Operational conditions:
| Molality, mol/kg of 1,3-Butanediol (2) - Liquid | Osmotic coefficient - Liquid |
|---|---|
| 0.2289 | 0.9766 |
| 0.7849 | 0.9509 |
| 1.0508 | 0.9416 |
| 2.9679 | 0.9042 |
| 2.9686 | 0.9042 |
| 4.1858 | 0.8953 |
| 4.1967 | 0.8953 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Water (1) - Liquid | Viscosity, Pa*s - Liquid |
| 298.15 | 0.0450 | 0.0926 |
| 298.15 | 0.1445 | 0.0811 |
| 298.15 | 0.2499 | 0.0676 |
| 298.15 | 0.3526 | 0.0542 |
| 298.15 | 0.4519 | 0.0417 |
| 298.15 | 0.5035 | 0.0357 |
| 298.15 | 0.5563 | 0.0299 |
| 298.15 | 0.6507 | 0.0207 |
| 298.15 | 0.7518 | 0.0126 |
| 298.15 | 0.8477 | 0.0068 |
| 298.15 | 0.9081 | 0.0040 |
| 298.15 | 0.9152 | 0.0037 |
| 298.15 | 0.9253 | 0.0033 |
| 298.15 | 0.9355 | 0.0029 |
| 298.15 | 0.9521 | 0.0023 |
| 298.15 | 0.9543 | 0.0023 |
| 298.15 | 0.9597 | 0.0021 |
| 298.15 | 0.9699 | 0.0018 |
| 298.15 | 0.9804 | 0.0014 |
| 298.15 | 0.9901 | 0.0012 |
| 298.15 | 0.9924 | 0.0011 |
| 298.15 | 0.9955 | 0.0010 |
| 308.15 | 0.0450 | 0.0499 |
| 308.15 | 0.1445 | 0.0434 |
| 308.15 | 0.2499 | 0.0361 |
| 308.15 | 0.3526 | 0.0291 |
| 308.15 | 0.4519 | 0.0227 |
| 308.15 | 0.5035 | 0.0196 |
| 308.15 | 0.5563 | 0.0166 |
| 308.15 | 0.6507 | 0.0117 |
| 308.15 | 0.7518 | 0.0072 |
| 308.15 | 0.8477 | 0.0039 |
| 308.15 | 0.9081 | 0.0023 |
| 308.15 | 0.9152 | 0.0022 |
| 308.15 | 0.9253 | 0.0020 |
| 308.15 | 0.9355 | 0.0018 |
| 308.15 | 0.9521 | 0.0014 |
| 308.15 | 0.9543 | 0.0014 |
| 308.15 | 0.9597 | 0.0013 |
| 308.15 | 0.9699 | 0.0011 |
| 308.15 | 0.9804 | 0.0010 |
| 308.15 | 0.9901 | 0.0009 |
| 308.15 | 0.9924 | 0.0008 |
| 308.15 | 0.9955 | 0.0008 |
| 318.15 | 0.0450 | 0.0289 |
| 318.15 | 0.1445 | 0.0252 |
| 318.15 | 0.2499 | 0.0208 |
| 318.15 | 0.3526 | 0.0166 |
| 318.15 | 0.4519 | 0.0128 |
| 318.15 | 0.5035 | 0.0109 |
| 318.15 | 0.5563 | 0.0092 |
| 318.15 | 0.6507 | 0.0063 |
| 318.15 | 0.7518 | 0.0039 |
| 318.15 | 0.8477 | 0.0021 |
| 318.15 | 0.9081 | 0.0013 |
| 318.15 | 0.9152 | 0.0012 |
| 318.15 | 0.9253 | 0.0011 |
| 318.15 | 0.9355 | 0.0010 |
| 318.15 | 0.9521 | 0.0009 |
| 318.15 | 0.9543 | 0.0009 |
| 318.15 | 0.9597 | 0.0008 |
| 318.15 | 0.9699 | 0.0008 |
| 318.15 | 0.9804 | 0.0007 |
| 318.15 | 0.9901 | 0.0006 |
| 318.15 | 0.9924 | 0.0006 |
| 318.15 | 0.9955 | 0.0006 |
| 328.15 | 0.0450 | 0.0179 |
| 328.15 | 0.1445 | 0.0155 |
| 328.15 | 0.2499 | 0.0127 |
| 328.15 | 0.3526 | 0.0099 |
| 328.15 | 0.4519 | 0.0075 |
| 328.15 | 0.5035 | 0.0063 |
| 328.15 | 0.5563 | 0.0052 |
| 328.15 | 0.6507 | 0.0034 |
| 328.15 | 0.7518 | 0.0020 |
| 328.15 | 0.8477 | 0.0010 |
| 328.15 | 0.9081 | 0.0007 |
| 328.15 | 0.9152 | 0.0006 |
| 328.15 | 0.9253 | 0.0006 |
| 328.15 | 0.9355 | 0.0006 |
| 328.15 | 0.9521 | 0.0005 |
| 328.15 | 0.9543 | 0.0005 |
| 328.15 | 0.9597 | 0.0005 |
| 328.15 | 0.9699 | 0.0005 |
| 328.15 | 0.9804 | 0.0005 |
| 328.15 | 0.9901 | 0.0005 |
| 328.15 | 0.9924 | 0.0005 |
| 328.15 | 0.9955 | 0.0005 |
| 338.15 | 0.0450 | 0.0116 |
| 338.15 | 0.1445 | 0.0100 |
| 338.15 | 0.2499 | 0.0080 |
| 338.15 | 0.3526 | 0.0061 |
| 338.15 | 0.4519 | 0.0044 |
| 338.15 | 0.5035 | 0.0036 |
| 338.15 | 0.5563 | 0.0029 |
| 338.15 | 0.6507 | 0.0018 |
| 338.15 | 0.7518 | 0.0009 |
| 338.15 | 0.8477 | 0.0004 |
| 338.15 | 0.9081 | 0.0003 |
| 338.15 | 0.9152 | 0.0003 |
| 338.15 | 0.9253 | 0.0003 |
| 338.15 | 0.9355 | 0.0003 |
| 338.15 | 0.9521 | 0.0003 |
| 338.15 | 0.9543 | 0.0003 |
| 338.15 | 0.9597 | 0.0003 |
| 338.15 | 0.9699 | 0.0003 |
| 338.15 | 0.9804 | 0.0004 |
| 338.15 | 0.9901 | 0.0004 |
| 338.15 | 0.9924 | 0.0004 |
| 338.15 | 0.9955 | 0.0004 |
Operational conditions:
| Fixed | Measured | |
|---|---|---|
| Initial molality of solute, mol/kg - Liquid | Final molality of solute, mol/kg - Liquid | Molar enthalpy of dilution, kJ/mol - Liquid |
| 0.4506 | 0.2101 | -0.1428 |
| 0.4979 | 0.2317 | -0.1505 |
| 0.5851 | 0.2712 | -0.1935 |
| 0.7361 | 0.3388 | -0.2571 |
| 0.9636 | 0.4390 | -0.3487 |
| 1.482 | 0.6596 | -0.5611 |
| 1.7357 | 0.7640 | -0.6683 |
| 2.4317 | 1.0389 | -0.9539 |
| 2.7568 | 1.1617 | -1.1094 |
| 3.3028 | 1.3608 | -1.3113 |
| 4.3911 | 1.7322 | -1.7495 |
| 5.1371 | 1.9691 | -2.0233 |
Operational conditions:
| Mole fraction of 1,3-Butanediol (2) - Liquid | Mass density, kg/m3 - Liquid |
|---|---|
| 0.0625 | 1008.2 |
| 0.1347 | 1015.9 |
| 0.2153 | 1019.2 |
| 0.3019 | 1018.8 |
| 0.3915 | 1016.8 |
| 0.4804 | 1014.4 |
| 0.5651 | 1012.2 |
| 0.6428 | 1009.9 |
| 0.7115 | 1007.9 |
| 0.7703 | 1006.2 |
| 0.8195 | 1004.8 |
| 0.8595 | 1003.8 |
| 0.8916 | 1003.0 |
| 0.9244 | 1002.2 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Water (1) - Liquid | Mass density, kg/m3 - Liquid |
| 298.15 | 0.0450 | 1001.0 |
| 298.15 | 0.1445 | 1003.36 |
| 298.15 | 0.2499 | 1006.05 |
| 298.15 | 0.3526 | 1008.62 |
| 298.15 | 0.4519 | 1011.07 |
| 298.15 | 0.5035 | 1012.39 |
| 298.15 | 0.5563 | 1013.79 |
| 298.15 | 0.6507 | 1016.24 |
| 298.15 | 0.7518 | 1017.77 |
| 298.15 | 0.8477 | 1015.59 |
| 298.15 | 0.9081 | 1010.74 |
| 298.15 | 0.9152 | 1009.95 |
| 298.15 | 0.9253 | 1008.73 |
| 298.15 | 0.9355 | 1007.4 |
| 298.15 | 0.9521 | 1005.03 |
| 298.15 | 0.9543 | 1004.7 |
| 298.15 | 0.9597 | 1003.86 |
| 298.15 | 0.9699 | 1002.22 |
| 298.15 | 0.9804 | 1000.46 |
| 298.15 | 0.9901 | 998.79 |
| 298.15 | 0.9924 | 998.38 |
| 298.15 | 0.9955 | 997.84 |
| 308.15 | 0.0450 | 995.14 |
| 308.15 | 0.1445 | 997.4 |
| 308.15 | 0.2499 | 999.97 |
| 308.15 | 0.3526 | 1002.45 |
| 308.15 | 0.4519 | 1004.84 |
| 308.15 | 0.5035 | 1006.14 |
| 308.15 | 0.5563 | 1007.52 |
| 308.15 | 0.6507 | 1009.99 |
| 308.15 | 0.7518 | 1011.69 |
| 308.15 | 0.8477 | 1010.07 |
| 308.15 | 0.9081 | 1005.92 |
| 308.15 | 0.9152 | 1005.23 |
| 308.15 | 0.9253 | 1004.18 |
| 308.15 | 0.9355 | 1003.02 |
| 308.15 | 0.9521 | 1000.96 |
| 308.15 | 0.9543 | 1000.67 |
| 308.15 | 0.9597 | 999.94 |
| 308.15 | 0.9699 | 998.52 |
| 308.15 | 0.9804 | 996.99 |
| 308.15 | 0.9901 | 995.53 |
| 308.15 | 0.9924 | 995.19 |
| 308.15 | 0.9955 | 994.71 |
| 318.15 | 0.0450 | 989.57 |
| 318.15 | 0.1445 | 991.66 |
| 318.15 | 0.2499 | 994.06 |
| 318.15 | 0.3526 | 996.38 |
| 318.15 | 0.4519 | 998.64 |
| 318.15 | 0.5035 | 999.86 |
| 318.15 | 0.5563 | 1001.18 |
| 318.15 | 0.6507 | 1003.55 |
| 318.15 | 0.7518 | 1005.28 |
| 318.15 | 0.8477 | 1004.06 |
| 318.15 | 0.9081 | 1000.51 |
| 318.15 | 0.9152 | 999.92 |
| 318.15 | 0.9253 | 999.0 |
| 318.15 | 0.9355 | 998.0 |
| 318.15 | 0.9521 | 996.21 |
| 318.15 | 0.9543 | 995.96 |
| 318.15 | 0.9597 | 995.33 |
| 318.15 | 0.9699 | 994.09 |
| 318.15 | 0.9804 | 992.76 |
| 318.15 | 0.9901 | 991.5 |
| 318.15 | 0.9924 | 991.2 |
| 318.15 | 0.9955 | 990.8 |
| 328.15 | 0.0450 | 980.01 |
| 328.15 | 0.1445 | 982.02 |
| 328.15 | 0.2499 | 984.33 |
| 328.15 | 0.3526 | 986.62 |
| 328.15 | 0.4519 | 988.88 |
| 328.15 | 0.5035 | 990.12 |
| 328.15 | 0.5563 | 991.47 |
| 328.15 | 0.6507 | 993.99 |
| 328.15 | 0.7518 | 996.11 |
| 328.15 | 0.8477 | 995.8 |
| 328.15 | 0.9081 | 993.31 |
| 328.15 | 0.9152 | 992.87 |
| 328.15 | 0.9253 | 992.19 |
| 328.15 | 0.9355 | 991.44 |
| 328.15 | 0.9521 | 990.11 |
| 328.15 | 0.9543 | 989.92 |
