Datasets
-
Mole fraction (4)
-
η - Viscosity, Pa*s (2)
-
Pvap - Vapor or sublimation pressure, kPa (4)
-
ρl - Mass density, kg/m3 (2)
Mole fraction of Isopropyl Alcohol (2)
[ref]
Fixed |
Measured |
Mole fraction of Isopropyl Alcohol (2) - Liquid |
Temperature, K - Liquid |
Mole fraction of Isopropyl Alcohol (2) - Gas |
0.0000 |
330.00 |
0.0000 |
0.0000 |
340.00 |
0.0000 |
0.0108 |
330.00 |
0.0504 |
0.0136 |
340.00 |
0.0624 |
0.0309 |
330.00 |
0.1471 |
0.0378 |
340.00 |
0.1587 |
0.0730 |
330.00 |
0.2734 |
0.0770 |
340.00 |
0.2797 |
0.1225 |
330.00 |
0.3829 |
0.1301 |
340.00 |
0.3942 |
0.1896 |
330.00 |
0.4864 |
0.1931 |
340.00 |
0.4927 |
0.2660 |
330.00 |
0.5695 |
0.2709 |
340.00 |
0.5763 |
0.2748 |
330.00 |
0.5736 |
0.2769 |
340.00 |
0.5809 |
0.3479 |
340.00 |
0.6413 |
0.3490 |
330.00 |
0.6329 |
0.3918 |
340.00 |
0.6675 |
0.4270 |
330.00 |
0.6857 |
0.4297 |
340.00 |
0.6912 |
0.5024 |
330.00 |
0.7257 |
0.5042 |
340.00 |
0.7353 |
0.5054 |
340.00 |
0.7376 |
0.5058 |
330.00 |
0.7266 |
0.5715 |
330.00 |
0.7609 |
0.5742 |
340.00 |
0.7705 |
0.6104 |
340.00 |
0.7901 |
0.6137 |
330.00 |
0.7797 |
0.6602 |
340.00 |
0.8122 |
0.6609 |
330.00 |
0.8035 |
0.7038 |
330.00 |
0.8239 |
0.7041 |
340.00 |
0.8336 |
0.7820 |
330.00 |
0.8618 |
0.7824 |
340.00 |
0.8720 |
0.8471 |
340.00 |
0.9048 |
0.8482 |
330.00 |
0.8975 |
0.8989 |
340.00 |
0.9341 |
0.9000 |
330.00 |
0.9283 |
0.9390 |
340.00 |
0.9583 |
0.9398 |
330.00 |
0.9541 |
0.9691 |
340.00 |
0.9782 |
0.9698 |
330.00 |
0.9761 |
0.9895 |
340.00 |
0.9924 |
0.9897 |
330.00 |
0.9915 |
1.0000 |
330.00 |
1.0000 |
1.0000 |
340.00 |
1.0000 |
Mole fraction of Isopropyl Alcohol (2)
[ref]
Fixed |
Measured |
Mole fraction of Isopropyl Alcohol (2) - Liquid |
Temperature, K - Liquid |
Mole fraction of Isopropyl Alcohol (2) - Gas |
0.0000 |
323.15 |
0.0000 |
0.0970 |
323.15 |
0.3230 |
0.1940 |
323.15 |
0.4900 |
0.2680 |
323.15 |
0.5790 |
0.3420 |
323.15 |
0.6250 |
0.4590 |
323.15 |
0.6810 |
0.6010 |
323.15 |
0.7520 |
0.6770 |
323.15 |
0.7980 |
0.7600 |
323.15 |
0.8380 |
0.8430 |
323.15 |
0.8870 |
0.8990 |
323.15 |
0.9200 |
0.9530 |
323.15 |
0.9580 |
1.0000 |
323.15 |
1.0000 |
0.0000 |
338.15 |
0.0000 |
0.1900 |
338.15 |
0.4860 |
0.2750 |
338.15 |
0.5610 |
0.4600 |
338.15 |
0.6880 |
0.5940 |
338.15 |
0.7710 |
0.6750 |
338.15 |
0.8140 |
0.7560 |
338.15 |
0.8540 |
0.8410 |
338.15 |
0.8980 |
0.8950 |
338.15 |
0.9270 |
0.9500 |
338.15 |
0.9630 |
1.0000 |
338.15 |
1.0000 |
0.0000 |
353.15 |
0.0000 |
0.0990 |
353.15 |
0.3010 |
0.3360 |
353.15 |
0.6180 |
0.3990 |
353.15 |
0.6710 |
0.4550 |
353.15 |
0.7100 |
0.5900 |
353.15 |
0.7890 |
0.6700 |
353.15 |
0.8270 |
0.7560 |
353.15 |
0.8660 |
0.8390 |
353.15 |
0.9070 |
0.8950 |
353.15 |
0.9360 |
0.9480 |
353.15 |
0.9690 |
1.0000 |
353.15 |
1.0000 |
Mole fraction of Isopropyl Alcohol (2)
[ref]
Fixed |
Measured |
Mole fraction of Isopropyl Alcohol (2) - Liquid |
Temperature, K - Liquid |
Mole fraction of Isopropyl Alcohol (2) - Gas |
0.0000 |
330.00 |
0.0000 |
0.0000 |
340.00 |
0.0000 |
0.0108 |
330.00 |
0.0504 |
0.0136 |
340.00 |
0.0624 |
0.0309 |
330.00 |
0.1471 |
0.0378 |
340.00 |
0.1587 |
0.0730 |
330.00 |
0.2734 |
0.0770 |
340.00 |
0.2797 |
0.1225 |
330.00 |
0.3829 |
0.1301 |
340.00 |
0.3942 |
0.1896 |
330.00 |
0.4864 |
0.1931 |
340.00 |
0.4927 |
0.2660 |
330.00 |
0.5695 |
0.2709 |
340.00 |
0.5763 |
0.2748 |
330.00 |
0.5736 |
0.2769 |
340.00 |
0.5809 |
0.3479 |
340.00 |
0.6413 |
0.3490 |
330.00 |
0.6329 |
0.3918 |
340.00 |
0.6675 |
0.4270 |
330.00 |
0.6857 |
0.4297 |
340.00 |
0.6912 |
0.5024 |
330.00 |
0.7257 |
0.5042 |
340.00 |
0.7353 |
0.5054 |
340.00 |
0.7376 |
0.5058 |
330.00 |
0.7266 |
0.5715 |
330.00 |
0.7609 |
0.5742 |
340.00 |
0.7705 |
0.6104 |
340.00 |
0.7901 |
0.6137 |
330.00 |
0.7797 |
0.6602 |
340.00 |
0.8122 |
0.6609 |
330.00 |
0.8035 |
0.7038 |
330.00 |
0.8239 |
0.7041 |
340.00 |
0.8336 |
0.7820 |
330.00 |
0.8618 |
0.7824 |
340.00 |
0.8720 |
0.8471 |
340.00 |
0.9048 |
0.8482 |
330.00 |
0.8975 |
0.8989 |
340.00 |
0.9341 |
0.9000 |
330.00 |
0.9283 |
0.9390 |
340.00 |
0.9583 |
0.9398 |
330.00 |
0.9541 |
0.9691 |
340.00 |
0.9782 |
0.9698 |
330.00 |
0.9761 |
0.9895 |
340.00 |
0.9924 |
0.9897 |
330.00 |
0.9915 |
1.0000 |
330.00 |
1.0000 |
1.0000 |
340.00 |
1.0000 |
Mole fraction of Isopropyl Alcohol (2)
[ref]
Fixed |
Measured |
Mole fraction of Isopropyl Alcohol (2) - Liquid |
Temperature, K - Liquid |
Mole fraction of Isopropyl Alcohol (2) - Gas |
0.0000 |
323.15 |
0.0000 |
0.0970 |
323.15 |
0.3230 |
0.1940 |
323.15 |
0.4900 |
0.2680 |
323.15 |
0.5790 |
0.3420 |
323.15 |
0.6250 |
0.4590 |
323.15 |
0.6810 |
0.6010 |
323.15 |
0.7520 |
0.6770 |
323.15 |
0.7980 |
0.7600 |
323.15 |
0.8380 |
0.8430 |
323.15 |
0.8870 |
0.8990 |
323.15 |
0.9200 |
0.9530 |
323.15 |
0.9580 |
1.0000 |
323.15 |
1.0000 |
0.0000 |
338.15 |
0.0000 |
0.1900 |
338.15 |
0.4860 |
0.2750 |
338.15 |
0.5610 |
0.4600 |
338.15 |
0.6880 |
0.5940 |
338.15 |
0.7710 |
0.6750 |
338.15 |
0.8140 |
0.7560 |
338.15 |
0.8540 |
0.8410 |
338.15 |
0.8980 |
0.8950 |
338.15 |
0.9270 |
0.9500 |
338.15 |
0.9630 |
1.0000 |
338.15 |
1.0000 |
0.0000 |
353.15 |
0.0000 |
0.0990 |
353.15 |
0.3010 |
0.3360 |
353.15 |
0.6180 |
0.3990 |
353.15 |
0.6710 |
0.4550 |
353.15 |
0.7100 |
0.5900 |
353.15 |
0.7890 |
0.6700 |
353.15 |
0.8270 |
0.7560 |
353.15 |
0.8660 |
0.8390 |
353.15 |
0.9070 |
0.8950 |
353.15 |
0.9360 |
0.9480 |
353.15 |
0.9690 |
1.0000 |
353.15 |
1.0000 |
Viscosity, Pa*s
[ref]
Operational condition: Pressure, kPa =
100 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Methyl Isobutyl Ketone (1) - Liquid |
Viscosity, Pa*s - Liquid |
293.15 |
0.0000 |
0.0024 |
293.15 |
0.0670 |
0.0017 |
293.15 |
0.1344 |
0.0014 |
293.15 |
0.2044 |
0.0011 |
293.15 |
0.3035 |
0.0010 |
293.15 |
0.3848 |
0.0009 |
293.15 |
0.5098 |
0.0007 |
293.15 |
0.5987 |
0.0007 |
293.15 |
0.6986 |
0.0007 |
293.15 |
0.8138 |
0.0006 |
293.15 |
0.9278 |
0.0006 |
293.15 |
1.0000 |
0.0006 |
298.15 |
0.0000 |
0.0021 |
298.15 |
0.0670 |
0.0015 |
298.15 |
0.1344 |
0.0012 |
298.15 |
0.2044 |
0.0010 |
298.15 |
0.3035 |
0.0009 |
298.15 |
0.3848 |
0.0008 |
298.15 |
0.5098 |
0.0007 |
298.15 |
0.5987 |
0.0006 |
298.15 |
0.6986 |
0.0006 |
298.15 |
0.8138 |
0.0006 |
298.15 |
0.9278 |
0.0006 |
298.15 |
1.0000 |
0.0006 |
303.15 |
0.0000 |
0.0018 |
303.15 |
0.0670 |
0.0013 |
303.15 |
0.1344 |
0.0011 |
303.15 |
0.2044 |
0.0009 |
303.15 |
0.3035 |
0.0008 |
303.15 |
0.3848 |
0.0007 |
303.15 |
0.5098 |
0.0006 |
303.15 |
0.5987 |
0.0006 |
303.15 |
0.6986 |
0.0006 |
303.15 |
0.8138 |
0.0005 |
303.15 |
0.9278 |
0.0005 |
303.15 |
1.0000 |
0.0005 |
308.15 |
0.0000 |
0.0016 |
308.15 |
0.0670 |
0.0012 |
308.15 |
0.1344 |
0.0010 |
308.15 |
0.2044 |
0.0008 |
308.15 |
0.3035 |
0.0007 |
308.15 |
0.3848 |
0.0007 |
308.15 |
0.5098 |
0.0006 |
308.15 |
0.5987 |
0.0006 |
308.15 |
0.6986 |
0.0005 |
308.15 |
0.8138 |
0.0005 |
308.15 |
0.9278 |
0.0005 |
308.15 |
1.0000 |
0.0005 |
313.15 |
0.0000 |
0.0014 |
313.15 |
0.0670 |
0.0011 |
313.15 |
0.1344 |
0.0009 |
313.15 |
0.2044 |
0.0008 |
313.15 |
0.3035 |
0.0007 |
313.15 |
0.3848 |
0.0006 |
313.15 |
0.5098 |
0.0006 |
313.15 |
0.5987 |
0.0005 |
313.15 |
0.6986 |
0.0005 |
313.15 |
0.8138 |
0.0005 |
313.15 |
0.9278 |
0.0005 |
313.15 |
1.0000 |
0.0005 |
318.15 |
0.0000 |
0.0012 |
318.15 |
0.0670 |
0.0009 |
318.15 |
0.1344 |
0.0008 |
318.15 |
0.2044 |
0.0007 |
318.15 |
0.3035 |
0.0006 |
318.15 |
0.3848 |
0.0006 |
318.15 |
0.5098 |
0.0005 |
318.15 |
0.5987 |
0.0005 |
318.15 |
0.6986 |
0.0005 |
318.15 |
0.8138 |
0.0005 |
318.15 |
0.9278 |
0.0004 |
318.15 |
