Mixture of Octane + Methyl valerate

Excel

Octane

Name
Octane
InChI
InChI=1S/C8H18/c1-3-5-7-8-6-4-2/h3-8H2,1-2H3
InChI Key
TVMXDCGIABBOFY-UHFFFAOYSA-N
Formula
C8H18
SMILES
CCCCCCCC
Mol. Weight (g/mol)
114.23
CAS
111-65-9

Methyl valerate

Name
Methyl valerate
InChI
InChI=1S/C6H12O2/c1-3-4-5-6(7)8-2/h3-5H2,1-2H3
InChI Key
HNBDRPTVWVGKBR-UHFFFAOYSA-N
Formula
C6H12O2
SMILES
CCCCC(=O)OC
Mol. Weight (g/mol)
116.16
CAS
624-24-8
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Datasets

  1. Mole fraction (2)
  2. Excess molar enthalpy (molar enthalpy (2)
  3. ρl - Mass density, kg/m3 (2)
  4. Tboil - Boiling temperature at pressure P, K (2)

Mole fraction of Methyl valerate (2) [ref]

Fixed Measured
Temperature, K - Gas Mole fraction of Methyl valerate (2) - Liquid Mole fraction of Methyl valerate (2) - Gas
380.82 0.0000 0.0000
380.94 0.0000 0.0000
379.94 0.0510 0.0820
379.32 0.0950 0.1420
379.05 0.1420 0.1850
378.94 0.1310 0.1860
378.58 0.1730 0.2230
378.56 0.1800 0.2310
378.15 0.2240 0.2670
377.96 0.2690 0.3070
377.95 0.2710 0.3080
377.69 0.3300 0.3500
377.71 0.3530 0.3700
377.64 0.3740 0.3810
377.53 0.4090 0.4060
377.64 0.4130 0.4130
377.65 0.4500 0.4320
377.74 0.4740 0.4530
377.69 0.4940 0.4600
377.73 0.5240 0.4880
377.91 0.5620 0.5090
377.84 0.5720 0.5190
378.05 0.6120 0.5520
378.07 0.6210 0.5580
378.21 0.6440 0.5740
378.34 0.6580 0.5850
378.33 0.6710 0.6000
378.51 0.7010 0.6200
378.70 0.7290 0.6370
378.87 0.7390 0.6530
379.02 0.7590 0.6720
379.53 0.7890 0.7040
379.67 0.8040 0.7170
379.71 0.8180 0.7300
380.05 0.8400 0.7520
380.24 0.8570 0.7750
380.69 0.8800 0.8040
381.08 0.8990 0.8330
381.44 0.9230 0.8640
381.43 0.9280 0.8670
381.90 0.9470 0.8990
381.98 0.9560 0.9160
382.12 0.9620 0.9250
382.78 0.9840 0.9680
383.29 1.0000 1.0000

Mole fraction of Methyl valerate (2) [ref]

Fixed Measured
Temperature, K - Gas Mole fraction of Methyl valerate (2) - Liquid Mole fraction of Methyl valerate (2) - Gas
380.82 0.0000 0.0000
380.94 0.0000 0.0000
379.94 0.0510 0.0820
379.32 0.0950 0.1420
379.05 0.1420 0.1850
378.94 0.1310 0.1860
378.58 0.1730 0.2230
378.56 0.1800 0.2310
378.15 0.2240 0.2670
377.96 0.2690 0.3070
377.95 0.2710 0.3080
377.69 0.3300 0.3500
377.71 0.3530 0.3700
377.64 0.3740 0.3810
377.53 0.4090 0.4060
377.64 0.4130 0.4130
377.65 0.4500 0.4320
377.74 0.4740 0.4530
377.69 0.4940 0.4600
377.73 0.5240 0.4880
377.91 0.5620 0.5090
377.84 0.5720 0.5190
378.05 0.6120 0.5520
378.07 0.6210 0.5580
378.21 0.6440 0.5740
378.34 0.6580 0.5850
378.33 0.6710 0.6000
378.51 0.7010 0.6200
378.70 0.7290 0.6370
378.87 0.7390 0.6530
379.02 0.7590 0.6720
379.53 0.7890 0.7040
379.67 0.8040 0.7170
379.71 0.8180 0.7300
380.05 0.8400 0.7520
380.24 0.8570 0.7750
380.69 0.8800 0.8040
381.08 0.8990 0.8330
381.44 0.9230 0.8640
381.43 0.9280 0.8670
381.90 0.9470 0.8990
381.98 0.9560 0.9160
382.12 0.9620 0.9250
382.78 0.9840 0.9680
383.29 1.0000 1.0000