| 328.15 | 0.9597 | 989.45 |
| 328.15 | 0.9699 | 988.53 |
| 328.15 | 0.9804 | 987.55 |
| 328.15 | 0.9901 | 986.62 |
| 328.15 | 0.9924 | 986.41 |
| 328.15 | 0.9955 | 986.11 |
| 338.15 | 0.0450 | 972.67 |
| 338.15 | 0.1445 | 974.54 |
| 338.15 | 0.2499 | 976.7 |
| 338.15 | 0.3526 | 978.84 |
| 338.15 | 0.4519 | 980.99 |
| 338.15 | 0.5035 | 982.18 |
| 338.15 | 0.5563 | 983.48 |
| 338.15 | 0.6507 | 985.94 |
| 338.15 | 0.7518 | 988.14 |
| 338.15 | 0.8477 | 988.28 |
| 338.15 | 0.9081 | 986.44 |
| 338.15 | 0.9152 | 986.1 |
| 338.15 | 0.9253 | 985.58 |
| 338.15 | 0.9355 | 985.0 |
| 338.15 | 0.9521 | 983.95 |
| 338.15 | 0.9543 | 983.8 |
| 338.15 | 0.9597 | 983.44 |
| 338.15 | 0.9699 | 982.72 |
| 338.15 | 0.9804 | 981.96 |
| 338.15 | 0.9901 | 981.25 |
| 338.15 | 0.9924 | 981.09 |
| 338.15 | 0.9955 | 980.87 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Water (1) - Liquid | Speed of sound, m/s - Liquid |
| 298.15 | 0.0450 | 1544.1 |
| 298.15 | 0.1445 | 1569.1 |
| 298.15 | 0.2499 | 1594.2 |
| 298.15 | 0.3526 | 1613.2 |
| 298.15 | 0.4519 | 1631.1 |
| 298.15 | 0.5035 | 1643.5 |
| 298.15 | 0.5563 | 1652.1 |
| 298.15 | 0.6507 | 1682.0 |
| 298.15 | 0.7518 | 1702.0 |
| 298.15 | 0.8477 | 1681.6 |
| 298.15 | 0.9081 | 1673.4 |
| 298.15 | 0.9152 | 1660.2 |
| 298.15 | 0.9253 | 1645.0 |
| 298.15 | 0.9355 | 1615.2 |
| 298.15 | 0.9521 | 1610.8 |
| 298.15 | 0.9543 | 1599.6 |
| 298.15 | 0.9597 | 1576.9 |
| 298.15 | 0.9699 | 1551.3 |
| 298.15 | 0.9804 | 1525.7 |
| 298.15 | 0.9901 | 1519.4 |
| 298.15 | 0.9924 | 1510.8 |
| 298.15 | 0.9955 | 1527.6 |
| 308.15 | 0.0450 | 1500.6 |
| 308.15 | 0.1445 | 1520.3 |
| 308.15 | 0.2499 | 1538.6 |
| 308.15 | 0.3526 | 1561.8 |
| 308.15 | 0.4519 | 1585.2 |
| 308.15 | 0.5035 | 1597.0 |
| 308.15 | 0.5563 | 1609.3 |
| 308.15 | 0.6507 | 1634.5 |
| 308.15 | 0.7518 | 1666.3 |
| 308.15 | 0.8477 | 1684.0 |
| 308.15 | 0.9081 | 1665.1 |
| 308.15 | 0.9152 | 1659.9 |
| 308.15 | 0.9253 | 1657.3 |
| 308.15 | 0.9355 | 1640.7 |
| 308.15 | 0.9521 | 1619.1 |
| 308.15 | 0.9543 | 1615.8 |
| 308.15 | 0.9597 | 1607.2 |
| 308.15 | 0.9699 | 1589.0 |
| 308.15 | 0.9804 | 1567.4 |
| 308.15 | 0.9901 | 1544.6 |
| 308.15 | 0.9924 | 1536.8 |
| 308.15 | 0.9955 | 1530.7 |
| 318.15 | 0.0450 | 1474.8 |
| 318.15 | 0.1445 | 1492.5 |
| 318.15 | 0.2499 | 1509.5 |
| 318.15 | 0.3526 | 1531.8 |
| 318.15 | 0.4519 | 1554.7 |