1.0000 |
0.0004 |
323.15 |
0.0000 |
0.0010 |
323.15 |
0.0670 |
0.0008 |
323.15 |
0.1344 |
0.0007 |
323.15 |
0.2044 |
0.0006 |
323.15 |
0.3035 |
0.0006 |
323.15 |
0.3848 |
0.0005 |
323.15 |
0.5098 |
0.0005 |
323.15 |
0.5987 |
0.0005 |
323.15 |
0.6986 |
0.0004 |
323.15 |
0.8138 |
0.0004 |
323.15 |
0.9278 |
0.0004 |
323.15 |
1.0000 |
0.0004 |
Viscosity, Pa*s
[ref]
Operational condition: Pressure, kPa =
100 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Methyl Isobutyl Ketone (1) - Liquid |
Viscosity, Pa*s - Liquid |
293.15 |
0.0000 |
0.0024 |
293.15 |
0.0670 |
0.0017 |
293.15 |
0.1344 |
0.0014 |
293.15 |
0.2044 |
0.0011 |
293.15 |
0.3035 |
0.0010 |
293.15 |
0.3848 |
0.0009 |
293.15 |
0.5098 |
0.0007 |
293.15 |
0.5987 |
0.0007 |
293.15 |
0.6986 |
0.0007 |
293.15 |
0.8138 |
0.0006 |
293.15 |
0.9278 |
0.0006 |
293.15 |
1.0000 |
0.0006 |
298.15 |
0.0000 |
0.0021 |
298.15 |
0.0670 |
0.0015 |
298.15 |
0.1344 |
0.0012 |
298.15 |
0.2044 |
0.0010 |
298.15 |
0.3035 |
0.0009 |
298.15 |
0.3848 |
0.0008 |
298.15 |
0.5098 |
0.0007 |
298.15 |
0.5987 |
0.0006 |
298.15 |
0.6986 |
0.0006 |
298.15 |
0.8138 |
0.0006 |
298.15 |
0.9278 |
0.0006 |
298.15 |
1.0000 |
0.0006 |
303.15 |
0.0000 |
0.0018 |
303.15 |
0.0670 |
0.0013 |
303.15 |
0.1344 |
0.0011 |
303.15 |
0.2044 |
0.0009 |
303.15 |
0.3035 |
0.0008 |
303.15 |
0.3848 |
0.0007 |
303.15 |
0.5098 |
0.0006 |
303.15 |
0.5987 |
0.0006 |
303.15 |
0.6986 |
0.0006 |
303.15 |
0.8138 |
0.0005 |
303.15 |
0.9278 |
0.0005 |
303.15 |
1.0000 |
0.0005 |
308.15 |
0.0000 |
0.0016 |
308.15 |
0.0670 |
0.0012 |
308.15 |
0.1344 |
0.0010 |
308.15 |
0.2044 |
0.0008 |
308.15 |
0.3035 |
0.0007 |
308.15 |
0.3848 |
0.0007 |
308.15 |
0.5098 |
0.0006 |
308.15 |
0.5987 |
0.0006 |
308.15 |
0.6986 |
0.0005 |
308.15 |
0.8138 |
0.0005 |
308.15 |
0.9278 |
0.0005 |
308.15 |
1.0000 |
0.0005 |
313.15 |
0.0000 |
0.0014 |
313.15 |
0.0670 |
0.0011 |
313.15 |
0.1344 |
0.0009 |
313.15 |
0.2044 |
0.0008 |
313.15 |
0.3035 |
0.0007 |
313.15 |
0.3848 |
0.0006 |
313.15 |
0.5098 |
0.0006 |
313.15 |
0.5987 |
0.0005 |
313.15 |
0.6986 |
0.0005 |
313.15 |
0.8138 |
0.0005 |
313.15 |
0.9278 |
0.0005 |
313.15 |
1.0000 |
0.0005 |
318.15 |
0.0000 |
0.0012 |
318.15 |
0.0670 |
0.0009 |
318.15 |
0.1344 |
0.0008 |
318.15 |
0.2044 |
0.0007 |
318.15 |
0.3035 |
0.0006 |
318.15 |
0.3848 |
0.0006 |
318.15 |
0.5098 |
0.0005 |
318.15 |
0.5987 |
0.0005 |
318.15 |
0.6986 |
0.0005 |
318.15 |
0.8138 |
0.0005 |
318.15 |
0.9278 |
0.0004 |
318.15 |
1.0000 |
0.0004 |
323.15 |
0.0000 |
