Volume correction factors—isopropyl alcohol (anhydrous)

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Note: These tables are intended for inspection purposes only and are not suitable in determining corrections for trade transactions of bulk commodities.

Volume correction factors to 15 °C for isopropyl alcohol (anhydrous)
Temperature °C Density(kg/m3) Volume correction factor
-30 823.2 1.0432
-29.5 822.9 1.0427
-29 822.5 1.0423
-28.5 822.2 1.0418
-28 821.8 1.0414
-27.5 821.5 1.0409
-27 821.1 1.0405
-26.5 820.8 1.0401
-26 820.4 1.0396
-25.5 820.1 1.0392
-25 819.7 1.0387
-24.5 819.4 1.0383
-24 819.0 1.0378
-23.5 818.7 1.0374
-23 818.3 1.0369
-22.5 817.9 1.0365
-22 817.6 1.0360
-21.5 817.2 1.0356
-21 816.9 1.0351
-20.5 816.5 1.0346
-20 816.1 1.0342
-19.5 815.8 1.0337
-19 815.4 1.0333
-18.5 815.1 1.0328
-18 814.7 1.0324
-17.5 814.3 1.0319
-17 814.0 1.0314
-16.5 813.6 1.0310
-16 813.2 1.0305
-15.5 812.0 1.0300
-15 812.5 1.0296
-14.5 812.1 1.0291
-14 811.8 1.0286
-13.5 811.4 1.0282
-13 811.0 1.0277
-12.5 810.7 1.0272
-12 810.3 1.0268
-11.5 809.9 1.0263
-11 809.5 1.0258
-10.5 809.2 1.0253
-10 808.8 1.0249
-9.5 808.4 1.0244
-9 808.0 1.0239
-8.5 807.7 1.0234
-8 807.3 1.0230
-7.5 806.9 1.0225
-7 806.5 1.0220
-6.5 806.1 1.0215
-6 805.8 1.0210
-5.5 805.4 1.0206
-5 805.0 1.0201
-4.5 804.6 1.0196
-4 804.2 1.0191
-3.5 803.9 1.0186
-3 803.5 1.0181
-2.5 803.1 1.0176
-2 802.7 1.0172
-1.5 802.3 1.0167
-1 801.9 1.0162
-0.5 801.5 1.0157
0 801.1 1.1052
0.5 800.8 1.0147
1 800.4 1.1042
1.5 800.0 1.0137
2 799.6 1.0132
2.5 799.2 1.1027
3 798.8 1.0122
3.5 798.4 1.0117
4 798.0 1.0112
4.5 797.6 1.0107
5 797.2 1.0102
5.5 796.8 1.0097
6 796.4 1.0092
6.5 796.0 1.0087
7 795.6 1.0082
7.5 795.2 1.0077
8 794.8 1.0072
8.5 794.4 1.0067
9 794.0 1.0062
9.5 793.6 1.0057
10 793.2 1.0052
10.5 792.8 1.0046
11 792.4 1.0041
11.5 792 1.0036
12 791.6 1.0031
12.5 791.2 1.0026
13 790.8 1.0021
13.5 790.4 1.0016
14 790 1.0010
14.5 789.6 1.0005
15 789.2 1.0000
15.5 788.8 0.9995
16 788.3 0.9990
16.5 787.9 0.9984
17 787.5 0.9979
17.5 787.1 0.9974
18 786.7 0.9969
18.5 786.3 0.9963
19 785.9 0.9958
19.5 785.4 0.9953
20 785.0 0.9948
20.5 784.6 0.9942
21 784.2 0.9937
21.5 783.8 0.9932
22 783.4 0.9926
22.5 782.9 0.9921
23 782.5 0.9916
23.5 782.1 0.9910
24 781.7 0.9905
24.5 781.2 0.9900
25 780.8 0.9894
25.5 780.4 0.9889
26 780.0 0.9884
26.5 779.5 0.9878
27 779.1 0.9873
27.5 778.7 0.9867
28 778.3 0.9862
28.5 777.8 0.9856
29 777.4 0.9851
29.5 777.0 0.9846
30 776.5 0.9840
30.5 776.1 0.9835
31 775.7 0.9829
31.5 775.2 0.9824
32 774.8 0.9818
32.5 774.4 0.9813
33 773.9 0.9807
33.5 773.5 0.9802
34 773.1 0.9796
34.5 772.6 0.9791
35 772.2 0.9785
35.5 771.8 0.9779
36 771.3 0.9774
36.5 770.9 0.9768
37 770.4 0.9763
37.5 770.0 0.9757
38 769.6 0.9752
38.5 769.1 0.9746
39 768.7 0.9740
39.5 768.2 0.9735
40 767.8 0.9729

Cubical coefficient of expansion at 15 °C = 0.001 016 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 isopropyl alcohol whose mass density is 785.027 kg/m3 at 20 °C. Volume correction factor data was derived using the equation in Table 4 of ASTM E 201-70.

Table last updated: September 2016

Date modified: