Mixture of «alpha»-Acetobutyrolactone + Ethanone, 1-cyclopropyl-

Excel

«alpha»-Acetobutyrolactone

Name
«alpha»-Acetobutyrolactone
InChI
InChI=1S/C6H8O3/c1-4(7)5-2-3-9-6(5)8/h5H,2-3H2,1H3
InChI Key
OMQHDIHZSDEIFH-UHFFFAOYSA-N
Formula
C6H8O3
SMILES
CC(=O)C1CCOC1=O
Mol. Weight (g/mol)
128.13
CAS
517-23-7

Ethanone, 1-cyclopropyl-

Name
Ethanone, 1-cyclopropyl-
InChI
InChI=1S/C5H8O/c1-4(6)5-2-3-5/h5H,2-3H2,1H3
InChI Key
HVCFCNAITDHQFX-UHFFFAOYSA-N
Formula
C5H8O
SMILES
CC(=O)C1CC1
Mol. Weight (g/mol)
84.12
CAS
765-43-5
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. Mole fraction (2)
  2. η - Viscosity, Pa*s (2)
  3. ρl - Mass density, kg/m3 (2)
  4. Tboil - Boiling temperature at pressure P, K (2)

Mole fraction of Ethanone, 1-cyclopropyl- (2) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Ethanone, 1-cyclopropyl- (2) - Liquid Mole fraction of Ethanone, 1-cyclopropyl- (2) - Gas
1.0000 1.0000
0.9278 0.9947
0.8100 0.9881
0.5145 0.9757
0.5042 0.9695
0.4197 0.9645
0.3267 0.9597
0.2410 0.9266
0.1968 0.8894
0.1178 0.7781
0.1137 0.7502
0.1054 0.7257
0.0998 0.7171
0.0698 0.6500
0.0365 0.4500
0.0000 0.0000

Mole fraction of Ethanone, 1-cyclopropyl- (2) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Ethanone, 1-cyclopropyl- (2) - Liquid Mole fraction of Ethanone, 1-cyclopropyl- (2) - Gas
1.0000 1.0000
0.9278 0.9947
0.8100 0.9881
0.5145 0.9757
0.5042 0.9695
0.4197 0.9645
0.3267 0.9597
0.2410 0.9266
0.1968 0.8894
0.1178 0.7781
0.1137 0.7502
0.1054 0.7257
0.0998 0.7171
0.0698 0.6500
0.0365 0.4500
0.0000 0.0000

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed Measured
Mole fraction of Ethanone, 1-cyclopropyl- (2) - Liquid Temperature, K - Liquid Viscosity, Pa*s - Liquid
1.0000 303.15 0.0006
0.8999 303.15 0.0007
0.7999 303.15 0.0008
0.6999 303.15 0.0010
0.5999 303.15 0.0012
0.4999 303.15 0.0015
0.4002 303.15 0.0018
0.3004 303.15 0.0022
0.2009 303.15 0.0026
0.0998 303.15 0.0032
0.0000 303.15 0.0038
1.0000 313.15 0.0005
0.8999 313.15 0.0006
0.7999 313.15 0.0007
0.6999 313.15 0.0009
0.5999 313.15 0.0011
0.4999 313.15 0.0013
0.4002 313.15 0.0016
0.3004 313.15 0.0019
0.2009 313.15 0.0024
0.0998 313.15 0.0029
0.0000 313.15 0.0034
1.0000 323.15 0.0005
0.8999 323.15 0.0005
0.7999 323.15 0.0006
0.6999 323.15 0.0008
0.5999 323.15 0.0009
0.4999 323.15 0.0012
0.4002 323.15 0.0014
0.3004 323.15 0.0017
0.2009 323.15 0.0021
0.0998 323.15 0.0026
0.0000 323.15 0.0031
1.0000 333.15 0.0004
0.8999 333.15 0.0005
0.7999 333.15 0.0006
0.6999 333.15 0.0007
0.5999 333.15 0.0008
0.4999 333.15 0.0010
0.4002 333.15 0.0013
0.3004 333.15 0.0016
0.2009 333.15 0.0019
0.0998 333.15 0.0023
0.0000 333.15 0.0027

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed Measured
Mole fraction of Ethanone, 1-cyclopropyl- (2) - Liquid Temperature, K - Liquid Viscosity, Pa*s - Liquid
1.0000 303.15 0.0006
0.8999 303.15 0.0007
0.7999 303.15 0.0008
0.6999 303.15 0.0010
0.5999 303.15 0.0012
0.4999 303.15 0.0015
0.4002 303.15 0.0018
0.3004 303.15 0.0022
0.2009 303.15 0.0026
0.0998 303.15 0.0032
0.0000 303.15 0.0038
1.0000 313.15 0.0005
0.8999 313.15 0.0006
0.7999 313.15 0.0007
0.6999 313.15 0.0009
0.5999 313.15 0.0011
0.4999 313.15 0.0013
0.4002 313.15 0.0016
0.3004 313.15 0.0019
0.2009 313.15 0.0024
0.0998 313.15 0.0029
0.0000 313.15 0.0034
1.0000 323.15 0.0005
0.8999 323.15 0.0005
0.7999 323.15 0.0006
0.6999 323.15 0.0008
0.5999 323.15 0.0009
0.4999 323.15 0.0012
0.4002 323.15 0.0014
0.3004 323.15 0.0017
0.2009 323.15 0.0021
0.0998 323.15 0.0026
0.0000 323.15 0.0031
1.0000 333.15 0.0004
0.8999 333.15 0.0005
0.7999 333.15 0.0006
0.6999 333.15 0.0007
0.5999 333.15 0.0008
0.4999 333.15 0.0010
0.4002 333.15 0.0013
0.3004 333.15 0.0016
0.2009 333.15 0.0019
0.0998 333.15 0.0023
0.0000 333.15 0.0027

