Mixture of Acetonitrile + Tetrahydrofuran

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Acetonitrile

Name
Acetonitrile
InChI
InChI=1S/C2H3N/c1-2-3/h1H3
InChI Key
WEVYAHXRMPXWCK-UHFFFAOYSA-N
Formula
C2H3N
SMILES
CC#N
Mol. Weight (g/mol)
41.05
CAS
75-05-8

Tetrahydrofuran

Name
Tetrahydrofuran
InChI
InChI=1S/C4H8O/c1-2-4-5-3-1/h1-4H2
InChI Key
WYURNTSHIVDZCO-UHFFFAOYSA-N
Formula
C4H8O
SMILES
C1CCOC1
Mol. Weight (g/mol)
72.11
CAS
109-99-9
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Datasets

  1. η - Viscosity, Pa*s (2)
  2. ρl - Mass density, kg/m3 (4)
  3. csound,fluid - Speed of Sound, m/s (2)
  4. Vapor Liquid Equilibrium at Constant Pressure
  5. Vapor Liquid Equilibrium at Constant Temperature

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Acetonitrile (1) - Liquid Viscosity, Pa*s - Liquid
298.15 0.0000 0.0005
298.15 0.1633 0.0004
298.15 0.3052 0.0004
298.15 0.4295 0.0004
298.15 0.5394 0.0004
298.15 0.6372 0.0004
298.15 0.7249 0.0004
298.15 0.8039 0.0004
298.15 0.8754 0.0004
298.15 0.9405 0.0003
298.15 1.0000 0.0003
308.15 0.0000 0.0004
308.15 0.1633 0.0004
308.15 0.3052 0.0004
308.15 0.4295 0.0004
308.15 0.5394 0.0004
308.15 0.6372 0.0003
308.15 0.7249 0.0003
308.15 0.8039 0.0003
308.15 0.8754 0.0003
308.15 0.9405 0.0003
308.15 1.0000 0.0003
318.15 0.0000 0.0004
318.15 0.1633 0.0004
318.15 0.3052 0.0003
318.15 0.4295 0.0003
318.15 0.5394 0.0003
318.15 0.6372 0.0003
318.15 0.7249 0.0003
318.15 0.8039 0.0003
318.15 0.8754 0.0003
318.15 0.9405 0.0003
318.15 1.0000 0.0003

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Acetonitrile (1) - Liquid Viscosity, Pa*s - Liquid
298.15 0.0000 0.0005
298.15 0.1633 0.0004
298.15 0.3052 0.0004
298.15 0.4295 0.0004
298.15 0.5394 0.0004
298.15 0.6372 0.0004
298.15 0.7249 0.0004
298.15 0.8039 0.0004
298.15 0.8754 0.0004
298.15 0.9405 0.0003
298.15 1.0000 0.0003
308.15 0.0000 0.0004
308.15 0.1633 0.0004
308.15 0.3052 0.0004
308.15 0.4295 0.0004
308.15 0.5394 0.0004
308.15 0.6372 0.0003
308.15 0.7249 0.0003
308.15 0.8039 0.0003
308.15 0.8754 0.0003
308.15 0.9405 0.0003
308.15 1.0000 0.0003
318.15 0.0000 0.0004
318.15 0.1633 0.0004
318.15 0.3052 0.0003
318.15 0.4295 0.0003
318.15 0.5394 0.0003
318.15 0.6372 0.0003
318.15 0.7249 0.0003
318.15 0.8039 0.0003
318.15 0.8754 0.0003
318.15 0.9405 0.0003
318.15 1.0000 0.0003

