Mixture of Ethylbenzene + n-Propyl acetate

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Ethylbenzene

Name
Ethylbenzene
InChI
InChI=1S/C8H10/c1-2-8-6-4-3-5-7-8/h3-7H,2H2,1H3
InChI Key
YNQLUTRBYVCPMQ-UHFFFAOYSA-N
Formula
C8H10
SMILES
CCc1ccccc1
Mol. Weight (g/mol)
106.17
CAS
100-41-4

n-Propyl acetate

Name
n-Propyl acetate
InChI
InChI=1S/C5H10O2/c1-3-4-7-5(2)6/h3-4H2,1-2H3
InChI Key
YKYONYBAUNKHLG-UHFFFAOYSA-N
Formula
C5H10O2
SMILES
CCCOC(C)=O
Mol. Weight (g/mol)
102.13
CAS
109-60-4
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Datasets

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

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of n-Propyl acetate (2) - Liquid Mass density, kg/m3 - Liquid
298.15 0.0000 862.25
298.15 0.1005 864.23
298.15 0.1994 866.18
298.15 0.3002 868.16
298.15 0.4005 870.14
298.15 0.5000 872.12
298.15 0.6002 874.14
298.15 0.6997 876.17
298.15 0.7998 878.24
298.15 0.9007 880.38
298.15 1.0000 882.54
303.15 0.0000 857.88
303.15 0.1001 859.75
303.15 0.1995 861.59
303.15 0.2995 863.45
303.15 0.4000 865.32
303.15 0.5004 867.2
303.15 0.5995 869.08
303.15 0.6999 871.0
303.15 0.8005 872.96
303.15 0.9007 874.96
303.15 1.0000 876.99
308.15 0.0000 853.43
308.15 0.1000 855.19
308.15 0.2000 856.93
308.15 0.2999 858.67
308.15 0.3997 860.41
308.15 0.5003 862.18
308.15 0.5999 863.95
308.15 0.7001 865.74
308.15 0.8007 867.58
308.15 0.9003 869.44
308.15 1.0000 871.35

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of n-Propyl acetate (2) - Liquid Mass density, kg/m3 - Liquid
298.15 0.0000 862.25
298.15 0.1005 864.23
298.15 0.1994 866.18
298.15 0.3002 868.16
298.15 0.4005 870.14
298.15 0.5000 872.12
298.15 0.6002 874.14
298.15 0.6997 876.17
298.15 0.7998 878.24
298.15 0.9007 880.38
298.15 1.0000 882.54
303.15 0.0000 857.88
303.15 0.1001 859.75
303.15 0.1995 861.59
303.15 0.2995 863.45
303.15 0.4000 865.32
303.15 0.5004 867.2
303.15 0.5995 869.08
303.15 0.6999 871.0
303.15 0.8005 872.96
303.15 0.9007 874.96
303.15 1.0000 876.99
308.15 0.0000 853.43
308.15 0.1000 855.19
308.15 0.2000 856.93
308.15 0.2999 858.67
308.15 0.3997 860.41
308.15 0.5003 862.18
308.15 0.5999 863.95
308.15 0.7001 865.74
308.15 0.8007 867.58
308.15 0.9003 869.44
308.15 1.0000 871.35

