| Temperature (°C) | Density (kg/m3) | Correction Factor |
|---|---|---|
| -30 | 847 | 1.0515 |
| -29.5 | 846.5 | 1.0509 |
| -29 | 846.1 | 1.0504 |
| -28.5 | 845.6 | 1.0498 |
| -28 | 845.2 | 1.0492 |
| -27.5 | 844.7 | 1.0486 |
| -27 | 844.2 | 1.0481 |
| -26.5 | 843.8 | 1.0475 |
| -26 | 843.3 | 1.0469 |
| -25.5 | 842.9 | 1.0464 |
| -25 | 842.4 | 1.0458 |
| -24.5 | 841.9 | 1.0452 |
| -24 | 841.5 | 1.0446 |
| -23.5 | 841 | 1.0441 |
| -23 | 840.5 | 1.0435 |
| -22.5 | 840.1 | 1.0429 |
| -22 | 839.6 | 1.0424 |
| -21.5 | 839.2 | 1.0418 |
| -21 | 838.7 | 1.0412 |
| -20.5 | 838.2 | 1.0406 |
| -20 | 837.8 | 1.0401 |
| -19.5 | 837.3 | 1.0395 |
| -19 | 836.9 | 1.0389 |
| -18.5 | 836.4 | 1.0383 |
| -18 | 835.9 | 1.0378 |
| -17.5 | 835.5 | 1.0372 |
| -17 | 835 | 1.0366 |
| -16.5 | 834.6 | 1.0361 |
| -16 | 834.1 | 1.0355 |
| -15.5 | 833.6 | 1.0349 |
| -15 | 833.2 | 1.0343 |
| -14.5 | 832.7 | 1.0338 |
| -14 | 832.2 | 1.0332 |
| -13.5 | 831.8 | 1.0326 |
| -13 | 831.3 | 1.032 |
| -12.5 | 380.9 | 1.0315 |
| -12 | 830.4 | 1.0309 |
| -11.5 | 829.9 | 1.0303 |
| -11 | 829.5 | 1.0298 |
| -10.5 | 829 | 1.0292 |
| -10 | 828.6 | 1.0286 |
| -9.5 | 828.1 | 1.028 |
| -9 | 827.6 | 1.0275 |
| -8.5 | 827.2 | 1.0269 |
| -8 | 826.7 | 1.0263 |
| -7.5 | 826.3 | 1.0258 |
| -7 | 825.8 | 1.0252 |
| -6.5 | 825.3 | 1.0246 |
| -6 | 824.9 | 1.024 |
| -5.5 | 824.4 | 1.0235 |
| -5 | 824 | 1.0229 |
| -4.5 | 823.5 | 1.0223 |
| -4 | 823 | 1.0217 |
| -3.5 | 822.6 | 1.0212 |
| -3 | 822.1 | 1.0206 |
| -2.5 | 821.6 | 1.02 |
| -2 | 821.2 | 1.0195 |
| -1.5 | 820.7 | 1.0189 |
| -1 | 820.3 | 1.0183 |
| -0.5 | 819.8 | 1.0177 |
| 0 | 819.3 | 1.0172 |
| 0.5 | 818.9 | 1.0166 |
| 1 | 818.4 | 1.016 |
| 1.5 | 818 | 1.0155 |
| 2 | 817.5 | 1.0149 |
| 2.5 | 817 | 1.0143 |
| 3 | 816.6 | 1.0137 |
| 3.5 | 816.1 | 1.0132 |
| 4 | 815.7 | 1.0126 |
| 4.5 | 815.2 | 1.012 |
| 5 | 814.7 | 1.0114 |
| 5.5 | 814.3 | 1.0109 |
| 6 | 813.8 | 1.0103 |
| 6.5 | 813.3 | 1.0097 |
| 7 | 812.9 | 1.0092 |
| 7.5 | 812.4 | 1.0086 |
| 8 | 812 | 1.008 |
| 8.5 | 811.5 | 1.0074 |
| 9 | 811 | 1.0069 |
| 9.5 | 810.6 | 1.0063 |
| 10 | 816.1 | 1.0057 |
| 10.5 | 809.7 | 1.0052 |
| 11 | 809.2 | 1.0046 |
| 11.5 | 808.7 | 1.004 |
| 12 | 808.3 | 1.0034 |
| 12.5 | 807.8 | 1.0029 |
| 13 | 807.4 | 1.0023 |
| 13.5 | 806.9 | 1.0017 |
| 14 | 806.4 | 1.0011 |
| 14.5 | 806 | 1.0006 |
| 15 | 805.5 | 1 |
| 15.5 | 805 | 0.9994 |
| 16 | 804.6 | 0.9989 |
| 16.5 | 804.1 | 0.9983 |
| 17 | 803.7 | 0.9977 |
| 17.5 | 803.2 | 0.9971 |
| 18 | 802.7 | 0.9966 |
| 18.5 | 802.3 | 0.996 |
| 19 | 801.8 | 0.9954 |
| 19.5 | 801.4 | 0.9948 |
| 20 | 800.9 | 0.9943 |
| 20.5 | 800.4 | 0.9937 |
| 21 | 800 | 0.9931 |
| 21.5 | 799.5 | 0.9926 |
| 22 | 799.1 | 0.992 |
| 22.5 | 798.6 | 0.9914 |
| 23 | 798.1 | 0.9908 |
| 23.5 | 797.7 | 0.9903 |
| 24 | 707.2 | 0.9897 |
| 24.5 | 796.8 | 0.9891 |
| 25 | 796.3 | 0.9886 |
| 25.5 | 795.8 | 0.988 |
| 26 | 795.4 | 0.9874 |
| 26.5 | 794.9 | 0.9868 |
| 27 | 794.4 | 0.9863 |
| 27.5 | 794 | 0.9857 |
| 28 | 793.5 | 0.9851 |
| 28.5 | 793.1 | 0.9845 |
| 29 | 792.6 | 0.984 |
| 29.5 | 792.1 | 0.9834 |
| 30 | 791.7 | 0.9828 |
| 30.5 | 791.2 | 0.9823 |
| 31 | 790.8 | 0.9817 |
| 31.5 | 790.3 | 0.9811 |
| 32 | 789.8 | 0.9805 |
| 32.5 | 789.4 | 0.98 |
| 33 | 788.9 | 0.9794 |
| 33.5 | 788.5 | 0.9788 |
| 34 | 788 | 0.9783 |
| 34.5 | 787.5 | 0.9777 |
| 35 | 787.1 | 0.9771 |
| 35.5 | 786.6 | 0.9765 |
| 36 | 786.1 | 0.976 |
| 36.5 | 785.7 | 0.9754 |
| 37 | 785.2 | 0.9748 |
| 37.5 | 784.8 | 0.9742 |
| 38 | 784.3 | 0.9737 |
| 38.5 | 783.8 | 0.9731 |
| 39 | 783.4 | 0.9725 |
| 39.5 | 782.9 | 0.972 |
| 40 | 782.5 | 0.9714 |
Cubical coefficient of expansion at 15°C = 0.001152 per °C
To obtain the net volume of liquid at 15°C, multiply the uncompensated meter reading by the Volume Correction Factor (VCF) which corresponds to the average measured temperature of the liquid during the delivery.
Densities are mass (in vacuum) and are based on specification grade methyl isobutyl ketone whose mass density is 800.9 kg/m3; at 20°C. Volume correction factor data was derived using equation in Table 13 of ASTM E 201-70.