| Température (°C) | Masse volumique (kg/m3) | Facteur de correction |
|---|---|---|
| -30 | 831.2 | 1.0475 |
| -29.5 | 830.8 | 1.047 |
| -29 | 830.3 | 1.0464 |
| -28.5 | 829.9 | 1.0459 |
| -28 | 829.5 | 1.0454 |
| -27.5 | 829.1 | 1.0449 |
| -27 | 828.7 | 1.0444 |
| -26.5 | 828.3 | 1.0438 |
| -26 | 827.9 | 1.0433 |
| -25.5 | 827.5 | 1.0428 |
| -25 | 827.1 | 1.0423 |
| -24.5 | 826.7 | 1.0418 |
| -24 | 826.2 | 1.0412 |
| -23.5 | 825.8 | 1.0407 |
| -23 | 825.4 | 1.0402 |
| -22.5 | 825 | 1.0397 |
| -22 | 824.6 | 1.0392 |
| -21.5 | 824.1 | 1.0386 |
| -21 | 823.7 | 1.0381 |
| -20.5 | 823.3 | 1.0376 |
| -20 | 822.9 | 1.0371 |
| -19.5 | 822.5 | 1.0365 |
| -19 | 822.1 | 1.036 |
| -18.5 | 821.7 | 1.0355 |
| -18 | 821.3 | 1.035 |
| -17.5 | 820.8 | 1.0344 |
| -17 | 820.4 | 1.0339 |
| -16.5 | 820 | 1.0334 |
| -16 | 819.6 | 1.0329 |
| -15.5 | 819.2 | 1.0324 |
| -15 | 818.7 | 1.0318 |
| -14.5 | 818.3 | 1.0313 |
| -14 | 817.9 | 1.0308 |
| -13.5 | 817.5 | 1.0303 |
| -13 | 817.1 | 1.0297 |
| -12.5 | 816.7 | 1.0292 |
| -12 | 816.3 | 1.0287 |
| -11.5 | 815.9 | 1.0282 |
| -11 | 815.4 | 1.0276 |
| -10.5 | 815 | 1.0271 |
| -10 | 814.6 | 1.0266 |
| -9.5 | 814.1 | 1.026 |
| -9 | 813.7 | 1.0255 |
| -8.5 | 813.3 | 1.025 |
| -8 | 812.9 | 1.0245 |
| -7.5 | 812.5 | 1.0239 |
| -7 | 812.1 | 1.0234 |
| -6.5 | 811.7 | 1.0229 |
| -6 | 811.3 | 1.0224 |
| -5.5 | 810.8 | 1.0218 |
| -5 | 810.4 | 1.0213 |
| -4.5 | 810 | 1.0208 |
| -4 | 809.5 | 1.0202 |
| -3.5 | 809.1 | 1.0197 |
| -3 | 808.7 | 1.0192 |
| -2.5 | 808.3 | 1.0187 |
| -2 | 807.9 | 1.0181 |
| -1.5 | 807.5 | 1.0176 |
| -1 | 807.1 | 1.0171 |
| -0.5 | 806.6 | 1.0165 |
| 0 | 806.2 | 1.016 |
| 0.5 | 805.8 | 1.0155 |
| 1 | 805.3 | 1.0149 |
| 1.5 | 804.9 | 1.0144 |
| 2 | 804.5 | 1.0139 |
| 2.5 | 804.1 | 1.0133 |
| 3 | 803.7 | 1.0128 |
| 3.5 | 803.3 | 1.0123 |
| 4 | 802.8 | 1.0117 |
| 4.5 | 802.4 | 1.0112 |
| 5 | 802 | 1.0107 |
| 5.5 | 801.6 | 1.0102 |
| 6 | 801.1 | 1.0096 |
| 6.5 | 800.7 | 1.0091 |
| 7 | 800.3 | 1.0086 |
| 7.5 | 799.8 | 1.008 |
| 8 | 799.5 | 1.0075 |
| 8.5 | 799.1 | 1.007 |
| 9 | 798.6 | 1.0064 |
| 9.5 | 798.2 | 1.0059 |
| 10 | 797.8 | 1.0054 |
| 10.5 | 797.3 | 1.0048 |
| 11 | 796.9 | 1.0043 |
| 11.5 | 796.4 | 1.0037 |
| 12 | 796 | 1.0032 |
| 12.5 | 795.6 | 1.0027 |
| 13 | 795.2 | 1.0021 |
| 13.5 | 794.8 | 1.0016 |
| 14 | 794.4 | 1.0011 |
| 14.5 | 793.9 | 1.0005 |
| 15 | 793.5 | 1 |
| 15.5 | 793.1 | 0.9995 |
| 16 | 792.6 | 0.9989 |
| 16.5 | 792.2 | 0.9984 |
| 17 | 791.8 | 0.9979 |
| 17.5 | 791.4 | 0.9973 |
| 18 | 791 | 0.9968 |
| 18.5 | 790.5 | 0.9962 |
| 19 | 790.1 | 0.9957 |
| 19.5 | 789.7 | 0.9952 |
| 20 | 789.2 | 0.9946 |
| 20.5 | 788.8 | 0.9941 |
| 21 | 788.4 | 0.9936 |
| 21.5 | 787.9 | 0.993 |
| 22 | 787.5 | 0.9925 |
| 22.5 | 787.1 | 0.9919 |
| 23 | 786.7 | 0.9914 |
| 23.5 | 786.3 | 0.9909 |
| 24 | 785.8 | 0.9903 |
| 24.5 | 785.4 | 0.9898 |
| 25 | 784.9 | 0.9892 |
| 25.5 | 784.5 | 0.9887 |
| 26 | 784.1 | 0.9882 |
| 26.5 | 783.7 | 0.9876 |
| 27 | 783.3 | 0.9871 |
| 27.5 | 782.8 | 0.9865 |
| 28 | 782.4 | 0.986 |
| 28.5 | 782 | 0.9855 |
| 29 | 781.5 | 0.9849 |
| 29.5 | 781.1 | 0.9844 |
| 30 | 780.6 | 0.9838 |
| 30.5 | 780.2 | 0.9833 |
| 31 | 779.9 | 0.9828 |
| 31.5 | 779.4 | 0.9822 |
| 32 | 779 | 0.9817 |
| 32.5 | 778.5 | 0.9811 |
| 33 | 778.1 | 0.9806 |
| 33.5 | 777.7 | 0.9801 |
| 34 | 777.2 | 0.9795 |
| 34.5 | 776.8 | 0.979 |
| 35 | 776.4 | 0.9784 |
| 35.5 | 776 | 0.9779 |
| 36 | 775.5 | 0.9773 |
| 36.5 | 775.1 | 0.9768 |
| 37 | 774.7 | 0.9763 |
| 37.5 | 774.2 | 0.9757 |
| 38 | 773.8 | 0.9752 |
| 38.5 | 773.3 | 0.9746 |
| 39 | 772.9 | 0.9741 |
| 39.5 | 772.5 | 0.9735 |
| 40 | 772.1 | 0.973 |
Coefficient cubique de dilatation à 15°C = 0.001072 par °C
Pour obtenir le volume net du liquide à 15°C, multiplier le volume non compensé enregistré par lecompteur, par le facteur de correction du volume (FCV) qui correspond à la température moyenne du liquide, mesurée pendant la livraison.
Les masses volumiques sont des masses (sous vide) et sont tirées de : Les propriétés thermodynamiques de l'éthanol à la pression atmosphérique, Journal of Engineering Physics, Vol. 47, No.3, 1984.