Datasets
-
Mole fraction (2)
-
ρl - Mass density, kg/m3 (2)
-
csound,fluid - Speed of Sound, m/s (2)
-
Tboil - Boiling temperature at pressure P, K (2)
Mole fraction of 1,3-Dioxolane (2)
[ref]
Fixed |
Measured |
Mole fraction of 1,3-Dioxolane (2) - Liquid |
Pressure, kPa - Gas |
Mole fraction of 1,3-Dioxolane (2) - Gas |
0.0154 |
40.00 |
0.0439 |
0.0206 |
101.30 |
0.0603 |
0.0819 |
40.00 |
0.1869 |
0.1210 |
101.30 |
0.2052 |
0.1725 |
101.30 |
0.2643 |
0.1808 |
40.00 |
0.3343 |
0.2436 |
40.00 |
0.4144 |
0.2437 |
101.30 |
0.3397 |
0.3372 |
40.00 |
0.5048 |
0.3630 |
101.30 |
0.4428 |
0.5056 |
101.30 |
0.5627 |
0.5159 |
40.00 |
0.6338 |
0.5631 |
40.00 |
0.6607 |
0.5672 |
101.30 |
0.6148 |
0.6011 |
101.30 |
0.6319 |
0.6018 |
40.00 |
0.6862 |
0.7104 |
101.30 |
0.7243 |
0.7114 |
40.00 |
0.7548 |
0.7534 |
40.00 |
0.7846 |
0.7535 |
101.30 |
0.7589 |
0.8450 |
40.00 |
0.8787 |
0.8452 |
101.30 |
0.8363 |
0.8870 |
101.30 |
0.8749 |
0.8881 |
40.00 |
0.8858 |
0.9547 |
40.00 |
0.9486 |
0.9548 |
101.30 |
0.9457 |
Mole fraction of 1,3-Dioxolane (2)
[ref]
Fixed |
Measured |
Mole fraction of 1,3-Dioxolane (2) - Liquid |
Pressure, kPa - Gas |
Mole fraction of 1,3-Dioxolane (2) - Gas |
0.0154 |
40.00 |
0.0439 |
0.0206 |
101.30 |
0.0603 |
0.0819 |
40.00 |
0.1869 |
0.1210 |
101.30 |
0.2052 |
0.1725 |
101.30 |
0.2643 |
0.1808 |
40.00 |
0.3343 |
0.2436 |
40.00 |
0.4144 |
0.2437 |
101.30 |
0.3397 |
0.3372 |
40.00 |
0.5048 |
0.3630 |
101.30 |
0.4428 |
0.5056 |
101.30 |
0.5627 |
0.5159 |
40.00 |
0.6338 |
0.5631 |
40.00 |
0.6607 |
0.5672 |
101.30 |
0.6148 |
0.6011 |
101.30 |
0.6319 |
0.6018 |
40.00 |
0.6862 |
0.7104 |
101.30 |
0.7243 |
0.7114 |
40.00 |
0.7548 |
0.7534 |
40.00 |
0.7846 |
0.7535 |
101.30 |
0.7589 |
0.8450 |
40.00 |
0.8787 |
0.8452 |
101.30 |
0.8363 |
0.8870 |
101.30 |
0.8749 |
0.8881 |
40.00 |
0.8858 |
0.9547 |
40.00 |
0.9486 |
0.9548 |
101.30 |
0.9457 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of 1,3-Dioxolane (2) - Liquid |
Mass density, kg/m3 - Liquid |
298.15 |
0.0495 |
789.79 |
298.15 |
0.0965 |
798.83 |
298.15 |
0.1996 |
820.33 |
298.15 |
0.2909 |
840.96 |
298.15 |
0.4049 |
868.7 |
298.15 |
0.4972 |
892.83 |
298.15 |
0.5974 |
920.82 |
298.15 |
0.7033 |
952.73 |
298.15 |
0.8033 |
985.46 |
298.15 |
0.8944 |
1017.75 |
298.15 |
0.9439 |
1036.49 |
313.15 |
0.0567 |
775.49 |
313.15 |
0.0949 |
782.77 |
313.15 |
0.1973 |
803.78 |
313.15 |
0.2919 |
824.8 |
313.15 |
0.4039 |
851.81 |
313.15 |
0.4951 |
875.4 |
313.15 |
0.5948 |
903.12 |
313.15 |
0.6997 |
934.45 |
313.15 |
0.8031 |
967.86 |
313.15 |
0.8959 |
1000.17 |
313.15 |
0.9464 |
1018.99 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of 1,3-Dioxolane (2) - Liquid |
Mass density, kg/m3 - Liquid |
298.15 |
0.0495 |
789.79 |
298.15 |
0.0965 |
798.83 |
298.15 |
0.1996 |
820.33 |
298.15 |
0.2909 |
840.96 |
298.15 |
0.4049 |
868.7 |
298.15 |
0.4972 |
892.83 |
298.15 |
0.5974 |
920.82 |
298.15 |
0.7033 |
952.73 |
298.15 |
0.8033 |
985.46 |
298.15 |
0.8944 |
1017.75 |
298.15 |
0.9439 |
1036.49 |
313.15 |
0.0567 |
775.49 |
313.15 |
0.0949 |
782.77 |
313.15 |
0.1973 |
803.78 |
313.15 |
0.2919 |
824.8 |
313.15 |
0.4039 |
851.81 |
313.15 |
0.4951 |
875.4 |
313.15 |
0.5948 |
903.12 |
313.15 |
0.6997 |
934.45 |
313.15 |
0.8031 |
967.86 |
313.15 |
0.8959 |