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

Fixed Measured
Temperature, K - Liquid Mole fraction of n-Propyl acetate (2) - Liquid Surface tension liquid-gas, N/m - Liquid
298.15 0.0000 0.0288
298.15 0.1005 0.0282
298.15 0.1994 0.0275
298.15 0.3002 0.0269
298.15 0.4005 0.0263
298.15 0.5000 0.0259
298.15 0.6002 0.0255
298.15 0.6997 0.0251
298.15 0.7998 0.0247
298.15 0.9007 0.0243
298.15 1.0000 0.0239
298.15 0.0000 0.0288
298.15 0.1005 0.0282
298.15 0.1994 0.0275
298.15 0.3002 0.0269
298.15 0.4005 0.0263
298.15 0.5000 0.0259
298.15 0.6002 0.0255
298.15 0.6997 0.0251
298.15 0.7998 0.0247
298.15 0.9007 0.0243
298.15 1.0000 0.0239
303.15 0.0000 0.0283
303.15 0.1001 0.0277
303.15 0.1995 0.0271
303.15 0.2995 0.0265
303.15 0.4000 0.0260
303.15 0.5004 0.0255
303.15 0.5995 0.0251
303.15 0.6999 0.0246
303.15 0.8005 0.0242
303.15 0.9007 0.0238
303.15 1.0000 0.0235
303.15 0.0000 0.0283
303.15 0.1001 0.0277
303.15 0.1995 0.0271
303.15 0.2995 0.0265
303.15 0.4000 0.0260
303.15 0.5004 0.0255
303.15 0.5995 0.0251
303.15 0.6999 0.0246
303.15 0.8005 0.0242
303.15 0.9007 0.0238
303.15 1.0000 0.0235
308.15 0.0000 0.0278
308.15 0.1000 0.0272
308.15 0.2000 0.0266
308.15 0.2999 0.0260
308.15 0.3997 0.0255
308.15 0.5003 0.0250
308.15 0.5999 0.0245
308.15 0.7001 0.0241
308.15 0.8007 0.0237
308.15 0.9003 0.0232
308.15 1.0000 0.0228
308.15 0.0000 0.0278
308.15 0.1000 0.0272
308.15 0.2000 0.0266
308.15 0.2999 0.0260
308.15 0.3997 0.0255
308.15 0.5003 0.0250
308.15 0.5999 0.0245
308.15 0.7001 0.0241
308.15 0.8007 0.0237
308.15 0.9003 0.0232

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

Fixed Measured
Temperature, K - Liquid Mole fraction of n-Propyl acetate (2) - Liquid Surface tension liquid-gas, N/m - Liquid
298.15 0.0000 0.0288
298.15 0.1005 0.0282
298.15 0.1994 0.0275
298.15 0.3002 0.0269
298.15 0.4005 0.0263
298.15 0.5000 0.0259
298.15 0.6002 0.0255
298.15 0.6997 0.0251
298.15 0.7998 0.0247
298.15 0.9007 0.0243
298.15 1.0000 0.0239
298.15 0.0000 0.0288
298.15 0.1005 0.0282
298.15 0.1994 0.0275
298.15 0.3002 0.0269
298.15 0.4005 0.0263
298.15 0.5000 0.0259
298.15 0.6002 0.0255
298.15 0.6997 0.0251
298.15 0.7998 0.0247
298.15 0.9007 0.0243
298.15 1.0000 0.0239
303.15 0.0000 0.0283
303.15 0.1001 0.0277
303.15 0.1995 0.0271
303.15 0.2995 0.0265
303.15 0.4000 0.0260
303.15 0.5004 0.0255
303.15 0.5995 0.0251
303.15 0.6999 0.0246
303.15 0.8005 0.0242
303.15 0.9007 0.0238
303.15 1.0000 0.0235
303.15 0.0000 0.0283
303.15 0.1001 0.0277
303.15 0.1995 0.0271
303.15 0.2995 0.0265
303.15 0.4000 0.0260
303.15 0.5004 0.0255
303.15 0.5995 0.0251
303.15 0.6999 0.0246
303.15 0.8005 0.0242
303.15 0.9007 0.0238
303.15 1.0000 0.0235
308.15 0.0000 0.0278
308.15 0.1000 0.0272
308.15 0.2000 0.0266
308.15 0.2999 0.0260
308.15 0.3997 0.0255
308.15 0.5003 0.0250
308.15 0.5999 0.0245
308.15 0.7001 0.0241
308.15 0.8007 0.0237
308.15 0.9003 0.0232
308.15 1.0000 0.0228
308.15 0.0000 0.0278
308.15 0.1000 0.0272
308.15 0.2000 0.0266
308.15 0.2999 0.0260
308.15 0.3997 0.0255
308.15 0.5003 0.0250
308.15 0.5999 0.0245
308.15 0.7001 0.0241
308.15 0.8007 0.0237
308.15 0.9003 0.0232

Sources