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Tetrahydrofuran (2) - Liquid Mass density, kg/m3 - Liquid
288.15 0.0053 788.34
288.15 0.0104 789.18
288.15 0.0197 790.72
288.15 0.0294 792.28
288.15 0.0389 793.83
288.15 0.0993 803.2
288.15 0.1598 812.11
288.15 0.1978 817.43
288.15 0.2441 823.65
288.15 0.2845 828.9
288.15 0.3445 836.2
288.15 0.4022 842.91
288.15 0.4545 848.62
288.15 0.4995 853.35
288.15 0.5298 856.4
288.15 0.5552 858.94
288.15 0.6054 863.65
288.15 0.6405 866.78
288.15 0.6603 868.52
288.15 0.6976 871.74
288.15 0.7470 875.76
288.15 0.8003 879.84
288.15 0.8179 881.06
288.15 0.8537 883.67
288.15 0.8975 886.63
288.15 0.9502 890.0
288.15 0.9671 890.93
288.15 0.9745 891.4
288.15 0.9854 892.01
288.15 0.9877 892.14
288.15 0.9940 892.51
293.15 0.0053 783.0
293.15 0.0104 783.84
293.15 0.0197 785.35
293.15 0.0294 786.96
293.15 0.0389 788.5
293.15 0.0993 797.8
293.15 0.1598 806.78
293.15 0.1978 812.02
293.15 0.2441 818.27
293.15 0.2845 823.5
293.15 0.3445 830.81
293.15 0.4022 837.51
293.15 0.4545 843.24
293.15 0.4995 847.94
293.15 0.5298 851.03
293.15 0.5552 853.51
293.15 0.6054 858.25
293.15 0.6405 861.42
293.15 0.6603 863.15
293.15 0.6976 866.29
293.15 0.7470 870.32
293.15 0.8003 874.36
293.15 0.8179 875.68
293.15 0.8537 878.23
293.15 0.8975 881.19
293.15 0.9502 884.59
293.15 0.9671 885.55
293.15 0.9745 886.03
293.15 0.9854 886.65
293.15 0.9877 886.76
293.15 0.9940 887.12
298.15 0.0053 777.57
298.15 0.0104 778.44
298.15 0.0197 779.94
298.15 0.0294 781.56
298.15 0.0389 783.1
298.15 0.0993 792.41
298.15 0.1598 801.3
298.15 0.1978 806.63
298.15 0.2441 812.84
298.15 0.2845 818.1
298.15 0.3445 825.36
298.15 0.4022 832.02
298.15 0.4545 837.79
298.15 0.4995 842.49
298.15 0.5298 845.55
298.15 0.5552 848.07
298.15 0.6054 852.78
298.15 0.6405 855.96
298.15 0.6603 857.69
298.15 0.6976 860.83
298.15 0.7470 864.86
298.15 0.8003 868.9
298.15 0.8179 870.22
298.15 0.8537 872.77
298.15 0.8975 875.76
298.15 0.9502 879.13
298.15 0.9671 880.09
298.15 0.9745 880.56
298.15 0.9854 881.17
298.15 0.9877 881.29
298.15 0.9940 881.66
303.15 0.0053 772.17
303.15 0.0104 773.01
303.15 0.0197 774.52
303.15 0.0294 776.11
303.15 0.0389 777.67
303.15 0.0993 786.97
303.15 0.1598 795.84
303.15 0.1978 801.18
303.15 0.2441 807.39
303.15 0.2845 812.64
303.15 0.3445 819.91
303.15 0.4022 826.57
303.15 0.4545 832.34
303.15 0.4995 837.08
303.15 0.5298 840.1
303.15 0.5552 842.6
303.15 0.6054 847.29
303.15 0.6405 850.47
303.15 0.6603 852.2
303.15 0.6976 855.34
303.15 0.7470 859.36
303.15 0.8003 863.41
303.15 0.8179 864.73
303.15 0.8537 867.28
303.15 0.8975 870.25
303.15 0.9502 873.61
303.15 0.9671 874.59
303.15 0.9745 875.07
303.15 0.9854 875.7
303.15 0.9877 875.8
303.15 0.9940 876.13

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Acetonitrile (1) - Liquid Mass density, kg/m3 - Liquid
298.15 0.0000 880.8
298.15 0.1633 870.3
298.15 0.3052 859.5
298.15 0.4295 848.6
298.15 0.5394 837.6
298.15 0.6372 826.8
298.15 0.7249 816.2
298.15 0.8039 805.8
298.15 0.8754 795.9
298.15 0.9405 786.2
298.15 1.0000 776.8
308.15 0.0000 871.5
308.15 0.1633 860.4
308.15 0.3052 849.2
308.15 0.4295 838.0
308.15 0.5394 827.0
308.15 0.6372 816.2
308.15 0.7249 805.7
308.15 0.8039 795.3
308.15 0.8754 785.2
308.15 0.9405 775.2
308.15 1.0000 765.4
318.15 0.0000 860.8
318.15 0.1633 851.0
318.15 0.3052 840.5
318.15 0.4295 829.6
318.15 0.5394 818.4
318.15 0.6372 807.3
318.15 0.7249 796.3
318.15 0.8039 785.5
318.15 0.8754 775.0
318.15 0.9405 764.7
318.15 1.0000 754.7

