Mixture of p-Xylene + Ethane, 1,2-dimethoxy-

Excel

p-Xylene

Name
p-Xylene
InChI
InChI=1S/C8H10/c1-7-3-5-8(2)6-4-7/h3-6H,1-2H3
InChI Key
URLKBWYHVLBVBO-UHFFFAOYSA-N
Formula
C8H10
SMILES
Cc1ccc(C)cc1
Mol. Weight (g/mol)
106.17
CAS
106-42-3

Ethane, 1,2-dimethoxy-

Name
Ethane, 1,2-dimethoxy-
InChI
InChI=1S/C4H10O2/c1-5-3-4-6-2/h3-4H2,1-2H3
InChI Key
XTHFKEDIFFGKHM-UHFFFAOYSA-N
Formula
C4H10O2
SMILES
COCCOC
Mol. Weight (g/mol)
90.12
CAS
110-71-4
Cheméo is a service of Céondo GmbH, since 2007, we provide simulation, modelling and software development services for the industry. Do not hesitate to contact us for your projects.

Datasets

  1. ρl - Mass density, kg/m3 (2)
  2. γ - Surface tension liquid-gas, N/m (2)
  3. Excess molar volume, m3/mol (2)

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Ethane, 1,2-dimethoxy- (2) - Liquid Mass density, kg/m3 - Liquid
298.15 0.0000 856.95
298.15 0.1002 857.45
298.15 0.2004 857.95
298.15 0.2996 858.44
298.15 0.4001 858.93
298.15 0.5009 859.41
298.15 0.5997 859.85
298.15 0.7018 860.28
298.15 0.8005 860.66
298.15 0.8998 861.02
298.15 1.0000 861.36
303.15 0.0000 852.61
303.15 0.0999 853.1
303.15 0.2007 853.58
303.15 0.3002 854.06
303.15 0.3999 854.52
303.15 0.4999 854.97
303.15 0.6001 855.4
303.15 0.7011 855.81
303.15 0.8003 856.19
303.15 0.9003 856.52
303.15 1.0000 856.79
308.15 0.0000 848.27
308.15 0.0996 848.66
308.15 0.1998 849.05
308.15 0.2997 849.41
308.15 0.4001 849.76
308.15 0.4995 850.09
308.15 0.6004 850.4
308.15 0.6993 850.67
308.15 0.7993 850.93
308.15 0.8998 851.14
308.15 1.0000 851.24

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Ethane, 1,2-dimethoxy- (2) - Liquid Mass density, kg/m3 - Liquid
298.15 0.0000 856.95
298.15 0.1002 857.45
298.15 0.2004 857.95
298.15 0.2996 858.44
298.15 0.4001 858.93
298.15 0.5009 859.41
298.15 0.5997 859.85
298.15 0.7018 860.28
298.15 0.8005 860.66
298.15 0.8998 861.02
298.15 1.0000 861.36
303.15 0.0000 852.61
303.15 0.0999 853.1
303.15 0.2007 853.58
303.15 0.3002 854.06
303.15 0.3999 854.52
303.15 0.4999 854.97
303.15 0.6001 855.4
303.15 0.7011 855.81
303.15 0.8003 856.19
303.15 0.9003 856.52
303.15 1.0000 856.79
308.15 0.0000 848.27
308.15 0.0996 848.66
308.15 0.1998 849.05
308.15 0.2997 849.41
308.15 0.4001 849.76
308.15 0.4995 850.09
308.15 0.6004 850.4
308.15 0.6993 850.67
308.15 0.7993 850.93
308.15 0.8998 851.14
308.15 1.0000 851.24

Surface tension liquid-gas, N/m [ref]

Fixed Measured
Temperature, K - Liquid Mole fraction of Ethane, 1,2-dimethoxy- (2) - Liquid Surface tension liquid-gas, N/m - Liquid
298.15 0.0000 0.0281
298.15 0.1002 0.0276
298.15 0.2004 0.0272
298.15 0.2996 0.0267
298.15 0.4001 0.0263
298.15 0.5009 0.0259
298.15 0.5997 0.0255
298.15 0.7018 0.0252
298.15 0.8005 0.0249
298.15 0.8998 0.0246
298.15 1.0000 0.0243
303.15 0.0000 0.0276
303.15 0.0999 0.0271
303.15 0.2007 0.0267
303.15 0.3002 0.0262
303.15 0.3999 0.0258
303.15 0.4999 0.0254
303.15 0.6001 0.0250
303.15 0.7011 0.0247
303.15 0.8003 0.0244
303.15 0.9003 0.0240
303.15 1.0000 0.0237
308.15 0.0000 0.0271
308.15 0.0996 0.0266
308.15 0.1998 0.0262
308.15 0.2997 0.0257
308.15 0.4001 0.0253
308.15 0.4995 0.0249
308.15 0.6004 0.0245
308.15 0.6993 0.0242
308.15 0.7993 0.0238
308.15 0.8998 0.0235
308.15 1.0000 0.0232