0.0010 |
323.15 |
0.0670 |
0.0008 |
323.15 |
0.1344 |
0.0007 |
323.15 |
0.2044 |
0.0006 |
323.15 |
0.3035 |
0.0006 |
323.15 |
0.3848 |
0.0005 |
323.15 |
0.5098 |
0.0005 |
323.15 |
0.5987 |
0.0005 |
323.15 |
0.6986 |
0.0004 |
323.15 |
0.8138 |
0.0004 |
323.15 |
0.9278 |
0.0004 |
323.15 |
1.0000 |
0.0004 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Mole fraction of Isopropyl Alcohol (2) - Liquid |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
0.0000 |
330.00 |
12.70 |
0.0000 |
340.00 |
19.27 |
0.0108 |
330.00 |
13.30 |
0.0136 |
340.00 |
20.31 |
0.0309 |
330.00 |
14.53 |
0.0378 |
340.00 |
22.16 |
0.0730 |
330.00 |
16.36 |
0.0770 |
340.00 |
24.86 |
0.1225 |
330.00 |
18.43 |
0.1301 |
340.00 |
28.04 |
0.1896 |
330.00 |
20.62 |
0.1931 |
340.00 |
31.36 |
0.2660 |
330.00 |
22.74 |
0.2709 |
340.00 |
34.71 |
0.2748 |
330.00 |
22.86 |
0.2769 |
340.00 |
34.86 |
0.3479 |
340.00 |
37.72 |
0.3490 |
330.00 |
24.57 |
0.3918 |
340.00 |
39.13 |
0.4270 |
330.00 |
26.17 |
0.4297 |
340.00 |
40.28 |
0.5024 |
330.00 |
27.47 |
0.5042 |
340.00 |
42.41 |
0.5054 |
340.00 |
42.65 |
0.5058 |
330.00 |
27.62 |
0.5715 |
330.00 |
28.56 |
0.5742 |
340.00 |
44.30 |
0.6104 |
340.00 |
45.39 |
0.6137 |
330.00 |
29.26 |
0.6602 |
340.00 |
46.28 |
0.6609 |
330.00 |
29.74 |
0.7038 |
330.00 |
30.36 |
0.7041 |
340.00 |
47.38 |
0.7820 |
330.00 |
31.31 |
0.7824 |
340.00 |
49.04 |
0.8471 |
340.00 |
50.29 |
0.8482 |
330.00 |
31.98 |
0.8989 |
340.00 |
51.25 |
0.9000 |
330.00 |
32.46 |
0.9390 |
340.00 |
51.88 |
0.9398 |
330.00 |
32.75 |
0.9691 |
340.00 |
52.36 |
0.9698 |
330.00 |
32.96 |
0.9895 |
340.00 |
52.66 |
0.9897 |
330.00 |
33.07 |
1.0000 |
330.00 |
33.25 |
1.0000 |
340.00 |
52.97 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Mole fraction of Isopropyl Alcohol (2) - Liquid |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
0.0000 |
323.15 |
9.22 |
0.0970 |
323.15 |
12.76 |
0.1940 |
323.15 |
15.07 |
0.2680 |
323.15 |
16.76 |
0.3420 |
323.15 |
17.95 |
0.4590 |
323.15 |
19.52 |
0.6010 |
323.15 |
20.99 |
0.6770 |
323.15 |
21.67 |
0.7600 |
323.15 |
22.30 |
0.8430 |
323.15 |
22.91 |
0.8990 |
323.15 |
23.14 |
0.9530 |
323.15 |
23.39 |
1.0000 |
323.15 |
23.48 |
0.0000 |
338.15 |
17.57 |
0.1900 |
338.15 |
28.92 |
0.2750 |
338.15 |
32.18 |
0.4600 |
338.15 |
38.07 |
0.5940 |
338.15 |
41.39 |
0.6750 |
338.15 |
43.03 |
0.7560 |
338.15 |
44.68 |
0.8410 |
338.15 |
46.13 |
0.8950 |
338.15 |
46.91 |
0.9500 |
338.15 |
47.71 |
1.0000 |
338.15 |
48.45 |
0.0000 |
353.15 |
31.41 |
0.0990 |
