Mixture of Acetonitrile + n-Butyl ether

Excel

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

n-Butyl ether

Name
n-Butyl ether
InChI
InChI=1S/C8H18O/c1-3-5-7-9-8-6-4-2/h3-8H2,1-2H3
InChI Key
DURPTKYDGMDSBL-UHFFFAOYSA-N
Formula
C8H18O
SMILES
CCCCOCCCC
Mol. Weight (g/mol)
130.23
CAS
142-96-1
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Datasets

  1. Excess molar enthalpy (molar enthalpy (2)
  2. Liquid-liquid equilibrium temperature, K (2)
  3. ρl - Mass density, kg/m3 (2)

Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Acetonitrile (1) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
298.15 0.0599 0.3246
298.15 0.1130 0.5487
298.15 0.1604 0.7169
298.15 0.2031 0.8468
298.15 0.2416 0.9459
298.15 0.3084 1.0858
298.15 0.3644 1.171
298.15 0.4120 1.2229
298.15 0.4530 1.2508
298.15 0.4886 1.2654
298.15 0.5199 1.2707
298.15 0.5476 1.268
298.15 0.5722 1.2603
298.15 0.5944 1.2497
298.15 0.6143 1.2378
298.15 0.6367 1.2199
298.15 0.6567 1.2005
298.15 0.6745 1.18
298.15 0.6906 1.1593
298.15 0.7052 1.1379
298.15 0.7185 1.1168
298.15 0.7306 1.0962
298.15 0.7417 1.0757
298.15 0.7520 1.0556
298.15 0.7615 1.0362
298.15 0.7952 0.9429
298.15 0.8161 0.8861
298.15 0.8382 0.8199
298.15 0.8615 0.7405
298.15 0.8761 0.6848
298.15 0.8911 0.6224
298.15 0.9068 0.5523
298.15 0.9229 0.4736
298.15 0.9397 0.3853
298.15 0.9512 0.3196
298.15 0.9629 0.2487
298.15 0.9750 0.1718
298.15 0.9873 0.0880
308.15 0.0591 0.3430
308.15 0.1116 0.5817
308.15 0.1586 0.7585
308.15 0.2008 0.8929
308.15 0.2390 0.9970
308.15 0.3054 1.1445
308.15 0.3612 1.2333
308.15 0.4087 1.2873
308.15 0.4496 1.3181
308.15 0.4852 1.3337
308.15 0.5164 1.3384
308.15 0.5441 1.3356
308.15 0.5688 1.3285
308.15 0.5910 1.3169
308.15 0.6110 1.3032
308.15 0.6335 1.2839
308.15 0.6535 1.2628
308.15 0.6715 1.2408
308.15 0.6877 1.2183
308.15 0.7023 1.1955
308.15 0.7157 1.1728
308.15 0.7177 1.1595
308.15 0.7279 1.1506
308.15 0.7386 1.1204
308.15 0.7391 1.1287
308.15 0.7494 1.1071
308.15 0.7589 1.086
308.15 0.7607 1.0734
308.15 0.7842 1.0167
308.15 0.8092 0.9479
308.15 0.8358 0.8638
308.15 0.8526 0.8043
308.15 0.8701 0.7370
308.15 0.8884 0.6599
308.15 0.9074 0.5712
308.15 0.9273 0.4689
308.15 0.9551 0.3080
308.15 0.9696 0.2151
308.15 0.9846 0.1122
308.15 0.9410 0.3924

Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Acetonitrile (1) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
298.15 0.0599 0.3246
298.15 0.1130 0.5487
298.15 0.1604 0.7169
298.15 0.2031 0.8468
298.15 0.2416 0.9459
298.15 0.3084 1.0858
298.15 0.3644 1.171
298.15 0.4120 1.2229
298.15 0.4530 1.2508
298.15 0.4886 1.2654
298.15 0.5199 1.2707
298.15 0.5476 1.268
298.15 0.5722 1.2603
298.15 0.5944 1.2497
298.15 0.6143 1.2378
298.15 0.6367 1.2199
298.15 0.6567 1.2005
298.15 0.6745 1.18
298.15 0.6906 1.1593
298.15 0.7052 1.1379
298.15 0.7185 1.1168
298.15 0.7306 1.0962
298.15 0.7417 1.0757
298.15 0.7520 1.0556
298.15 0.7615 1.0362
298.15 0.7952 0.9429
298.15 0.8161 0.8861
298.15 0.8382 0.8199
298.15 0.8615 0.7405
298.15 0.8761 0.6848
298.15 0.8911 0.6224
298.15 0.9068 0.5523
298.15 0.9229 0.4736
298.15 0.9397 0.3853
298.15 0.9512 0.3196
298.15 0.9629 0.2487
298.15 0.9750 0.1718
298.15 0.9873 0.0880
308.15 0.0591 0.3430
308.15 0.1116 0.5817
308.15 0.1586 0.7585
308.15 0.2008 0.8929
308.15 0.2390 0.9970
308.15 0.3054 1.1445
308.15 0.3612 1.2333
308.15 0.4087 1.2873
308.15 0.4496 1.3181
308.15 0.4852 1.3337
308.15 0.5164 1.3384
308.15 0.5441 1.3356
308.15 0.5688 1.3285
308.15 0.5910 1.3169
308.15 0.6110 1.3032
308.15 0.6335 1.2839
308.15 0.6535 1.2628
308.15 0.6715 1.2408
308.15 0.6877 1.2183
308.15 0.7023 1.1955
308.15 0.7157 1.1728
308.15 0.7177 1.1595
308.15 0.7279 1.1506
308.15 0.7386 1.1204
308.15 0.7391 1.1287
308.15 0.7494 1.1071
308.15 0.7589 1.086
308.15 0.7607 1.0734
308.15 0.7842 1.0167
308.15 0.8092 0.9479
308.15 0.8358 0.8638
308.15 0.8526 0.8043
308.15 0.8701 0.7370
308.15 0.8884 0.6599
308.15 0.9074 0.5712
308.15 0.9273 0.4689
308.15 0.9551 0.3080
308.15 0.9696 0.2151
308.15 0.9846 0.1122
308.15 0.9410 0.3924

Liquid-liquid equilibrium temperature, K [ref]

Operational condition: Pressure, kPa = 100 (Liquid mixture 1)

Mole fraction of Acetonitrile (1) - Liquid mixture 1 Liquid-liquid equilibrium temperature, K - Liquid mixture 1
0.2704 248.00
0.2925 251.30
0.3107 254.20
0.3276 256.59
0.3640 261.04
0.4028 264.12
0.4290 266.01
0.4578 267.86
0.5023 269.98
0.5215 271.32
0.5354 271.83
0.5705 272.70
0.6062 273.29
0.6416 273.37
0.6782 273.40
0.7085 273.40
0.7393 273.34
0.7759 272.75
0.8135 271.18
0.8505 267.64
0.8694 264.81
0.8878 260.89
0.8996 257.95
0.9093 253.67
0.9112 253.83
0.9179 250.36
0.9265 245.97

Liquid-liquid equilibrium temperature, K [ref]

Operational condition: Pressure, kPa = 100 (Liquid mixture 1)

Mole fraction of Acetonitrile (1) - Liquid mixture 1 Liquid-liquid equilibrium temperature, K - Liquid mixture 1
0.2704 248.00
0.2925 251.30
0.3107 254.20
0.3276 256.59
0.3640 261.04
0.4028 264.12
0.4290 266.01
0.4578 267.86
0.5023 269.98
0.5215 271.32
0.5354 271.83
0.5705 272.70
0.6062 273.29
0.6416 273.37
0.6782 273.40
0.7085 273.40
0.7393 273.34
0.7759 272.75
0.8135 271.18
0.8505 267.64
0.8694 264.81
0.8878 260.89
0.8996 257.95
0.9093 253.67
0.9112 253.83
0.9179 250.36
0.9265 245.97