Surface tension liquid-gas, N/m [ref]

Fixed Measured
Temperature, K - Liquid Mole fraction of Ethane, 1,2-dimethoxy- (2) - Liquid Surface tension liquid-gas, N/m - Liquid
298.15 0.0000 0.0281
298.15 0.1002 0.0276
298.15 0.2004 0.0272
298.15 0.2996 0.0267
298.15 0.4001 0.0263
298.15 0.5009 0.0259
298.15 0.5997 0.0255
298.15 0.7018 0.0252
298.15 0.8005 0.0249
298.15 0.8998 0.0246
298.15 1.0000 0.0243
303.15 0.0000 0.0276
303.15 0.0999 0.0271
303.15 0.2007 0.0267
303.15 0.3002 0.0262
303.15 0.3999 0.0258
303.15 0.4999 0.0254
303.15 0.6001 0.0250
303.15 0.7011 0.0247
303.15 0.8003 0.0244
303.15 0.9003 0.0240
303.15 1.0000 0.0237
308.15 0.0000 0.0271
308.15 0.0996 0.0266
308.15 0.1998 0.0262
308.15 0.2997 0.0257
308.15 0.4001 0.0253
308.15 0.4995 0.0249
308.15 0.6004 0.0245
308.15 0.6993 0.0242
308.15 0.7993 0.0238
308.15 0.8998 0.0235
308.15 1.0000 0.0232

Excess molar volume, m3/mol [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Ethane, 1,2-dimethoxy- (2) - Liquid Excess molar volume, m3/mol - Liquid
298.15 0.0000 0.0000
298.15 0.1002 -1.7200e-08
298.15 0.2004 -3.2100e-08
298.15 0.2996 -4.4000e-08
298.15 0.4001 -5.2900e-08
298.15 0.5009 -5.7900e-08
298.15 0.5997 -5.7100e-08
298.15 0.7018 -5.0600e-08
298.15 0.8005 -3.8400e-08
298.15 0.8998 -2.1500e-08
298.15 1.0000 0.0000
303.15 0.0000 0.0000
303.15 0.0999 -1.8500e-08
303.15 0.2007 -3.3900e-08
303.15 0.3002 -4.6900e-08
303.15 0.3999 -5.4800e-08
303.15 0.4999 -6.0400e-08
303.15 0.6001 -6.0000e-08
303.15 0.7011 -5.4500e-08
303.15 0.8003 -4.4400e-08
303.15 0.9003 -2.7200e-08
303.15 1.0000 0.0000
308.15 0.0000 0.0000
308.15 0.0996 -1.9700e-08
308.15 0.1998 -3.7400e-08
308.15 0.2997 -4.9300e-08
308.15 0.4001 -5.7900e-08
308.15 0.4995 -6.2600e-08
308.15 0.6004 -6.2500e-08
308.15 0.6993 -5.6600e-08
308.15 0.7993 -4.7700e-08
308.15 0.8998 -3.1100e-08
308.15 1.0000 0.0000

Excess molar volume, m3/mol [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Ethane, 1,2-dimethoxy- (2) - Liquid Excess molar volume, m3/mol - Liquid
298.15 0.0000 0.0000
298.15 0.1002 -1.7200e-08
298.15 0.2004 -3.2100e-08
298.15 0.2996 -4.4000e-08
298.15 0.4001 -5.2900e-08
298.15 0.5009 -5.7900e-08
298.15 0.5997 -5.7100e-08
298.15 0.7018 -5.0600e-08
298.15 0.8005 -3.8400e-08
298.15 0.8998 -2.1500e-08
298.15 1.0000 0.0000
303.15 0.0000 0.0000
303.15 0.0999 -1.8500e-08
303.15 0.2007 -3.3900e-08
303.15 0.3002 -4.6900e-08
303.15 0.3999 -5.4800e-08
303.15 0.4999 -6.0400e-08
303.15 0.6001 -6.0000e-08
303.15 0.7011 -5.4500e-08
303.15 0.8003 -4.4400e-08
303.15 0.9003 -2.7200e-08
303.15 1.0000 0.0000
308.15 0.0000 0.0000
308.15 0.0996 -1.9700e-08
308.15 0.1998 -3.7400e-08
308.15 0.2997 -4.9300e-08
308.15 0.4001 -5.7900e-08
308.15 0.4995 -6.2600e-08
308.15 0.6004 -6.2500e-08
308.15 0.6993 -5.6600e-08
308.15 0.7993 -4.7700e-08
308.15 0.8998 -3.1100e-08
308.15 1.0000 0.0000

Sources