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Tetrahydrofuran (2) - Liquid Mass density, kg/m3 - Liquid
288.15 0.0053 788.34
288.15 0.0104 789.18
288.15 0.0197 790.72
288.15 0.0294 792.28
288.15 0.0389 793.83
288.15 0.0993 803.2
288.15 0.1598 812.11
288.15 0.1978 817.43
288.15 0.2441 823.65
288.15 0.2845 828.9
288.15 0.3445 836.2
288.15 0.4022 842.91
288.15 0.4545 848.62
288.15 0.4995 853.35
288.15 0.5298 856.4
288.15 0.5552 858.94
288.15 0.6054 863.65
288.15 0.6405 866.78
288.15 0.6603 868.52
288.15 0.6976 871.74
288.15 0.7470 875.76
288.15 0.8003 879.84
288.15 0.8179 881.06
288.15 0.8537 883.67
288.15 0.8975 886.63
288.15 0.9502 890.0
288.15 0.9671 890.93
288.15 0.9745 891.4
288.15 0.9854 892.01
288.15 0.9877 892.14
288.15 0.9940 892.51
293.15 0.0053 783.0
293.15 0.0104 783.84
293.15 0.0197 785.35
293.15 0.0294 786.96
293.15 0.0389 788.5
293.15 0.0993 797.8
293.15 0.1598 806.78
293.15 0.1978 812.02
293.15 0.2441 818.27
293.15 0.2845 823.5
293.15 0.3445 830.81
293.15 0.4022 837.51
293.15 0.4545 843.24
293.15 0.4995 847.94
293.15 0.5298 851.03
293.15 0.5552 853.51
293.15 0.6054 858.25
293.15 0.6405 861.42
293.15 0.6603 863.15
293.15 0.6976 866.29
293.15 0.7470 870.32
293.15 0.8003 874.36
293.15 0.8179 875.68
293.15 0.8537 878.23
293.15 0.8975 881.19
293.15 0.9502 884.59
293.15 0.9671 885.55
293.15 0.9745 886.03
293.15 0.9854 886.65
293.15 0.9877 886.76
293.15 0.9940 887.12
298.15 0.0053 777.57
298.15 0.0104 778.44
298.15 0.0197 779.94
298.15 0.0294 781.56
298.15 0.0389 783.1
298.15 0.0993 792.41
298.15 0.1598 801.3
298.15 0.1978 806.63
298.15 0.2441 812.84
298.15 0.2845 818.1
298.15 0.3445 825.36
298.15 0.4022 832.02
298.15 0.4545 837.79
298.15 0.4995 842.49
298.15 0.5298 845.55
298.15 0.5552 848.07
298.15 0.6054 852.78
298.15 0.6405 855.96
298.15 0.6603 857.69
298.15 0.6976 860.83
298.15 0.7470 864.86
298.15 0.8003 868.9
298.15 0.8179 870.22
298.15 0.8537 872.77
298.15 0.8975 875.76
298.15 0.9502 879.13
298.15 0.9671 880.09
298.15 0.9745 880.56
298.15 0.9854 881.17
298.15 0.9877 881.29
298.15 0.9940 881.66
303.15 0.0053 772.17
303.15 0.0104 773.01
303.15 0.0197 774.52
303.15 0.0294 776.11
303.15 0.0389 777.67
303.15 0.0993 786.97
303.15 0.1598 795.84
303.15 0.1978 801.18
303.15 0.2441 807.39
303.15 0.2845 812.64
303.15 0.3445 819.91
303.15 0.4022 826.57
303.15 0.4545 832.34
303.15 0.4995 837.08
303.15 0.5298 840.1
303.15 0.5552 842.6
303.15 0.6054 847.29
303.15 0.6405 850.47
303.15 0.6603 852.2
303.15 0.6976 855.34
303.15 0.7470 859.36
303.15 0.8003 863.41
303.15 0.8179 864.73
303.15 0.8537 867.28
303.15 0.8975 870.25
303.15 0.9502 873.61
303.15 0.9671 874.59
303.15 0.9745 875.07
303.15 0.9854 875.7
303.15 0.9877 875.8
303.15 0.9940 876.13

