Datasets
-
ρl - Mass density, kg/m3 (2)
-
γ - Surface tension liquid-gas, N/m (2)
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Mole fraction of 1,6-Hexanediol (1) - Liquid |
Temperature, K - Liquid |
Mass density, kg/m3 - Liquid |
0.0000 |
283.15 |
999.7 |
0.0009 |
283.15 |
999.67 |
0.0019 |
283.15 |
999.65 |
0.0037 |
283.15 |
999.63 |
0.0054 |
283.15 |
999.64 |
0.0074 |
283.15 |
999.66 |
0.0090 |
283.15 |
999.68 |
0.0107 |
283.15 |
999.71 |
0.0125 |
283.15 |
999.76 |
0.0145 |
283.15 |
999.83 |
0.0159 |
283.15 |
999.88 |
0.0177 |
283.15 |
999.96 |
0.0349 |
283.15 |
1000.78 |
0.0514 |
283.15 |
1001.11 |
0.0694 |
283.15 |
1001.08 |
0.0983 |
283.15 |
1000.63 |
0.1120 |
283.15 |
1000.09 |
0.0000 |
288.15 |
999.1 |
0.0009 |
288.15 |
999.02 |
0.0019 |
288.15 |
998.96 |
0.0037 |
288.15 |
998.86 |
0.0054 |
288.15 |
998.8 |
0.0074 |
288.15 |
998.78 |
0.0090 |
288.15 |
998.78 |
0.0107 |
288.15 |
998.8 |
0.0125 |
288.15 |
998.83 |
0.0145 |
288.15 |
998.88 |
0.0159 |
288.15 |
998.92 |
0.0177 |
288.15 |
998.98 |
0.0349 |
288.15 |
999.42 |
0.0514 |
288.15 |
999.3 |
0.0694 |
288.15 |
998.88 |
0.0983 |
288.15 |
997.95 |
0.1120 |
288.15 |
997.54 |
0.0000 |
293.15 |
998.2 |
0.0009 |
293.15 |
998.12 |
0.0019 |
293.15 |
998.04 |
0.0037 |
293.15 |
997.92 |
0.0054 |
293.15 |
997.84 |
0.0074 |
293.15 |
997.78 |
0.0090 |
293.15 |
997.76 |
0.0107 |
293.15 |
997.72 |
0.0125 |
293.15 |
997.7 |
0.0145 |
293.15 |
997.68 |
0.0159 |
293.15 |
997.67 |
0.0177 |
293.15 |
997.66 |
0.0349 |
293.15 |
997.56 |
0.0514 |
293.15 |
997.34 |
0.0694 |
293.15 |
996.87 |
0.0983 |
293.15 |
995.62 |
0.1120 |
293.15 |
994.84 |
0.0000 |
298.15 |
997.04 |
0.0009 |
298.15 |
996.93 |
0.0019 |
298.15 |
996.83 |
0.0037 |
298.15 |
996.68 |
0.0054 |
298.15 |
996.58 |
0.0074 |
298.15 |
996.49 |
0.0090 |
298.15 |
996.43 |
0.0107 |
298.15 |
996.38 |
0.0125 |
298.15 |
996.32 |
0.0145 |
298.15 |
996.26 |
0.0159 |
298.15 |
996.23 |
0.0177 |
298.15 |
996.18 |
0.0349 |
298.15 |
995.67 |
0.0514 |
298.15 |
995.07 |
0.0694 |
298.15 |
994.3 |
0.0983 |
298.15 |
992.81 |
0.1120 |
298.15 |
992.04 |
0.0000 |
303.15 |
995.65 |
0.0009 |
303.15 |
995.54 |
0.0019 |
303.15 |
995.42 |
0.0037 |
303.15 |
995.24 |
0.0054 |
303.15 |
995.11 |
0.0074 |
303.15 |
994.99 |
0.0090 |
303.15 |
994.89 |
0.0107 |
303.15 |
994.79 |
0.0125 |
303.15 |
994.69 |
0.0145 |
303.15 |
994.59 |
0.0159 |
303.15 |
994.52 |
0.0177 |
303.15 |
994.43 |
0.0349 |
303.15 |
993.61 |
0.0514 |
303.15 |
992.8 |
0.0694 |
303.15 |
991.84 |
0.0983 |
303.15 |
990.14 |
0.1120 |
303.15 |
989.26 |
0.0000 |
308.15 |
994.03 |
0.0009 |
308.15 |
993.92 |
0.0019 |
308.15 |
993.78 |
0.0037 |
308.15 |
993.57 |
0.0054 |
308.15 |
993.41 |
0.0074 |
308.15 |
993.24 |
0.0090 |
308.15 |
993.11 |
0.0107 |
308.15 |
992.99 |
0.0125 |
308.15 |
992.87 |
0.0145 |
308.15 |
992.74 |
0.0159 |
308.15 |
992.65 |
0.0177 |
308.15 |
992.54 |
0.0349 |
308.15 |
991.57 |
0.0514 |
308.15 |
990.58 |
0.0694 |
308.15 |
989.39 |
0.0983 |
308.15 |
987.3 |
0.1120 |
308.15 |
986.33 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Mole fraction of 1,6-Hexanediol (1) - Liquid |
Temperature, K - Liquid |
Mass density, kg/m3 - Liquid |
0.0000 |
283.15 |
999.7 |
0.0009 |
283.15 |
999.67 |
0.0019 |
283.15 |
999.65 |
0.0037 |
283.15 |
999.63 |
0.0054 |
283.15 |
999.64 |
0.0074 |
283.15 |
999.66 |
0.0090 |
283.15 |
999.68 |
0.0107 |
283.15 |
999.71 |
0.0125 |
283.15 |
999.76 |
0.0145 |
283.15 |
999.83 |
0.0159 |
283.15 |
999.88 |
0.0177 |
283.15 |
999.96 |
0.0349 |
283.15 |
1000.78 |
0.0514 |
283.15 |
1001.11 |
0.0694 |
283.15 |
1001.08 |
0.0983 |
283.15 |
1000.63 |
0.1120 |
283.15 |
1000.09 |
0.0000 |
288.15 |
999.1 |
0.0009 |
288.15 |
999.02 |
0.0019 |
288.15 |
998.96 |
0.0037 |
288.15 |
998.86 |
0.0054 |
288.15 |
998.8 |
0.0074 |
288.15 |
998.78 |
0.0090 |
288.15 |
998.78 |
0.0107 |
288.15 |
998.8 |
0.0125 |
288.15 |
998.83 |
0.0145 |
288.15 |
998.88 |
0.0159 |
288.15 |
998.92 |
0.0177 |
288.15 |
998.98 |
0.0349 |
288.15 |
999.42 |
0.0514 |
288.15 |
999.3 |
0.0694 |
288.15 |
998.88 |
0.0983 |
288.15 |
997.95 |
0.1120 |
288.15 |
997.54 |
0.0000 |
293.15 |
998.2 |
0.0009 |
293.15 |
998.12 |
0.0019 |
293.15 |
998.04 |
0.0037 |
293.15 |
997.92 |
0.0054 |
293.15 |
997.84 |
0.0074 |
293.15 |
997.78 |
0.0090 |
293.15 |
997.76 |
0.0107 |
293.15 |
997.72 |
0.0125 |
293.15 |
997.7 |
0.0145 |
293.15 |
997.68 |
0.0159 |
293.15 |
997.67 |
0.0177 |
293.15 |
997.66 |
0.0349 |
293.15 |
997.56 |
0.0514 |
293.15 |
997.34 |
0.0694 |
293.15 |
996.87 |
0.0983 |
293.15 |
995.62 |
0.1120 |
293.15 |
994.84 |
0.0000 |
298.15 |
997.04 |
0.0009 |
298.15 |
996.93 |
0.0019 |
298.15 |
996.83 |
0.0037 |
298.15 |
996.68 |
0.0054 |
298.15 |
996.58 |
0.0074 |
298.15 |
996.49 |
0.0090 |
298.15 |
996.43 |
0.0107 |
298.15 |
996.38 |
0.0125 |
298.15 |
996.32 |
0.0145 |
298.15 |
996.26 |
0.0159 |
298.15 |
996.23 |
0.0177 |
298.15 |
996.18 |
0.0349 |
298.15 |
995.67 |
0.0514 |
298.15 |
995.07 |
0.0694 |
298.15 |
994.3 |
0.0983 |
298.15 |
992.81 |
0.1120 |
298.15 |
992.04 |
0.0000 |
303.15 |
995.65 |
0.0009 |
303.15 |
995.54 |
0.0019 |
303.15 |
995.42 |
0.0037 |
303.15 |
995.24 |
0.0054 |
303.15 |
995.11 |
0.0074 |
303.15 |
994.99 |
0.0090 |
303.15 |
994.89 |
0.0107 |
303.15 |
994.79 |
0.0125 |
303.15 |
994.69 |
0.0145 |
303.15 |
994.59 |
0.0159 |
303.15 |
994.52 |
0.0177 |
303.15 |
994.43 |
0.0349 |
303.15 |
993.61 |
0.0514 |
303.15 |
992.8 |
0.0694 |
303.15 |
991.84 |
0.0983 |
303.15 |
990.14 |
0.1120 |
303.15 |
989.26 |
0.0000 |
308.15 |
994.03 |
0.0009 |
308.15 |
993.92 |
0.0019 |
308.15 |
993.78 |
0.0037 |
308.15 |
993.57 |
0.0054 |
308.15 |
993.41 |
0.0074 |
308.15 |
993.24 |
0.0090 |
308.15 |
993.11 |
0.0107 |
308.15 |
992.99 |
0.0125 |
308.15 |
992.87 |
0.0145 |
308.15 |
992.74 |
0.0159 |
308.15 |
992.65 |
0.0177 |
308.15 |
992.54 |
0.0349 |
308.15 |
991.57 |
0.0514 |
308.15 |
990.58 |
0.0694 |
308.15 |
989.39 |
0.0983 |
308.15 |
987.3 |
0.1120 |
308.15 |
986.33 |
Surface tension liquid-gas, N/m
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of 1,6-Hexanediol (1) - Liquid |
Surface tension liquid-gas, N/m - Liquid |
283.15 |
0.0000 |
0.0741 |
283.15 |
0.0013 |
0.0638 |
283.15 |
0.0017 |
0.0625 |
283.15 |
0.0021 |
0.0615 |
283.15 |
0.0029 |
0.0600 |
283.15 |
0.0057 |
0.0569 |
283.15 |
0.0070 |
0.0551 |
283.15 |
0.0089 |
0.0533 |
283.15 |
0.0140 |
0.0506 |
283.15 |
0.0159 |
0.0494 |
283.15 |
0.0237 |
0.0485 |
283.15 |
0.0373 |
0.0461 |
283.15 |
0.0463 |
0.0444 |
283.15 |
0.0545 |
0.0437 |
283.15 |
0.0742 |
0.0435 |
283.15 |
0.0980 |
0.0434 |
283.15 |
0.1165 |
0.0434 |
288.15 |
0.0000 |
0.0734 |
288.15 |
0.0013 |
0.0631 |
288.15 |
0.0017 |
0.0618 |
288.15 |
0.0021 |
0.0607 |
288.15 |
0.0029 |
0.0592 |
288.15 |
0.0057 |
0.0557 |
288.15 |
0.0070 |
0.0543 |
288.15 |
0.0089 |
0.0524 |
288.15 |
0.0140 |
0.0494 |
288.15 |
0.0159 |
0.0486 |
288.15 |
0.0237 |
0.0476 |
288.15 |
0.0373 |
0.0457 |
288.15 |
0.0463 |
0.0441 |
288.15 |
0.0545 |
0.0434 |
288.15 |
0.0742 |
0.0433 |
288.15 |
0.0980 |
0.0431 |
288.15 |
0.1165 |
0.0431 |
293.15 |
0.0000 |
0.0726 |
293.15 |
0.0013 |
0.0623 |
293.15 |
0.0017 |
0.0612 |
293.15 |
0.0021 |
0.0603 |
293.15 |
0.0029 |
0.0586 |
293.15 |
0.0057 |
0.0550 |
293.15 |
0.0070 |
0.0534 |
293.15 |
0.0089 |
0.0514 |
293.15 |
0.0140 |
0.0491 |
293.15 |
0.0159 |
0.0480 |
293.15 |
0.0237 |
0.0470 |
293.15 |
0.0373 |
0.0454 |
293.15 |
0.0463 |
0.0439 |
293.15 |
0.0545 |
0.0432 |
293.15 |
0.0742 |
0.0430 |
293.15 |
0.0980 |
0.0429 |
293.15 |
0.1165 |
0.0428 |
298.15 |
0.0000 |
0.0718 |
298.15 |
0.0013 |
0.0620 |
298.15 |
0.0017 |
0.0604 |
298.15 |
0.0021 |
0.0594 |
298.15 |
0.0029 |
0.0575 |
298.15 |
0.0057 |
0.0538 |
298.15 |
0.0070 |
0.0521 |
298.15 |
0.0089 |
0.0502 |
298.15 |
0.0140 |
0.0483 |
298.15 |
0.0159 |
0.0475 |
298.15 |
0.0237 |
0.0465 |
298.15 |
0.0373 |
0.0450 |
298.15 |
0.0463 |
0.0436 |
298.15 |
0.0545 |
0.0429 |
298.15 |
0.0742 |
0.0428 |
298.15 |
0.0980 |
0.0427 |
298.15 |
0.1165 |
0.0426 |
303.15 |
0.0000 |
0.0710 |
303.15 |
0.0013 |
0.0611 |
303.15 |
0.0017 |
0.0597 |
303.15 |
0.0021 |
0.0585 |
303.15 |
0.0029 |
0.0568 |
303.15 |
0.0057 |
0.0533 |
303.15 |
0.0070 |
0.0517 |
303.15 |
0.0089 |
0.0500 |
303.15 |
0.0140 |
0.0483 |
303.15 |
0.0159 |
0.0470 |
303.15 |
0.0237 |
0.0461 |
303.15 |
0.0373 |
0.0445 |
303.15 |
0.0463 |
0.0433 |
303.15 |
0.0545 |
0.0425 |
303.15 |
0.0742 |
0.0424 |
303.15 |
0.0980 |
0.0424 |
303.15 |
0.1165 |
0.0423 |
308.15 |
0.0000 |
0.0702 |
308.15 |
0.0013 |
0.0606 |
308.15 |
0.0017 |
0.0588 |
308.15 |
0.0021 |
0.0576 |
308.15 |
0.0029 |
0.0560 |
308.15 |
0.0057 |
0.0524 |
308.15 |
0.0070 |
0.0509 |
308.15 |
0.0089 |
0.0494 |
308.15 |
0.0140 |
0.0472 |
308.15 |
0.0159 |
0.0466 |
308.15 |
0.0237 |
0.0458 |
308.15 |
0.0373 |
0.0442 |
308.15 |
0.0463 |
0.0430 |
308.15 |
0.0545 |
0.0422 |
308.15 |
0.0742 |
0.0421 |
308.15 |
0.0980 |
0.0421 |
308.15 |
0.1165 |
0.0420 |
Surface tension liquid-gas, N/m
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of 1,6-Hexanediol (1) - Liquid |
Surface tension liquid-gas, N/m - Liquid |
283.15 |
0.0000 |
0.0741 |
283.15 |
0.0013 |
0.0638 |
283.15 |
0.0017 |
0.0625 |
283.15 |
0.0021 |
0.0615 |
283.15 |
0.0029 |
0.0600 |
283.15 |
0.0057 |
0.0569 |
283.15 |
0.0070 |
0.0551 |
283.15 |
0.0089 |
0.0533 |
283.15 |
0.0140 |
0.0506 |
283.15 |
0.0159 |
0.0494 |
283.15 |
0.0237 |
0.0485 |
283.15 |
0.0373 |
0.0461 |
283.15 |
0.0463 |
0.0444 |
283.15 |
0.0545 |
0.0437 |
283.15 |
0.0742 |
0.0435 |
283.15 |
0.0980 |
0.0434 |
283.15 |
0.1165 |
0.0434 |
288.15 |
0.0000 |
0.0734 |
288.15 |
0.0013 |
0.0631 |
288.15 |
0.0017 |
0.0618 |
288.15 |
0.0021 |
0.0607 |
288.15 |
0.0029 |
0.0592 |
288.15 |
0.0057 |
0.0557 |
288.15 |
0.0070 |
0.0543 |
288.15 |
0.0089 |
0.0524 |
288.15 |
0.0140 |
0.0494 |
288.15 |
0.0159 |
0.0486 |
288.15 |
