of the composition.
Dependencies are inferred from the claim text.