1000.17 |
313.15 |
0.9464 |
1018.99 |
Speed of sound, m/s
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of 1,3-Dioxolane (2) - Liquid |
Speed of sound, m/s - Liquid |
298.15 |
0.0495 |
1129.2 |
298.15 |
0.0965 |
1135.6 |
298.15 |
0.1996 |
1151.0 |
298.15 |
0.2909 |
1165.8 |
298.15 |
0.4049 |
1186.2 |
298.15 |
0.4972 |
1204.9 |
298.15 |
0.5974 |
1226.8 |
298.15 |
0.7033 |
1252.5 |
298.15 |
0.8033 |
1279.3 |
298.15 |
0.8944 |
1305.9 |
298.15 |
0.9439 |
1321.3 |
313.15 |
0.0567 |
1065.2 |
313.15 |
0.0949 |
1071.1 |
313.15 |
0.1973 |
1087.4 |
313.15 |
0.2919 |
1103.5 |
313.15 |
0.4039 |
1123.4 |
313.15 |
0.4951 |
1141.2 |
313.15 |
0.5948 |
1162.4 |
313.15 |
0.6997 |
1187.1 |
313.15 |
0.8031 |
1213.5 |
313.15 |
0.8959 |
1239.6 |
313.15 |
0.9464 |
1254.3 |
Speed of sound, m/s
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of 1,3-Dioxolane (2) - Liquid |
Speed of sound, m/s - Liquid |
298.15 |
0.0495 |
1129.2 |
298.15 |
0.0965 |
1135.6 |
298.15 |
0.1996 |
1151.0 |
298.15 |
0.2909 |
1165.8 |
298.15 |
0.4049 |
1186.2 |
298.15 |
0.4972 |
1204.9 |
298.15 |
0.5974 |
1226.8 |
298.15 |
0.7033 |
1252.5 |
298.15 |
0.8033 |
1279.3 |
298.15 |
0.8944 |
1305.9 |
298.15 |
0.9439 |
1321.3 |
313.15 |
0.0567 |
1065.2 |
313.15 |
0.0949 |
1071.1 |
313.15 |
0.1973 |
1087.4 |
313.15 |
0.2919 |
1103.5 |
313.15 |
0.4039 |
1123.4 |
313.15 |
0.4951 |
1141.2 |
313.15 |
0.5948 |
1162.4 |
313.15 |
0.6997 |
1187.1 |
313.15 |
0.8031 |
1213.5 |
313.15 |
0.8959 |
1239.6 |
313.15 |
0.9464 |
1254.3 |
Boiling temperature at pressure P, K
[ref]
Fixed |
Measured |
Mole fraction of 1,3-Dioxolane (2) - Liquid |
Pressure, kPa - Liquid |
Boiling temperature at pressure P, K - Liquid |
0.0154 |
40.00 |
333.27 |
0.0206 |
101.30 |
354.19 |
0.0819 |
40.00 |
331.10 |
0.1210 |
101.30 |
352.15 |
0.1725 |
101.30 |
351.89 |
0.1808 |
40.00 |
328.67 |
0.2436 |
40.00 |
327.13 |
0.2437 |
101.30 |
351.02 |
0.3372 |
40.00 |
326.14 |
0.3630 |
101.30 |
349.80 |
0.5056 |
101.30 |
348.63 |
0.5159 |
40.00 |
324.39 |
0.5631 |
40.00 |
324.16 |
0.5672 |
101.30 |
348.38 |
0.6011 |
101.30 |
348.26 |
0.6018 |
40.00 |
323.78 |
0.7104 |
101.30 |
347.91 |
0.7114 |
40.00 |
323.32 |
0.7534 |
40.00 |
323.18 |
0.7535 |
101.30 |
347.88 |
0.8450 |
40.00 |
322.94 |
0.8452 |
101.30 |
347.90 |
0.8870 |
101.30 |
348.05 |
0.8881 |
40.00 |
322.95 |
0.9547 |
40.00 |
323.04 |
0.9548 |
101.30 |
348.28 |
Boiling temperature at pressure P, K
[ref]
Fixed |
Measured |
Mole fraction of 1,3-Dioxolane (2) - Liquid |
Pressure, kPa - Liquid |
Boiling temperature at pressure P, K - Liquid |
0.0154 |
40.00 |
333.27 |
0.0206 |
101.30 |
354.19 |
0.0819 |
40.00 |
331.10 |
0.1210 |
101.30 |
352.15 |
0.1725 |
101.30 |
351.89 |
0.1808 |
40.00 |
328.67 |
0.2436 |
40.00 |
327.13 |
0.2437 |
101.30 |
351.02 |
0.3372 |
40.00 |
326.14 |
0.3630 |
101.30 |
349.80 |
0.5056 |
101.30 |
348.63 |
0.5159 |
40.00 |
324.39 |
0.5631 |
40.00 |
324.16 |
0.5672 |
101.30 |
348.38 |
0.6011 |
101.30 |
348.26 |
0.6018 |
40.00 |
323.78 |
0.7104 |
101.30 |
347.91 |
0.7114 |
40.00 |
323.32 |
0.7534 |
40.00 |
323.18 |
0.7535 |
101.30 |
347.88 |
0.8450 |
40.00 |
322.94 |
0.8452 |
101.30 |
347.90 |
0.8870 |
101.30 |
348.05 |
0.8881 |
40.00 |
322.95 |
0.9547 |
40.00 |
323.04 |
0.9548 |
101.30 |
348.28 |
Sources