353.15 |
42.51 |
0.3360 |
353.15 |
61.56 |
0.3990 |
353.15 |
65.66 |
0.4550 |
353.15 |
69.08 |
0.5900 |
353.15 |
76.20 |
0.6700 |
353.15 |
79.66 |
0.7560 |
353.15 |
83.35 |
0.8390 |
353.15 |
86.70 |
0.8950 |
353.15 |
88.57 |
0.9480 |
353.15 |
90.61 |
1.0000 |
353.15 |
92.48 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Mole fraction of Isopropyl Alcohol (2) - Liquid |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
0.0000 |
330.00 |
12.70 |
0.0000 |
340.00 |
19.27 |
0.0108 |
330.00 |
13.30 |
0.0136 |
340.00 |
20.31 |
0.0309 |
330.00 |
14.53 |
0.0378 |
340.00 |
22.16 |
0.0730 |
330.00 |
16.36 |
0.0770 |
340.00 |
24.86 |
0.1225 |
330.00 |
18.43 |
0.1301 |
340.00 |
28.04 |
0.1896 |
330.00 |
20.62 |
0.1931 |
340.00 |
31.36 |
0.2660 |
330.00 |
22.74 |
0.2709 |
340.00 |
34.71 |
0.2748 |
330.00 |
22.86 |
0.2769 |
340.00 |
34.86 |
0.3479 |
340.00 |
37.72 |
0.3490 |
330.00 |
24.57 |
0.3918 |
340.00 |
39.13 |
0.4270 |
330.00 |
26.17 |
0.4297 |
340.00 |
40.28 |
0.5024 |
330.00 |
27.47 |
0.5042 |
340.00 |
42.41 |
0.5054 |
340.00 |
42.65 |
0.5058 |
330.00 |
27.62 |
0.5715 |
330.00 |
28.56 |
0.5742 |
340.00 |
44.30 |
0.6104 |
340.00 |
45.39 |
0.6137 |
330.00 |
29.26 |
0.6602 |
340.00 |
46.28 |
0.6609 |
330.00 |
29.74 |
0.7038 |
330.00 |
30.36 |
0.7041 |
340.00 |
47.38 |
0.7820 |
330.00 |
31.31 |
0.7824 |
340.00 |
49.04 |
0.8471 |
340.00 |
50.29 |
0.8482 |
330.00 |
31.98 |
0.8989 |
340.00 |
51.25 |
0.9000 |
330.00 |
32.46 |
0.9390 |
340.00 |
51.88 |
0.9398 |
330.00 |
32.75 |
0.9691 |
340.00 |
52.36 |
0.9698 |
330.00 |
32.96 |
0.9895 |
340.00 |
52.66 |
0.9897 |
330.00 |
33.07 |
1.0000 |
330.00 |
33.25 |
1.0000 |
340.00 |
52.97 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Mole fraction of Isopropyl Alcohol (2) - Liquid |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
0.0000 |
323.15 |
9.22 |
0.0970 |
323.15 |
12.76 |
0.1940 |
323.15 |
15.07 |
0.2680 |
323.15 |
16.76 |
0.3420 |
323.15 |
17.95 |
0.4590 |
323.15 |
19.52 |
0.6010 |
323.15 |
20.99 |
0.6770 |
323.15 |
21.67 |
0.7600 |
323.15 |
22.30 |
0.8430 |
323.15 |
22.91 |
0.8990 |
323.15 |
23.14 |
0.9530 |
323.15 |
23.39 |
1.0000 |
323.15 |
23.48 |
0.0000 |
338.15 |
17.57 |
0.1900 |
338.15 |
28.92 |
0.2750 |
338.15 |
32.18 |
0.4600 |
338.15 |
38.07 |
0.5940 |
338.15 |
41.39 |
0.6750 |
338.15 |
43.03 |
0.7560 |
338.15 |
44.68 |
0.8410 |
338.15 |
46.13 |
0.8950 |
338.15 |
46.91 |
0.9500 |
338.15 |
47.71 |
1.0000 |
338.15 |
48.45 |
0.0000 |
353.15 |
31.41 |
0.0990 |
353.15 |
42.51 |
0.3360 |
