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 1,4-Butanediol (1)
[ref]
Fixed |
Measured |
Mole fraction of 1,4-Butanediol (1) - Liquid |
Pressure, kPa - Liquid |
Mole fraction of 1,4-Butanediol (1) - Gas |
0.0000 |
10.00 |
0.0000 |
0.0920 |
10.00 |
0.1340 |
0.1780 |
10.00 |
0.2340 |
0.2840 |
10.00 |
0.3580 |
0.3250 |
10.00 |
0.4040 |
0.3780 |
10.00 |
0.4620 |
0.4460 |
10.00 |
0.5310 |
0.5270 |
10.00 |
0.6090 |
0.5890 |
10.00 |
0.6680 |
0.6940 |
10.00 |
0.7620 |
0.7960 |
10.00 |
0.8500 |
0.9060 |
10.00 |
0.9370 |
1.0000 |
10.00 |
1.0000 |
0.0000 |
20.00 |
0.0000 |
0.1180 |
20.00 |
0.1580 |
0.1920 |
20.00 |
0.2510 |
0.2580 |
20.00 |
0.3300 |
0.3130 |
20.00 |
0.3920 |
0.3730 |
20.00 |
0.4580 |
0.4410 |
20.00 |
0.5300 |
0.5140 |
20.00 |
0.6050 |
0.5750 |
20.00 |
0.6640 |
0.6890 |
20.00 |
0.7670 |
0.8100 |
20.00 |
0.8690 |
0.9150 |
20.00 |
0.9460 |
1.0000 |
20.00 |
1.0000 |
0.0000 |
40.00 |
0.0000 |
0.0670 |
40.00 |
0.1070 |
0.1400 |
40.00 |
0.2060 |
0.2010 |
40.00 |
0.2840 |
0.2830 |
40.00 |
0.3780 |
0.3640 |
40.00 |
0.4680 |
0.4560 |
40.00 |
0.5600 |
0.5520 |
40.00 |
0.6520 |
0.6490 |
40.00 |
0.7340 |
0.7360 |
40.00 |
0.8040 |
0.8270 |
40.00 |
0.8750 |
0.9150 |
40.00 |
0.9380 |
1.0000 |
40.00 |
1.0000 |
Mole fraction of 1,4-Butanediol (1)
[ref]
Fixed |
Measured |
Mole fraction of 1,4-Butanediol (1) - Liquid |
Pressure, kPa - Liquid |
Mole fraction of 1,4-Butanediol (1) - Gas |
0.0000 |
10.00 |
0.0000 |
0.0920 |
10.00 |
0.1340 |
0.1780 |
10.00 |
0.2340 |
0.2840 |
10.00 |
0.3580 |
0.3250 |
10.00 |
0.4040 |
0.3780 |
10.00 |
0.4620 |
0.4460 |
10.00 |
0.5310 |
0.5270 |
10.00 |
0.6090 |
0.5890 |
10.00 |
0.6680 |
0.6940 |
10.00 |
0.7620 |
0.7960 |
10.00 |
0.8500 |
0.9060 |
10.00 |
0.9370 |
1.0000 |
10.00 |
1.0000 |
0.0000 |
20.00 |
0.0000 |
0.1180 |
20.00 |
0.1580 |
0.1920 |
20.00 |
0.2510 |
0.2580 |
20.00 |
0.3300 |
0.3130 |
20.00 |
0.3920 |
0.3730 |
20.00 |
0.4580 |
0.4410 |
20.00 |
0.5300 |
0.5140 |
20.00 |
0.6050 |
0.5750 |
20.00 |
0.6640 |
0.6890 |
20.00 |
0.7670 |
0.8100 |
20.00 |
0.8690 |
0.9150 |
20.00 |
0.9460 |
1.0000 |
20.00 |
1.0000 |
0.0000 |
40.00 |
0.0000 |
0.0670 |
40.00 |
0.1070 |
0.1400 |
40.00 |
0.2060 |
0.2010 |
40.00 |
0.2840 |
0.2830 |
40.00 |
0.3780 |
0.3640 |
40.00 |
0.4680 |
0.4560 |
40.00 |
0.5600 |
0.5520 |
40.00 |
0.6520 |
0.6490 |
40.00 |
0.7340 |
0.7360 |
40.00 |
0.8040 |
0.8270 |
40.00 |
0.8750 |
0.9150 |
40.00 |
0.9380 |
1.0000 |
40.00 |
1.0000 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethanol, 2,2'-oxybis- (2) - Liquid |
Mass density, kg/m3 - Liquid |
298.15 |
0.0000 |
1012.6 |
298.15 |
0.1080 |
1019.9 |
298.15 |
0.1977 |
1026.6 |
298.15 |
0.2897 |
1035.0 |
298.15 |