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed Measured
Mole fraction of Ethanone, 1-cyclopropyl- (2) - Liquid Temperature, K - Liquid Mass density, kg/m3 - Liquid
1.0000 303.15 889.8
0.8999 303.15 924.5
0.7999 303.15 958.3
0.6999 303.15 991.1
0.5999 303.15 1022.5
0.4999 303.15 1052.8
0.4002 303.15 1081.9
0.3004 303.15 1109.7
0.2009 303.15 1136.2
0.0998 303.15 1161.9
0.0000 303.15 1185.7
1.0000 313.15 880.3
0.8999 313.15 915.5
0.7999 313.15 949.2
0.6999 313.15 982.1
0.5999 313.15 1013.8
0.4999 313.15 1044.3
0.4002 313.15 1073.7
0.3004 313.15 1101.8
0.2009 313.15 1128.5
0.0998 313.15 1154.3
0.0000 313.15 1178.3
1.0000 323.15 870.6
0.8999 323.15 905.9
0.7999 323.15 939.6
0.6999 323.15 972.4
0.5999 323.15 1004.2
0.4999 323.15 1034.8
0.4002 323.15 1064.2
0.3004 323.15 1092.3
0.2009 323.15 1119.1
0.0998 323.15 1144.9
0.0000 323.15 1168.9
1.0000 333.15 861.2
0.8999 333.15 896.5
0.7999 333.15 930.2
0.6999 333.15 963.1
0.5999 333.15 994.8
0.4999 333.15 1025.4
0.4002 333.15 1054.8
0.3004 333.15 1082.9
0.2009 333.15 1109.7
0.0998 333.15 1135.6
0.0000 333.15 1159.4

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed Measured
Mole fraction of Ethanone, 1-cyclopropyl- (2) - Liquid Temperature, K - Liquid Mass density, kg/m3 - Liquid
1.0000 303.15 889.8
0.8999 303.15 924.5
0.7999 303.15 958.3
0.6999 303.15 991.1
0.5999 303.15 1022.5
0.4999 303.15 1052.8
0.4002 303.15 1081.9
0.3004 303.15 1109.7
0.2009 303.15 1136.2
0.0998 303.15 1161.9
0.0000 303.15 1185.7
1.0000 313.15 880.3
0.8999 313.15 915.5
0.7999 313.15 949.2
0.6999 313.15 982.1
0.5999 313.15 1013.8
0.4999 313.15 1044.3
0.4002 313.15 1073.7
0.3004 313.15 1101.8
0.2009 313.15 1128.5
0.0998 313.15 1154.3
0.0000 313.15 1178.3
1.0000 323.15 870.6
0.8999 323.15 905.9
0.7999 323.15 939.6
0.6999 323.15 972.4
0.5999 323.15 1004.2
0.4999 323.15 1034.8
0.4002 323.15 1064.2
0.3004 323.15 1092.3
0.2009 323.15 1119.1
0.0998 323.15 1144.9
0.0000 323.15 1168.9
1.0000 333.15 861.2
0.8999 333.15 896.5
0.7999 333.15 930.2
0.6999 333.15 963.1
0.5999 333.15 994.8
0.4999 333.15 1025.4
0.4002 333.15 1054.8
0.3004 333.15 1082.9
0.2009 333.15 1109.7
0.0998 333.15 1135.6
0.0000 333.15 1159.4

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Ethanone, 1-cyclopropyl- (2) - Liquid Boiling temperature at pressure P, K - Liquid
1.0000 384.80
0.9278 387.40
0.8100 392.40
0.5145 411.30
0.5042 412.20
0.4197 420.40
0.3267 431.90
0.2410 445.80
0.1968 454.70
0.1178 475.50
0.1137 476.80
0.1054 479.60
0.0998 481.50
0.0698 490.20
0.0365 508.20
0.0000 530.90

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Ethanone, 1-cyclopropyl- (2) - Liquid Boiling temperature at pressure P, K - Liquid
1.0000 384.80
0.9278 387.40
0.8100 392.40
0.5145 411.30
0.5042 412.20
0.4197 420.40
0.3267 431.90
0.2410 445.80
0.1968 454.70
0.1178 475.50
0.1137 476.80
0.1054 479.60
0.0998 481.50
0.0698 490.20
0.0365 508.20
0.0000 530.90

Sources