353.15 |
61.56 |
0.3990 |
353.15 |
65.66 |
0.4550 |
353.15 |
69.08 |
0.5900 |
353.15 |
76.20 |
0.6700 |
353.15 |
79.66 |
0.7560 |
353.15 |
83.35 |
0.8390 |
353.15 |
86.70 |
0.8950 |
353.15 |
88.57 |
0.9480 |
353.15 |
90.61 |
1.0000 |
353.15 |
92.48 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
100 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Methyl Isobutyl Ketone (1) - Liquid |
Mass density, kg/m3 - Liquid |
293.15 |
0.0000 |
785.4 |
293.15 |
0.0670 |
786.4 |
293.15 |
0.1344 |
787.5 |
293.15 |
0.2044 |
788.6 |
293.15 |
0.3035 |
790.2 |
293.15 |
0.3848 |
791.4 |
293.15 |
0.5098 |
793.4 |
293.15 |
0.5987 |
794.7 |
293.15 |
0.6986 |
796.3 |
293.15 |
0.8138 |
798.0 |
293.15 |
0.9278 |
799.8 |
293.15 |
1.0000 |
800.8 |
298.15 |
0.0000 |
781.1 |
298.15 |
0.0670 |
782.1 |
298.15 |
0.1344 |
783.1 |
298.15 |
0.2044 |
784.1 |
298.15 |
0.3035 |
785.6 |
298.15 |
0.3848 |
786.8 |
298.15 |
0.5098 |
788.6 |
298.15 |
0.5987 |
790.0 |
298.15 |
0.6986 |
791.5 |
298.15 |
0.8138 |
793.2 |
298.15 |
0.9278 |
795.0 |
298.15 |
1.0000 |
796.1 |
303.15 |
0.0000 |
776.8 |
303.15 |
0.0670 |
777.7 |
303.15 |
0.1344 |
778.6 |
303.15 |
0.2044 |
779.6 |
303.15 |
0.3035 |
781.0 |
303.15 |
0.3848 |
782.2 |
303.15 |
0.5098 |
784.0 |
303.15 |
0.5987 |
785.4 |
303.15 |
0.6986 |
786.9 |
303.15 |
0.8138 |
788.7 |
303.15 |
0.9278 |
790.5 |
303.15 |
1.0000 |
791.6 |
308.15 |
0.0000 |
772.4 |
308.15 |
0.0670 |
773.2 |
308.15 |
0.1344 |
774.1 |
308.15 |
0.2044 |
775.0 |
308.15 |
0.3035 |
776.4 |
308.15 |
0.3848 |
777.5 |
308.15 |
0.5098 |
779.3 |
308.15 |
0.5987 |
780.7 |
308.15 |
0.6986 |
782.2 |
308.15 |
0.8138 |
784.0 |
308.15 |
0.9278 |
785.7 |
308.15 |
1.0000 |
786.9 |
313.15 |
0.0000 |
768.0 |
313.15 |
0.0670 |
768.7 |
313.15 |
0.1344 |
769.5 |
313.15 |
0.2044 |
770.4 |
313.15 |
0.3035 |
771.8 |
313.15 |
0.3848 |
772.9 |
313.15 |
0.5098 |
774.7 |
313.15 |
0.5987 |
776.0 |
313.15 |
0.6986 |
777.5 |
313.15 |
0.8138 |
779.3 |
313.15 |
0.9278 |
781.1 |
313.15 |
1.0000 |
782.3 |
318.15 |
0.0000 |
763.4 |
318.15 |
0.0670 |
764.1 |
318.15 |
0.1344 |
764.8 |
318.15 |
0.2044 |
765.7 |
318.15 |
0.3035 |
767.0 |
318.15 |
0.3848 |
768.1 |
318.15 |
0.5098 |
769.9 |
318.15 |
0.5987 |
771.2 |
318.15 |
0.6986 |
772.7 |
318.15 |
0.8138 |
774.6 |
318.15 |
0.9278 |
776.4 |
318.15 |
1.0000 |
777.6 |
323.15 |
0.0000 |
758.8 |
323.15 |
0.0670 |
759.4 |
323.15 |
0.1344 |
760.2 |
323.15 |
0.2044 |
761.0 |
323.15 |
0.3035 |
762.3 |
323.15 |
0.3848 |
763.4 |
323.15 |
0.5098 |
765.2 |
323.15 |
