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Petroleum, LPG, LNG, Chemicals, Dry Cargo Software, Table 54A, 54B, 54D, 54E, Klosek - McKinley, COSTALD, ASTM D1555M, NBS 1045-1981, IUPAC
Analysis of boil-off rate problem in Liquefied Natural Gas (LNG) receiving terminals.
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Predicting saturated vapor pressure of LNG from density and temperature data with a view to improving tank pressure management - ScienceDirect
PDF) IBP1081_17 SIMPLE EQUATION FOR THE CALCULATION OF LNG DENSITY FROM COMPOSITION
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Petroleum, LPG, LNG, Chemicals, Dry Cargo Software, Table 54A, 54B, 54D, 54E, Klosek - McKinley, COSTALD, ASTM D1555M, NBS 1045-1981, IUPAC
Enhancement of the revised Klosek and McKinley method for density calculations of liquefied natural gas (LNG) over the temperature range from (100 to 135) K at pressures up to 10 MPa - ScienceDirect
Density measurements of liquefied natural gas (LNG) over the temperature range from (105 to 135) K at pressures up to 8.9 MPa - ScienceDirect
LNG Custody Transfer: LNG Energy determination
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