Mixture of 2-Propanol, 1-methoxy- + Cyclohexane

Name: 2-Propanol, 1-methoxy-
InChI: InChI=1S/C4H10O2/c1-4(5)3-6-2/h4-5H,3H2,1-2H3
InChI Key: ARXJGSRGQADJSQ-UHFFFAOYSA-N
Formula: C4H10O2
SMILES: COCC(C)O
Mol. Weight (g/mol): 90.12
CAS: 107-98-2

Name: Cyclohexane
InChI: InChI=1S/C6H12/c1-2-4-6-5-3-1/h1-6H2
InChI Key: XDTMQSROBMDMFD-UHFFFAOYSA-N
Formula: C6H12
SMILES: C1CCCCC1
Mol. Weight (g/mol): 84.16
CAS: 110-82-7

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Datasets

Azeotropic composition: mole fraction (2)
Excess molar enthalpy (molar enthalpy (2)
T_fus - Solid-liquid equilibrium temperature, K (2)
Azeotropic temperature, K (2)

Azeotropic composition: mole fraction of 2-Propanol, 1-methoxy- (1) [ref]

Pressure, kPa - Liquid	Azeotropic composition: mole fraction of 2-Propanol, 1-methoxy- (1) - Liquid
20.04	0.0568
60.05	0.0768
99.71	0.0892

Azeotropic composition: mole fraction of 2-Propanol, 1-methoxy- (1) [ref]

Pressure, kPa - Liquid	Azeotropic composition: mole fraction of 2-Propanol, 1-methoxy- (1) - Liquid
20.04	0.0568
60.05	0.0768
99.71	0.0892

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

Operational conditions:

Temperature, K = 313.15 (Liquid)
Pressure, kPa = 101 (Liquid)

Mole fraction of 2-Propanol, 1-methoxy- (1) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0547	0.5849
0.1090	0.8917
0.1626	1.093
0.2158	1.235
0.2684	1.333
0.3205	1.395
0.3721	1.426
0.4232	1.438
0.4738	1.427
0.5239	1.402
0.5736	1.345
0.6227	1.277
0.6715	1.186
0.7197	1.079
0.7675	0.9494
0.8149	0.7998
0.8618	0.6270
0.9083	0.4390
0.9544	0.2266

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

Operational conditions:

Temperature, K = 313.15 (Liquid)
Pressure, kPa = 101 (Liquid)

Mole fraction of 2-Propanol, 1-methoxy- (1) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0547	0.5849
0.1090	0.8917
0.1626	1.093
0.2158	1.235
0.2684	1.333
0.3205	1.395
0.3721	1.426
0.4232	1.438
0.4738	1.427
0.5239	1.402
0.5736	1.345
0.6227	1.277
0.6715	1.186
0.7197	1.079
0.7675	0.9494
0.8149	0.7998
0.8618	0.6270
0.9083	0.4390
0.9544	0.2266

Solid-liquid equilibrium temperature, K [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Mole fraction of 2-Propanol, 1-methoxy- (1) - Liquid	Solid-liquid equilibrium temperature, K - Liquid
0.0000	279.96
0.0509	274.26
0.1002	271.65
0.1524	269.89
0.2011	268.74
0.2508	267.50
0.2993	266.58
0.3504	265.57
0.3998	264.50
0.4508	263.14
0.4995	262.07
0.5498	260.61
0.5992	258.36
0.6501	255.70
0.6999	251.99
0.7487	247.33
0.8000	239.93
0.8507	227.09

Solid-liquid equilibrium temperature, K [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Mole fraction of 2-Propanol, 1-methoxy- (1) - Liquid	Solid-liquid equilibrium temperature, K - Liquid
0.0000	279.96
0.0509	274.26
0.1002	271.65
0.1524	269.89
0.2011	268.74
0.2508	267.50
0.2993	266.58
0.3504	265.57
0.3998	264.50
0.4508	263.14
0.4995	262.07
0.5498	260.61
0.5992	258.36
0.6501	255.70
0.6999	251.99
0.7487	247.33
0.8000	239.93
0.8507	227.09

Azeotropic temperature, K [ref]

Pressure, kPa - Liquid	Azeotropic temperature, K - Liquid
20.04	307.40
60.05	336.76
99.71	352.66

Azeotropic temperature, K [ref]

Pressure, kPa - Liquid	Azeotropic temperature, K - Liquid
20.04	307.40
60.05	336.76
99.71	352.66

Sources