0.4096 |
1047.0 |
298.15 |
0.5090 |
1057.6 |
298.15 |
0.6116 |
1069.4 |
298.15 |
0.6912 |
1078.5 |
298.15 |
0.7992 |
1090.6 |
298.15 |
0.8838 |
1100.0 |
298.15 |
1.0000 |
1112.7 |
303.15 |
0.0000 |
1009.6 |
303.15 |
0.1080 |
1017.1 |
303.15 |
0.1977 |
1024.0 |
303.15 |
0.2897 |
1032.3 |
303.15 |
0.4096 |
1044.3 |
303.15 |
0.5090 |
1054.9 |
303.15 |
0.6116 |
1066.5 |
303.15 |
0.6912 |
1075.6 |
303.15 |
0.7992 |
1087.6 |
303.15 |
0.8838 |
1096.8 |
303.15 |
1.0000 |
1109.3 |
308.15 |
0.0000 |
1006.7 |
308.15 |
0.1080 |
1014.4 |
308.15 |
0.1977 |
1021.4 |
308.15 |
0.2897 |
1029.6 |
308.15 |
0.4096 |
1041.6 |
308.15 |
0.5090 |
1052.1 |
308.15 |
0.6116 |
1063.7 |
308.15 |
0.6912 |
1072.6 |
308.15 |
0.7992 |
1084.5 |
308.15 |
0.8838 |
1093.6 |
308.15 |
1.0000 |
1105.9 |
313.15 |
0.0000 |
1003.7 |
313.15 |
0.1080 |
1011.7 |
313.15 |
0.1977 |
1018.7 |
313.15 |
0.2897 |
1027.0 |
313.15 |
0.4096 |
1038.9 |
313.15 |
0.5090 |
1049.4 |
313.15 |
0.6116 |
1060.8 |
313.15 |
0.6912 |
1069.6 |
313.15 |
0.7992 |
1081.3 |
313.15 |
0.8838 |
1090.3 |
313.15 |
1.0000 |
1102.5 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethanol, 2,2'-oxybis- (2) - Liquid |
Mass density, kg/m3 - Liquid |
298.15 |
0.0000 |
1012.6 |
298.15 |
0.1080 |
1019.9 |
298.15 |
0.1977 |
1026.6 |
298.15 |
0.2897 |
1035.0 |
298.15 |
0.4096 |
1047.0 |
298.15 |
0.5090 |
1057.6 |
298.15 |
0.6116 |
1069.4 |
298.15 |
0.6912 |
1078.5 |
298.15 |
0.7992 |
1090.6 |
298.15 |
0.8838 |
1100.0 |
298.15 |
1.0000 |
1112.7 |
303.15 |
0.0000 |
1009.6 |
303.15 |
0.1080 |
1017.1 |
303.15 |
0.1977 |
1024.0 |
303.15 |
0.2897 |
1032.3 |
303.15 |
0.4096 |
1044.3 |
303.15 |
0.5090 |
1054.9 |
303.15 |
0.6116 |
1066.5 |
303.15 |
0.6912 |
1075.6 |
303.15 |
0.7992 |
1087.6 |
303.15 |
0.8838 |
1096.8 |
303.15 |
1.0000 |
1109.3 |
308.15 |
0.0000 |
1006.7 |
308.15 |
0.1080 |
1014.4 |
308.15 |
0.1977 |
1021.4 |
308.15 |
0.2897 |
1029.6 |
308.15 |
0.4096 |
1041.6 |
308.15 |
0.5090 |
1052.1 |
308.15 |
0.6116 |
1063.7 |
308.15 |
0.6912 |
1072.6 |
308.15 |
0.7992 |
1084.5 |
308.15 |
0.8838 |
1093.6 |
308.15 |
1.0000 |
1105.9 |
313.15 |
0.0000 |
1003.7 |
313.15 |
0.1080 |
1011.7 |
313.15 |
0.1977 |
1018.7 |
313.15 |
0.2897 |
1027.0 |
313.15 |
0.4096 |
1038.9 |
313.15 |
0.5090 |
1049.4 |
313.15 |
0.6116 |
1060.8 |
313.15 |
0.6912 |
1069.6 |
313.15 |
0.7992 |
1081.3 |
313.15 |
0.8838 |
1090.3 |
313.15 |
1.0000 |
1102.5 |
Speed of sound, m/s
[ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Frequency, MHz = 2 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethanol, 2,2'-oxybis- (2) - Liquid |
Speed of sound, m/s - Liquid |
298.15 |
0.0000 |
1601.6 |
298.15 |
0.1080 |
1568.1 |