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of n-Butyl ether (2) - Liquid Mass density, kg/m3 - Liquid
288.15 0.0200 786.5
288.15 0.0339 785.97
288.15 0.0514 785.31
288.15 0.0960 783.78
288.15 0.1542 782.12
288.15 0.1891 781.24
288.15 0.2048 780.89
288.15 0.2371 780.21
288.15 0.2433 780.08
288.15 0.2540 779.88
288.15 0.2763 779.47
288.15 0.3218 778.71
288.15 0.3456 778.33
288.15 0.3553 778.18
288.15 0.4008 777.55
288.15 0.4461 777.02
288.15 0.4902 776.53
288.15 0.5653 775.78
288.15 0.5808 775.64
288.15 0.6292 775.21
288.15 0.6996 774.64
288.15 0.7545 774.22
288.15 0.8041 773.84
288.15 0.8421 773.56
288.15 0.8638 773.4
288.15 0.9076 773.09
288.15 0.9500 772.82
288.15 0.9777 772.59
288.15 0.9902 772.49
293.15 0.0200 781.19
293.15 0.0339 780.66
293.15 0.0514 780.03
293.15 0.0960 778.6
293.15 0.1542 777.03
293.15 0.1891 776.24
293.15 0.2048 775.91
293.15 0.2371 775.27
293.15 0.2433 775.16
293.15 0.2540 774.97
293.15 0.2763 774.58
293.15 0.3218 773.86
293.15 0.3456 773.51
293.15 0.3553 773.39
293.15 0.4008 772.8
293.15 0.4461 772.3
293.15 0.4902 771.85
293.15 0.5653 771.18
293.15 0.5808 771.05
293.15 0.6292 770.68
293.15 0.6996 770.17
293.15 0.7545 769.79
293.15 0.8041 769.45
293.15 0.8421 769.21
293.15 0.8638 769.06
293.15 0.9076 768.76
293.15 0.9500 768.49
293.15 0.9777 768.29
293.15 0.9902 768.2
298.15 0.0200 775.84
298.15 0.0339 775.34
298.15 0.0514 774.76
298.15 0.0960 773.41
298.15 0.1542 771.94
298.15 0.1891 771.18
298.15 0.2048 770.88
298.15 0.2371 770.29
298.15 0.2433 770.18
298.15 0.2540 770.0
298.15 0.2763 769.65
298.15 0.3218 768.99
298.15 0.3456 768.67
298.15 0.3553 768.55
298.15 0.4008 768.01
298.15 0.4461 767.57
298.15 0.4902 767.15
298.15 0.5653 766.56
298.15 0.5808 766.44
298.15 0.6292 766.11
298.15 0.6996 765.64
298.15 0.7545 765.3
298.15 0.8041 765.0
298.15 0.8421 764.78
298.15 0.8638 764.65
298.15 0.9076 764.38
298.15 0.9500 764.12
298.15 0.9777 763.95
298.15 0.9902 763.86
303.15 0.0200 770.48
303.15 0.0339 770.01
303.15 0.0514 769.46
303.15 0.0960 768.2
303.15 0.1542 766.82
303.15 0.1891 766.12
303.15 0.2048 765.83
303.15 0.2371 765.28
303.15 0.2433 765.18
303.15 0.2540 765.01
303.15 0.2763 764.68
303.15 0.3218 764.07
303.15 0.3456 763.78
303.15 0.3553 763.68
303.15 0.4008 763.2
303.15 0.4461 762.79
303.15 0.4902 762.42
303.15 0.5653 761.87
303.15 0.5808 761.78
303.15 0.6292 761.48
303.15 0.6996 761.1
303.15 0.7545 760.8
303.15 0.8041 760.54
303.15 0.8421 760.34
303.15 0.8638 760.23
303.15 0.9076 759.98
303.15 0.9500 759.75
303.15 0.9777 759.6
303.15 0.9902 759.52