0.5987 |
766.5 |
323.15 |
0.6986 |
768.1 |
323.15 |
0.8138 |
769.9 |
323.15 |
0.9278 |
771.8 |
323.15 |
1.0000 |
773.0 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
100 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Methyl Isobutyl Ketone (1) - Liquid |
Mass density, kg/m3 - Liquid |
293.15 |
0.0000 |
785.4 |
293.15 |
0.0670 |
786.4 |
293.15 |
0.1344 |
787.5 |
293.15 |
0.2044 |
788.6 |
293.15 |
0.3035 |
790.2 |
293.15 |
0.3848 |
791.4 |
293.15 |
0.5098 |
793.4 |
293.15 |
0.5987 |
794.7 |
293.15 |
0.6986 |
796.3 |
293.15 |
0.8138 |
798.0 |
293.15 |
0.9278 |
799.8 |
293.15 |
1.0000 |
800.8 |
298.15 |
0.0000 |
781.1 |
298.15 |
0.0670 |
782.1 |
298.15 |
0.1344 |
783.1 |
298.15 |
0.2044 |
784.1 |
298.15 |
0.3035 |
785.6 |
298.15 |
0.3848 |
786.8 |
298.15 |
0.5098 |
788.6 |
298.15 |
0.5987 |
790.0 |
298.15 |
0.6986 |
791.5 |
298.15 |
0.8138 |
793.2 |
298.15 |
0.9278 |
795.0 |
298.15 |
1.0000 |
796.1 |
303.15 |
0.0000 |
776.8 |
303.15 |
0.0670 |
777.7 |
303.15 |
0.1344 |
778.6 |
303.15 |
0.2044 |
779.6 |
303.15 |
0.3035 |
781.0 |
303.15 |
0.3848 |
782.2 |
303.15 |
0.5098 |
784.0 |
303.15 |
0.5987 |
785.4 |
303.15 |
0.6986 |
786.9 |
303.15 |
0.8138 |
788.7 |
303.15 |
0.9278 |
790.5 |
303.15 |
1.0000 |
791.6 |
308.15 |
0.0000 |
772.4 |
308.15 |
0.0670 |
773.2 |
308.15 |
0.1344 |
774.1 |
308.15 |
0.2044 |
775.0 |
308.15 |
0.3035 |
776.4 |
308.15 |
0.3848 |
777.5 |
308.15 |
0.5098 |
779.3 |
308.15 |
0.5987 |
780.7 |
308.15 |
0.6986 |
782.2 |
308.15 |
0.8138 |
784.0 |
308.15 |
0.9278 |
785.7 |
308.15 |
1.0000 |
786.9 |
313.15 |
0.0000 |
768.0 |
313.15 |
0.0670 |
768.7 |
313.15 |
0.1344 |
769.5 |
313.15 |
0.2044 |
770.4 |
313.15 |
0.3035 |
771.8 |
313.15 |
0.3848 |
772.9 |
313.15 |
0.5098 |
774.7 |
313.15 |
0.5987 |
776.0 |
313.15 |
0.6986 |
777.5 |
313.15 |
0.8138 |
779.3 |
313.15 |
0.9278 |
781.1 |
313.15 |
1.0000 |
782.3 |
318.15 |
0.0000 |
763.4 |
318.15 |
0.0670 |
764.1 |
318.15 |
0.1344 |
764.8 |
318.15 |
0.2044 |
765.7 |
318.15 |
0.3035 |
767.0 |
318.15 |
0.3848 |
768.1 |
318.15 |
0.5098 |
769.9 |
318.15 |
0.5987 |
771.2 |
318.15 |
0.6986 |
772.7 |
318.15 |
0.8138 |
774.6 |
318.15 |
0.9278 |
776.4 |
318.15 |
1.0000 |
777.6 |
323.15 |
0.0000 |
758.8 |
323.15 |
0.0670 |
759.4 |
323.15 |
0.1344 |
760.2 |
323.15 |
0.2044 |
761.0 |
323.15 |
0.3035 |
762.3 |
323.15 |
0.3848 |
763.4 |
323.15 |
0.5098 |
765.2 |
323.15 |
0.5987 |
766.5 |
323.15 |
0.6986 |
768.1 |
323.15 |
0.8138 |
769.9 |
323.15 |
0.9278 |
771.8 |
323.15 |
1.0000 |
773.0 |
Sources