Mixture of Pyrrole + Cyclohexane

Datasets

1. Excess molar enthalpy (molar enthalpy
2. P_vap - Vapor or sublimation pressure, kPa

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

Operational conditions:

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

Mole fraction of Pyrrole (1) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0150	0.2344
0.0300	0.4145
0.0451	0.5479
0.0601	0.6500
0.0752	0.7315
0.0905	0.8041
0.1057	0.8674
0.1208	0.9243
0.1358	0.9731
0.1543	1.0282
0.1692	1.068
0.1840	1.1035
0.1989	1.1369
0.2139	1.1672
0.2288	1.1952
0.2437	1.2204
0.2587	1.2437
0.2737	1.2648
0.2887	1.2841
0.3037	1.302
0.3186	1.3179
0.3337	1.3356
0.3485	1.3478
0.3677	1.3673
0.3829	1.3797
0.3982	1.3922
0.4135	1.402
0.4287	1.4099
0.4440	1.4162
0.4592	1.4212
0.4745	1.4247
0.4898	1.4268
0.5050	1.4275
0.5203	1.4267
0.5355	1.4244
0.5507	1.4207
0.5660	1.4152
0.5812	1.4083
0.5964	1.3996
0.6116	1.3889
0.6269	1.3761
0.6421	1.3614
0.6573	1.3447
0.6725	1.3259
0.6878	1.3038
0.7030	1.2788
0.7182	1.245
0.7310	1.2101
0.7468	1.171
0.7627	1.127
0.7786	1.0844
0.7945	1.0378
0.8104	0.9871
0.8263	0.9323
0.8421	0.8731
0.8580	0.8083
0.8740	0.7390
0.8899	0.6637
0.9058	0.5830
0.9218	0.4959
0.9377	0.4027
0.9537	0.3036
0.9691	0.2013
0.9846	0.0929

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Pyrrole (1) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
1.0000	338.15	9.40
0.9481	338.15	22.70
0.9385	338.15	25.50
0.9140	338.15	29.90
0.8957	338.15	33.40
0.8717	338.15	35.50
0.8573	338.15	38.80
0.8340	338.15	41.60
0.7700	338.15	47.40
0.7613	338.15	47.80
0.7316	338.15	50.40
0.6856	338.15	52.50
0.6083	338.15	55.40
0.5497	338.15	56.60
0.4974	338.15	57.50
0.4242	338.15	58.80
0.3440	338.15	59.70
0.2762	338.15	60.30
0.1900	338.15	61.20
0.0000	338.15	61.50
1.0000	348.15	14.60
0.9462	348.15	31.40
0.9377	348.15	34.20
0.9169	348.15	40.00
0.8985	348.15	45.00
0.8794	348.15	48.70
0.8567	348.15	53.20
0.8189	348.15	58.50
0.7853	348.15	63.60
0.7708	348.15	65.00
0.7287	348.15	68.60
0.6630	348.15	71.50
0.6145	348.15	74.70
0.5424	348.15	77.20
0.4954	348.15	78.70
0.4425	348.15	80.00
0.3372	348.15	82.00
0.2696	348.15	83.10
0.1861	348.15	84.30
0.0000	348.15	84.70
1.0000	358.15	21.90
0.9482	358.15	42.20
0.9371	358.15	46.60
0.9168	358.15	53.90
0.8941	358.15	61.00
0.8699	358.15	65.90
0.8375	358.15	71.70
0.8162	358.15	78.00
0.7762	358.15	83.80
0.7574	358.15	86.40
0.7053	358.15	91.60
0.6651	358.15	95.30
0.5981	358.15	99.80

Sources

• Phase equilibria and excess molar enthalpies study of the binary systems (pyrrole + hydrocarbon, or an alcohol) and modeling

Note: These property values are available through the Cheméo API. A free account gives you an access key.