298.15 |
0.1977 |
1549.9 |
298.15 |
0.2897 |
1543.5 |
298.15 |
0.4096 |
1546.2 |
298.15 |
0.5090 |
1552.2 |
298.15 |
0.6116 |
1558.9 |
298.15 |
0.6912 |
1564.5 |
298.15 |
0.7992 |
1571.3 |
298.15 |
0.8838 |
1575.3 |
298.15 |
1.0000 |
1579.3 |
303.15 |
0.0000 |
1589.3 |
303.15 |
0.1080 |
1558.9 |
303.15 |
0.1977 |
1542.0 |
303.15 |
0.2897 |
1535.7 |
303.15 |
0.4096 |
1538.6 |
303.15 |
0.5090 |
1544.0 |
303.15 |
0.6116 |
1550.2 |
303.15 |
0.6912 |
1555.3 |
303.15 |
0.7992 |
1561.2 |
303.15 |
0.8838 |
1564.6 |
303.15 |
1.0000 |
1568.0 |
308.15 |
0.0000 |
1577.7 |
308.15 |
0.1080 |
1549.8 |
308.15 |
0.1977 |
1534.4 |
308.15 |
0.2897 |
1528.2 |
308.15 |
0.4096 |
1531.1 |
308.15 |
0.5090 |
1536.3 |
308.15 |
0.6116 |
1541.8 |
308.15 |
0.6912 |
1546.4 |
308.15 |
0.7992 |
1551.7 |
308.15 |
0.8838 |
1554.7 |
308.15 |
1.0000 |
1557.3 |
313.15 |
0.0000 |
1565.6 |
313.15 |
0.1080 |
1540.6 |
313.15 |
0.1977 |
1526.6 |
313.15 |
0.2897 |
1520.3 |
313.15 |
0.4096 |
1523.2 |
313.15 |
0.5090 |
1528.1 |
313.15 |
0.6116 |
1533.1 |
313.15 |
0.6912 |
1537.2 |
313.15 |
0.7992 |
1541.7 |
313.15 |
0.8838 |
1544.4 |
313.15 |
1.0000 |
1546.1 |
Speed of sound, m/s
[ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Frequency, MHz = 2 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethanol, 2,2'-oxybis- (2) - Liquid |
Speed of sound, m/s - Liquid |
298.15 |
0.0000 |
1601.6 |
298.15 |
0.1080 |
1568.1 |
298.15 |
0.1977 |
1549.9 |
298.15 |
0.2897 |
1543.5 |
298.15 |
0.4096 |
1546.2 |
298.15 |
0.5090 |
1552.2 |
298.15 |
0.6116 |
1558.9 |
298.15 |
0.6912 |
1564.5 |
298.15 |
0.7992 |
1571.3 |
298.15 |
0.8838 |
1575.3 |
298.15 |
1.0000 |
1579.3 |
303.15 |
0.0000 |
1589.3 |
303.15 |
0.1080 |
1558.9 |
303.15 |
0.1977 |
1542.0 |
303.15 |
0.2897 |
1535.7 |
303.15 |
0.4096 |
1538.6 |
303.15 |
0.5090 |
1544.0 |
303.15 |
0.6116 |
1550.2 |
303.15 |
0.6912 |
1555.3 |
303.15 |
0.7992 |
1561.2 |
303.15 |
0.8838 |
1564.6 |
303.15 |
1.0000 |
1568.0 |
308.15 |
0.0000 |
1577.7 |
308.15 |
0.1080 |
1549.8 |
308.15 |
0.1977 |
1534.4 |
308.15 |
0.2897 |
1528.2 |
308.15 |
0.4096 |
1531.1 |
308.15 |
0.5090 |
1536.3 |
308.15 |
0.6116 |
1541.8 |
308.15 |
0.6912 |
1546.4 |
308.15 |
0.7992 |
1551.7 |
308.15 |
0.8838 |
1554.7 |
308.15 |
1.0000 |
1557.3 |
313.15 |
0.0000 |
1565.6 |
313.15 |
0.1080 |
1540.6 |
313.15 |
0.1977 |
1526.6 |
313.15 |
0.2897 |
1520.3 |
313.15 |
0.4096 |
1523.2 |
313.15 |
0.5090 |
1528.1 |
313.15 |
0.6116 |
1533.1 |
313.15 |
0.6912 |
1537.2 |
313.15 |
0.7992 |
1541.7 |
313.15 |
0.8838 |
1544.4 |
313.15 |
1.0000 |
1546.1 |
Boiling temperature at pressure P, K
[ref]
Fixed |
Measured |
Mole fraction of 1,4-Butanediol (1) - Liquid |