| 318.15 | 0.5035 | 1566.6 |
| 318.15 | 0.5563 | 1579.1 |
| 318.15 | 0.6507 | 1604.8 |
| 318.15 | 0.7518 | 1638.6 |
| 318.15 | 0.8477 | 1662.4 |
| 318.15 | 0.9081 | 1652.9 |
| 318.15 | 0.9152 | 1649.3 |
| 318.15 | 0.9253 | 1643.0 |
| 318.15 | 0.9355 | 1635.1 |
| 318.15 | 0.9521 | 1618.5 |
| 318.15 | 0.9543 | 1616.0 |
| 318.15 | 0.9597 | 1609.2 |
| 318.15 | 0.9699 | 1594.8 |
| 318.15 | 0.9804 | 1577.4 |
| 318.15 | 0.9901 | 1558.9 |
| 318.15 | 0.9924 | 1554.1 |
| 318.15 | 0.9955 | 1547.5 |
| 328.15 | 0.0450 | 1456.8 |
| 328.15 | 0.1445 | 1473.0 |
| 328.15 | 0.2499 | 1489.7 |
| 328.15 | 0.3526 | 1509.9 |
| 328.15 | 0.4519 | 1530.8 |
| 328.15 | 0.5035 | 1542.3 |
| 328.15 | 0.5563 | 1554.1 |
| 328.15 | 0.6507 | 1579.6 |
| 328.15 | 0.7518 | 1612.2 |
| 328.15 | 0.8477 | 1638.8 |
| 328.15 | 0.9081 | 1635.3 |
| 328.15 | 0.9152 | 1633.0 |
| 328.15 | 0.9253 | 1628.7 |
| 328.15 | 0.9355 | 1622.5 |
| 328.15 | 0.9521 | 1610.6 |
| 328.15 | 0.9543 | 1608.3 |
| 328.15 | 0.9597 | 1603.1 |
| 328.15 | 0.9699 | 1591.7 |
| 328.15 | 0.9804 | 1578.7 |
| 328.15 | 0.9901 | 1563.6 |
| 328.15 | 0.9924 | 1559.6 |
| 328.15 | 0.9955 | 1555.0 |
| 338.15 | 0.0450 | 1438.1 |
| 338.15 | 0.1445 | 1452.7 |
| 338.15 | 0.2499 | 1468.1 |
| 338.15 | 0.3526 | 1486.2 |
| 338.15 | 0.4519 | 1506.1 |
| 338.15 | 0.5035 | 1516.1 |
| 338.15 | 0.5563 | 1527.9 |
| 338.15 | 0.6507 | 1552.0 |
| 338.15 | 0.7518 | 1584.1 |
| 338.15 | 0.8477 | 1611.3 |
| 338.15 | 0.9081 | 1614.1 |
| 338.15 | 0.9152 | 1612.4 |
| 338.15 | 0.9253 | 1609.7 |
| 338.15 | 0.9355 | 1606.3 |
| 338.15 | 0.9521 | 1597.7 |
| 338.15 | 0.9543 | 1596.6 |
| 338.15 | 0.9597 | 1592.9 |
| 338.15 | 0.9699 | 1585.4 |
| 338.15 | 0.9804 | 1575.5 |
| 338.15 | 0.9901 | 1565.5 |
| 338.15 | 0.9924 | 1561.7 |
| 338.15 | 0.9955 | 1558.4 |
Operational conditions:
| Mole fraction of 1,3-Butanediol (2) - Liquid | Excess molar volume, m3/mol - Liquid |
|---|---|
| 0.0625 | -2.1880e-07 |
| 0.1347 | -4.7070e-07 |
| 0.2153 | -6.4850e-07 |
| 0.3019 | -7.4780e-07 |
| 0.3915 | -7.7520e-07 |
| 0.4804 | -7.7060e-07 |
| 0.5651 | -7.2940e-07 |
| 0.6428 | -6.5900e-07 |
| 0.7115 | -5.7040e-07 |
| 0.7703 | -4.8740e-07 |
| 0.8195 | -4.0090e-07 |
| 0.8595 | -3.3850e-07 |
| 0.8916 | -2.8150e-07 |
| 0.9244 | -2.0500e-07 |
Note: These property values are available through the Cheméo API. A free account gives you an access key.