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Acetonitrile (1) - Liquid Mass density, kg/m3 - Liquid
298.15 0.0000 880.8
298.15 0.1633 870.3
298.15 0.3052 859.5
298.15 0.4295 848.6
298.15 0.5394 837.6
298.15 0.6372 826.8
298.15 0.7249 816.2
298.15 0.8039 805.8
298.15 0.8754 795.9
298.15 0.9405 786.2
298.15 1.0000 776.8
308.15 0.0000 871.5
308.15 0.1633 860.4
308.15 0.3052 849.2
308.15 0.4295 838.0
308.15 0.5394 827.0
308.15 0.6372 816.2
308.15 0.7249 805.7
308.15 0.8039 795.3
308.15 0.8754 785.2
308.15 0.9405 775.2
308.15 1.0000 765.4
318.15 0.0000 860.8
318.15 0.1633 851.0
318.15 0.3052 840.5
318.15 0.4295 829.6
318.15 0.5394 818.4
318.15 0.6372 807.3
318.15 0.7249 796.3
318.15 0.8039 785.5
318.15 0.8754 775.0
318.15 0.9405 764.7
318.15 1.0000 754.7

Speed of sound, m/s [ref]

Operational conditions:

Mole fraction of Acetonitrile (1) - Liquid Speed of sound, m/s - Liquid
0.0000 1292.2
0.1633 1344.3
0.3052 1395.2
0.4295 1443.9
0.5394 1490.4
0.6372 1533.8
0.7249 1573.6
0.8039 1610.3
0.8754 1645.5
0.9405 1679.0
1.0000 1713.2

Speed of sound, m/s [ref]

Operational conditions:

Mole fraction of Acetonitrile (1) - Liquid Speed of sound, m/s - Liquid
0.0000 1292.2
0.1633 1344.3
0.3052 1395.2
0.4295 1443.9
0.5394 1490.4
0.6372 1533.8
0.7249 1573.6
0.8039 1610.3
0.8754 1645.5
0.9405 1679.0
1.0000 1713.2

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 93.8 (VLE)

Fixed Measured
T [K] - VLE x1[mol/mol] of Tetrahydrofuran (2) - Liquid y1[mol/mol] of Tetrahydrofuran (2) - Vapour
352.3 0.0000 0.0000
347.4 0.0850 0.1890
346.9 0.0860 0.1920
345.9 0.1140 0.2560
345.2 0.1410 0.2930
344.4 0.1740 0.3320
343.7 0.2100 0.3740
343.9 0.2390 0.3910
342.0 0.3500 0.4950
340.7 0.4030 0.5360
339.5 0.4880 0.6040
339.0 0.5390 0.6410
338.1 0.6270 0.7050
337.9 0.6520 0.7140
337.7 0.6860 0.7340
337.2 0.8100 0.8340
337.1 0.8440 0.8580
337.0 0.8950 0.9030
336.9 1.0000 1.0000

Vapor Liquid Equilibrium at Constant Temperature [ref]

Operational condition: Temperature, K = 302.15 (VLE)

Fixed Measured
P [kPa] - VLE x1[mol/mol] of Tetrahydrofuran (2) - Liquid y1[mol/mol] of Tetrahydrofuran (2) - Vapour
14.004 0.0031 0.0126
14.179 0.0072 0.0288
14.437 0.0131 0.0505
14.772 0.0217 0.0804
15.328 0.0344 0.1198
15.997 0.0513 0.1661
17.061 0.0857 0.2426
18.474 0.1404 0.3333
19.894 0.2108 0.4176
20.974 0.2785 0.4798
21.913 0.3528 0.5365
22.401 0.3926 0.5639
22.538 0.4136 0.5779
22.978 0.4470 0.5993
23.658 0.5228 0.6466
24.355 0.6128 0.7024
24.726 0.6664 0.7365
25.035 0.7174 0.7701
25.299 0.7859 0.8179
25.537 0.8624 0.8762
25.671 0.9386 0.9412
25.678 0.9729 0.9732
25.678 0.9905 0.9905

Sources