Pressure, kPa - Liquid |
Boiling temperature at pressure P, K - Liquid |
0.0000 |
10.00 |
445.07 |
0.0920 |
10.00 |
444.24 |
0.1780 |
10.00 |
443.55 |
0.2840 |
10.00 |
442.68 |
0.3250 |
10.00 |
442.34 |
0.3780 |
10.00 |
441.90 |
0.4460 |
10.00 |
441.40 |
0.5270 |
10.00 |
440.81 |
0.5890 |
10.00 |
440.34 |
0.6940 |
10.00 |
439.62 |
0.7960 |
10.00 |
438.92 |
0.9060 |
10.00 |
438.15 |
1.0000 |
10.00 |
437.48 |
0.0000 |
20.00 |
464.36 |
0.1180 |
20.00 |
463.09 |
0.1920 |
20.00 |
462.35 |
0.2580 |
20.00 |
461.65 |
0.3130 |
20.00 |
461.14 |
0.3730 |
20.00 |
460.52 |
0.4410 |
20.00 |
459.86 |
0.5140 |
20.00 |
459.08 |
0.5750 |
20.00 |
458.48 |
0.6890 |
20.00 |
457.44 |
0.8100 |
20.00 |
456.32 |
0.9150 |
20.00 |
455.38 |
1.0000 |
20.00 |
454.63 |
0.0000 |
40.00 |
485.33 |
0.0670 |
40.00 |
484.17 |
0.1400 |
40.00 |
483.06 |
0.2010 |
40.00 |
482.15 |
0.2830 |
40.00 |
481.08 |
0.3640 |
40.00 |
480.05 |
0.4560 |
40.00 |
478.92 |
0.5520 |
40.00 |
477.84 |
0.6490 |
40.00 |
476.77 |
0.7360 |
40.00 |
475.84 |
0.8270 |
40.00 |
474.87 |
0.9150 |
40.00 |
474.04 |
1.0000 |
40.00 |
473.22 |
Boiling temperature at pressure P, K
[ref]
Fixed |
Measured |
Mole fraction of 1,4-Butanediol (1) - Liquid |
Pressure, kPa - Liquid |
Boiling temperature at pressure P, K - Liquid |
0.0000 |
10.00 |
445.07 |
0.0920 |
10.00 |
444.24 |
0.1780 |
10.00 |
443.55 |
0.2840 |
10.00 |
442.68 |
0.3250 |
10.00 |
442.34 |
0.3780 |
10.00 |
441.90 |
0.4460 |
10.00 |
441.40 |
0.5270 |
10.00 |
440.81 |
0.5890 |
10.00 |
440.34 |
0.6940 |
10.00 |
439.62 |
0.7960 |
10.00 |
438.92 |
0.9060 |
10.00 |
438.15 |
1.0000 |
10.00 |
437.48 |
0.0000 |
20.00 |
464.36 |
0.1180 |
20.00 |
463.09 |
0.1920 |
20.00 |
462.35 |
0.2580 |
20.00 |
461.65 |
0.3130 |
20.00 |
461.14 |
0.3730 |
20.00 |
460.52 |
0.4410 |
20.00 |
459.86 |
0.5140 |
20.00 |
459.08 |
0.5750 |
20.00 |
458.48 |
0.6890 |
20.00 |
457.44 |
0.8100 |
20.00 |
456.32 |
0.9150 |
20.00 |
455.38 |
1.0000 |
20.00 |
454.63 |
0.0000 |
40.00 |
485.33 |
0.0670 |
40.00 |
484.17 |
0.1400 |
40.00 |
483.06 |
0.2010 |
40.00 |
482.15 |
0.2830 |
40.00 |
481.08 |
0.3640 |
40.00 |
480.05 |
0.4560 |
40.00 |
478.92 |
0.5520 |
40.00 |
477.84 |
0.6490 |
40.00 |
476.77 |
0.7360 |
40.00 |
475.84 |
0.8270 |
40.00 |
474.87 |
0.9150 |
40.00 |
474.04 |
1.0000 |
40.00 |
473.22 |
Sources
-
Densities, Ultrasonic Speeds, and Excess Properties of Binary Mixtures of Diethylene Glycol with 1-Butanol, 2-Butanol, and 1,4-Butanediol at Different Temperatures
-
Isobaric Vapor-Liquid Equilibrium for Four Binary Systems of Ethane-1,2-diol, Butane-1,4-diol, 2-(2- Hydroxyethoxy)ethan-1-ol and 2-[2-(2- Hydroxyethoxy)ethoxy]ethanol at 10.0 kPa, 20.0 kPa and 40.0 kPa