0.0237 |
0.0476 |
288.15 |
0.0373 |
0.0457 |
288.15 |
0.0463 |
0.0441 |
288.15 |
0.0545 |
0.0434 |
288.15 |
0.0742 |
0.0433 |
288.15 |
0.0980 |
0.0431 |
288.15 |
0.1165 |
0.0431 |
293.15 |
0.0000 |
0.0726 |
293.15 |
0.0013 |
0.0623 |
293.15 |
0.0017 |
0.0612 |
293.15 |
0.0021 |
0.0603 |
293.15 |
0.0029 |
0.0586 |
293.15 |
0.0057 |
0.0550 |
293.15 |
0.0070 |
0.0534 |
293.15 |
0.0089 |
0.0514 |
293.15 |
0.0140 |
0.0491 |
293.15 |
0.0159 |
0.0480 |
293.15 |
0.0237 |
0.0470 |
293.15 |
0.0373 |
0.0454 |
293.15 |
0.0463 |
0.0439 |
293.15 |
0.0545 |
0.0432 |
293.15 |
0.0742 |
0.0430 |
293.15 |
0.0980 |
0.0429 |
293.15 |
0.1165 |
0.0428 |
298.15 |
0.0000 |
0.0718 |
298.15 |
0.0013 |
0.0620 |
298.15 |
0.0017 |
0.0604 |
298.15 |
0.0021 |
0.0594 |
298.15 |
0.0029 |
0.0575 |
298.15 |
0.0057 |
0.0538 |
298.15 |
0.0070 |
0.0521 |
298.15 |
0.0089 |
0.0502 |
298.15 |
0.0140 |
0.0483 |
298.15 |
0.0159 |
0.0475 |
298.15 |
0.0237 |
0.0465 |
298.15 |
0.0373 |
0.0450 |
298.15 |
0.0463 |
0.0436 |
298.15 |
0.0545 |
0.0429 |
298.15 |
0.0742 |
0.0428 |
298.15 |
0.0980 |
0.0427 |
298.15 |
0.1165 |
0.0426 |
303.15 |
0.0000 |
0.0710 |
303.15 |
0.0013 |
0.0611 |
303.15 |
0.0017 |
0.0597 |
303.15 |
0.0021 |
0.0585 |
303.15 |
0.0029 |
0.0568 |
303.15 |
0.0057 |
0.0533 |
303.15 |
0.0070 |
0.0517 |
303.15 |
0.0089 |
0.0500 |
303.15 |
0.0140 |
0.0483 |
303.15 |
0.0159 |
0.0470 |
303.15 |
0.0237 |
0.0461 |
303.15 |
0.0373 |
0.0445 |
303.15 |
0.0463 |
0.0433 |
303.15 |
0.0545 |
0.0425 |
303.15 |
0.0742 |
0.0424 |
303.15 |
0.0980 |
0.0424 |
303.15 |
0.1165 |
0.0423 |
308.15 |
0.0000 |
0.0702 |
308.15 |
0.0013 |
0.0606 |
308.15 |
0.0017 |
0.0588 |
308.15 |
0.0021 |
0.0576 |
308.15 |
0.0029 |
0.0560 |
308.15 |
0.0057 |
0.0524 |
308.15 |
0.0070 |
0.0509 |
308.15 |
0.0089 |
0.0494 |
308.15 |
0.0140 |
0.0472 |
308.15 |
0.0159 |
0.0466 |
308.15 |
0.0237 |
0.0458 |
308.15 |
0.0373 |
0.0442 |
308.15 |
0.0463 |
0.0430 |
308.15 |
0.0545 |
0.0422 |
308.15 |
0.0742 |
0.0421 |
308.15 |
0.0980 |
0.0421 |
308.15 |
0.1165 |
0.0420 |
Sources
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Effect of temperature on the surface tension of diluted aqueous solutions of 1,2-hexanediol, 1,5-hexanediol, 1,6-hexanediol and 2,5-hexanediol
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Effect of temperature on the volumetric properties of dilute aqueous solutions of 1,2-hexanediol, 1,5-hexanediol, 1,6-hexanediol, and 2,5-hexanediol