Mixture of Formic acid, propyl ester + Butane, 1,4-dichloro-

Name: Formic acid, propyl ester
InChI: InChI=1S/C4H8O2/c1-2-3-6-4-5/h4H,2-3H2,1H3
InChI Key: KFNNIILCVOLYIR-UHFFFAOYSA-N
Formula: C4H8O2
SMILES: CCCOC=O
Mol. Weight (g/mol): 88.11
CAS: 110-74-7

Name: Butane, 1,4-dichloro-
InChI: InChI=1S/C4H8Cl2/c5-3-1-2-4-6/h1-4H2
InChI Key: KJDRSWPQXHESDQ-UHFFFAOYSA-N
Formula: C4H8Cl2
SMILES: ClCCCCCl
Mol. Weight (g/mol): 127.01
CAS: 110-56-5

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Datasets

Excess molar enthalpy (molar enthalpy (4)
ρ_l - Mass density, kg/m3 (4)

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

Operational conditions:

Pressure, kPa = 101 (Liquid)
Temperature, K = 298.15 (Liquid)

Mole fraction of Formic acid, propyl ester (1) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0711	0.0285
0.1446	0.0411
0.2182	0.0439
0.2908	0.0273
0.3554	0.0089
0.4191	-0.0128
0.4755	-0.0293
0.5267	-0.0443
0.5668	-0.0557
0.6196	-0.0705
0.6810	-0.0777
0.7427	-0.0719
0.8085	-0.0598
0.8750	-0.0393
0.9390	-0.0223

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

Operational conditions:

Pressure, kPa = 101 (Liquid)
Temperature, K = 298.15 (Liquid)

Mole fraction of Formic acid, propyl ester (1) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0692	0.0390
0.1586	0.0650
0.2416	0.0800
0.3365	0.0770
0.4234	0.0620
0.5005	0.0420
0.5667	0.0170
0.6288	-0.0160
0.6884	-0.0350
0.7528	-0.0380
0.8170	-0.0380
0.8815	-0.0280
0.9414	-0.0130

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

Operational conditions:

Pressure, kPa = 101 (Liquid)
Temperature, K = 298.15 (Liquid)

Mole fraction of Formic acid, propyl ester (1) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0711	0.0285
0.1446	0.0411
0.2182	0.0439
0.2908	0.0273
0.3554	0.0089
0.4191	-0.0128
0.4755	-0.0293
0.5267	-0.0443
0.5668	-0.0557
0.6196	-0.0705
0.6810	-0.0777
0.7427	-0.0719
0.8085	-0.0598
0.8750	-0.0393
0.9390	-0.0223

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

Operational conditions:

Pressure, kPa = 101 (Liquid)
Temperature, K = 298.15 (Liquid)

Mole fraction of Formic acid, propyl ester (1) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0692	0.0390
0.1586	0.0650
0.2416	0.0800
0.3365	0.0770
0.4234	0.0620
0.5005	0.0420
0.5667	0.0170
0.6288	-0.0160
0.6884	-0.0350
0.7528	-0.0380
0.8170	-0.0380
0.8815	-0.0280
0.9414	-0.0130

Mass density, kg/m3 [ref]

Operational conditions:

Pressure, kPa = 101 (Liquid)
Temperature, K = 298.15 (Liquid)

Mole fraction of Formic acid, propyl ester (1) - Liquid	Mass density, kg/m3 - Liquid
0.0695	1119.11
0.1347	1106.03
0.1987	1092.92
0.2624	1079.78
0.3279	1066.03
0.3884	1053.07
0.4509	1039.59
0.5061	1027.51
0.5671	1013.93
0.6204	1001.93
0.6808	988.13
0.7363	975.18
0.7901	962.5
0.8426	950.01
0.8965	936.97
0.9466	924.57

Mass density, kg/m3 [ref]

Operational conditions:

Pressure, kPa = 101 (Liquid)
Temperature, K = 298.15 (Liquid)

Mole fraction of Formic acid, propyl ester (1) - Liquid	Mass density, kg/m3 - Liquid
0.0699	1119.28
0.1344	1105.73
0.2012	1091.45
0.3873	1050.4
0.4476	1036.71
0.5676	1008.76
0.6231	995.55
0.6814	981.44
0.7384	967.39
0.7933	953.67
0.8452	940.47
0.8982	926.78
0.9521	912.65
1.0000	899.81

Mass density, kg/m3 [ref]

Operational conditions:

Pressure, kPa = 101 (Liquid)
Temperature, K = 298.15 (Liquid)

Mole fraction of Formic acid, propyl ester (1) - Liquid	Mass density, kg/m3 - Liquid
0.0695	1119.11
0.1347	1106.03
0.1987	1092.92
0.2624	1079.78
0.3279	1066.03
0.3884	1053.07
0.4509	1039.59
0.5061	1027.51
0.5671	1013.93
0.6204	1001.93
0.6808	988.13
0.7363	975.18
0.7901	962.5
0.8426	950.01
0.8965	936.97
0.9466	924.57

Mass density, kg/m3 [ref]

Operational conditions:

Pressure, kPa = 101 (Liquid)
Temperature, K = 298.15 (Liquid)

Mole fraction of Formic acid, propyl ester (1) - Liquid	Mass density, kg/m3 - Liquid
0.0699	1119.28
0.1344	1105.73
0.2012	1091.45
0.3873	1050.4
0.4476	1036.71
0.5676	1008.76
0.6231	995.55
0.6814	981.44
0.7384	967.39
0.7933	953.67
0.8452	940.47
0.8982	926.78
0.9521	912.65
1.0000	899.81

Sources