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

Operational conditions:

Mole fraction of Octane (1) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0427 0.1620
0.0951 0.3370
0.1523 0.5110
0.2098 0.6590
0.2677 0.7840
0.3234 0.8820
0.3770 0.9560
0.4266 1.005
0.4619 1.042
0.4695 1.043
0.5113 1.053
0.5126 1.048
0.5411 1.042
0.5701 1.039
0.6364 0.9870
0.7090 0.8880
0.7745 0.7570
0.8541 0.5480
0.9325 0.2290

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

Operational conditions:

Mole fraction of Octane (1) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0427 0.1620
0.0951 0.3370
0.1523 0.5110
0.2098 0.6590
0.2677 0.7840
0.3234 0.8820
0.3770 0.9560
0.4266 1.005
0.4619 1.042
0.4695 1.043
0.5113 1.053
0.5126 1.048
0.5411 1.042
0.5701 1.039
0.6364 0.9870
0.7090 0.8880
0.7745 0.7570
0.8541 0.5480
0.9325 0.2290

Mass density, kg/m3 [ref]

Operational conditions:

Mole fraction of Octane (1) - Liquid Mass density, kg/m3 - Liquid
0.0000 884.84
0.0514 872.35
0.1005 860.71
0.1610 846.85
0.2134 835.46
0.2601 825.47
0.3084 815.53
0.3625 804.47
0.4427 788.93
0.4558 786.45
0.5104 776.34
0.5504 769.1
0.6116 758.45
0.6541 751.22
0.7081 742.25
0.7535 734.86
0.8013 727.38
0.8518 719.71
0.9059 711.73
0.9521 705.03
1.0000 698.58

Mass density, kg/m3 [ref]

Operational conditions:

Mole fraction of Octane (1) - Liquid Mass density, kg/m3 - Liquid
0.0000 884.84
0.0514 872.35
0.1005 860.71
0.1610 846.85
0.2134 835.46
0.2601 825.47
0.3084 815.53
0.3625 804.47
0.4427 788.93
0.4558 786.45
0.5104 776.34
0.5504 769.1
0.6116 758.45
0.6541 751.22
0.7081 742.25
0.7535 734.86
0.8013 727.38
0.8518 719.71
0.9059 711.73
0.9521 705.03
1.0000 698.58

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 60 (Liquid)

Mole fraction of Methyl valerate (2) - Liquid Boiling temperature at pressure P, K - Liquid
0.0000 380.82
0.0000 380.94
0.0510 379.94
0.0950 379.32
0.1420 379.05
0.1310 378.94
0.1730 378.58
0.1800 378.56
0.2240 378.15
0.2690 377.96
0.2710 377.95
0.3300 377.69
0.3530 377.71
0.3740 377.64
0.4090 377.53
0.4130 377.64
0.4500 377.65
0.4740 377.74
0.4940 377.69
0.5240 377.73
0.5620 377.91
0.5720 377.84
0.6120 378.05
0.6210 378.07
0.6440 378.21
0.6580 378.34
0.6710 378.33
0.7010 378.51
0.7290 378.70
0.7390 378.87
0.7590 379.02
0.7890 379.53
0.8040 379.67
0.8180 379.71
0.8400 380.05
0.8570 380.24
0.8800 380.69
0.8990 381.08
0.9230 381.44
0.9280 381.43
0.9470 381.90
0.9560 381.98
0.9620 382.12
0.9840 382.78
1.0000 383.29

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 60 (Liquid)

Mole fraction of Methyl valerate (2) - Liquid Boiling temperature at pressure P, K - Liquid
0.0000 380.82
0.0000 380.94
0.0510 379.94
0.0950 379.32
0.1420 379.05
0.1310 378.94
0.1730 378.58
0.1800 378.56
0.2240 378.15
0.2690 377.96
0.2710 377.95
0.3300 377.69
0.3530 377.71
0.3740 377.64
0.4090 377.53
0.4130 377.64
0.4500 377.65
0.4740 377.74
0.4940 377.69
0.5240 377.73
0.5620 377.91
0.5720 377.84
0.6120 378.05
0.6210 378.07
0.6440 378.21
0.6580 378.34
0.6710 378.33
0.7010 378.51
0.7290 378.70
0.7390 378.87
0.7590 379.02
0.7890 379.53
0.8040 379.67
0.8180 379.71
0.8400 380.05
0.8570 380.24
0.8800 380.69
0.8990 381.08
0.9230 381.44
0.9280 381.43
0.9470 381.90
0.9560 381.98
0.9620 382.12
0.9840 382.78
1.0000 383.29

Sources