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LNG
| Row |
Properties |
Unit |
Result |
| 1. |
Methane CH4 |
% Mol |
91.1300 |
| 2. |
Ethane:C2H6 |
% Mol |
6.1100 |
| 3. |
Propane:C3H8 |
% Mol |
2.1600 |
| 4. |
lso Butane :1-C4H10 |
% Mol |
0.3100 |
| 5. |
N·Butane :n-C4H10 |
% Mol |
0.2600 |
| 6. |
lso Pentane:i-C5H12 |
% Mal |
0.0000 |
| 9. |
N·Petane:n-C5H12 |
% Mol |
0.0000 |
| 8. |
N-Hexane:n-C6H14 |
% Mal |
0.0000 |
| 9. |
Nitrogen :N2 |
% Mal |
0.0300 |
| 10. |
Oxygen 02 |
% Mol |
0.0000 |
| 11. |
Carbon Dioxide :C02 |
% Mol |
0.0000 |
| 12. |
Hydrogen Sulphur.H2S |
mg/m3 |
<0.2 |
| 13. |
Total Sulphur: S |
mg/m3 |
<0.2 |
| 14. |
Hydrocarbon Ana:lys1s Method = ISO 6974 |
| 15. |
H2S &Total Sulphur Analysis Method ASTM 06667& ISO 1973 Average Liquid Temp Prior to Discharge ·c -159.10 Average Density @ Observed Temp (Calculated) Kg/m3 451.79 |
| 16. |
Calorific Value Minimum 36.4 MJ/m3 Maximum 40.9 MJ/m3 |