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of n-Butyl ether (2) - Liquid Mass density, kg/m3 - Liquid
288.15 0.0200 786.5
288.15 0.0339 785.97
288.15 0.0514 785.31
288.15 0.0960 783.78
288.15 0.1542 782.12
288.15 0.1891 781.24
288.15 0.2048 780.89
288.15 0.2371 780.21
288.15 0.2433 780.08
288.15 0.2540 779.88
288.15 0.2763 779.47
288.15 0.3218 778.71
288.15 0.3456 778.33
288.15 0.3553 778.18
288.15 0.4008 777.55
288.15 0.4461 777.02
288.15 0.4902 776.53
288.15 0.5653 775.78
288.15 0.5808 775.64
288.15 0.6292 775.21
288.15 0.6996 774.64
288.15 0.7545 774.22
288.15 0.8041 773.84
288.15 0.8421 773.56
288.15 0.8638 773.4
288.15 0.9076 773.09
288.15 0.9500 772.82
288.15 0.9777 772.59
288.15 0.9902 772.49
293.15 0.0200 781.19
293.15 0.0339 780.66
293.15 0.0514 780.03
293.15 0.0960 778.6
293.15 0.1542 777.03
293.15 0.1891 776.24
293.15 0.2048 775.91
293.15 0.2371 775.27
293.15 0.2433 775.16
293.15 0.2540 774.97
293.15 0.2763 774.58
293.15 0.3218 773.86
293.15 0.3456 773.51
293.15 0.3553 773.39
293.15 0.4008 772.8
293.15 0.4461 772.3
293.15 0.4902 771.85
293.15 0.5653 771.18
293.15 0.5808 771.05
293.15 0.6292 770.68
293.15 0.6996 770.17
293.15 0.7545 769.79
293.15 0.8041 769.45
293.15 0.8421 769.21
293.15 0.8638 769.06
293.15 0.9076 768.76
293.15 0.9500 768.49
293.15 0.9777 768.29
293.15 0.9902 768.2
298.15 0.0200 775.84
298.15 0.0339 775.34
298.15 0.0514 774.76
298.15 0.0960 773.41
298.15 0.1542 771.94
298.15 0.1891 771.18
298.15 0.2048 770.88
298.15 0.2371 770.29
298.15 0.2433 770.18
298.15 0.2540 770.0
298.15 0.2763 769.65
298.15 0.3218 768.99
298.15 0.3456 768.67
298.15 0.3553 768.55
298.15 0.4008 768.01
298.15 0.4461 767.57
298.15 0.4902 767.15
298.15 0.5653 766.56
298.15 0.5808 766.44
298.15 0.6292 766.11
298.15 0.6996 765.64
298.15 0.7545 765.3
298.15 0.8041 765.0
298.15 0.8421 764.78
298.15 0.8638 764.65
298.15 0.9076 764.38
298.15 0.9500 764.12
298.15 0.9777 763.95
298.15 0.9902 763.86
303.15 0.0200 770.48
303.15 0.0339 770.01
303.15 0.0514 769.46
303.15 0.0960 768.2
303.15 0.1542 766.82
303.15 0.1891 766.12
303.15 0.2048 765.83
303.15 0.2371 765.28
303.15 0.2433 765.18
303.15 0.2540 765.01
303.15 0.2763 764.68
303.15 0.3218 764.07
303.15 0.3456 763.78
303.15 0.3553 763.68
303.15 0.4008 763.2
303.15 0.4461 762.79
303.15 0.4902 762.42
303.15 0.5653 761.87
303.15 0.5808 761.78
303.15 0.6292 761.48
303.15 0.6996 761.1
303.15 0.7545 760.8
303.15 0.8041 760.54
303.15 0.8421 760.34
303.15 0.8638 760.23
303.15 0.9076 759.98
303.15 0.9500 759.75
303.15 0.9777 759.6
303.15 0.9902 759.52

Sources