Mixture of 1-Propene, 2-methyl- + Ethyl Acetate

Excel

1-Propene, 2-methyl-

Name
1-Propene, 2-methyl-
InChI
InChI=1S/C4H8/c1-4(2)3/h1H2,2-3H3
InChI Key
VQTUBCCKSQIDNK-UHFFFAOYSA-N
Formula
C4H8
SMILES
C=C(C)C
Mol. Weight (g/mol)
56.11
CAS
115-11-7

Ethyl Acetate

Name
Ethyl Acetate
InChI
InChI=1S/C4H8O2/c1-3-6-4(2)5/h3H2,1-2H3
InChI Key
XEKOWRVHYACXOJ-UHFFFAOYSA-N
Formula
C4H8O2
SMILES
CCOC(C)=O
Mol. Weight (g/mol)
88.11
CAS
141-78-6
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. Pvap - Vapor or sublimation pressure, kPa (2)

Vapor or sublimation pressure, kPa [ref]

Fixed Measured
Temperature, K - Liquid Mole fraction of 1-Propene, 2-methyl- (1) - Liquid Vapor or sublimation pressure, kPa - Liquid
318.40 0.0130 41.57
318.40 0.0330 56.67
318.40 0.0560 73.57
318.40 0.1020 104.87
318.40 0.1510 136.57
318.40 0.2020 167.67
318.40 0.3020 224.56
318.40 0.3530 250.66
318.40 0.4040 275.46
318.40 0.4550 299.06
318.40 0.5060 321.96
318.40 0.5970 360.35
318.40 0.6470 381.05
318.40 0.6970 401.65
318.40 0.7460 421.95
318.40 0.7960 442.95
318.40 0.9690 521.85
318.40 0.9880 532.05
318.40 1.0000 538.15
318.41 0.0000 31.37
318.41 0.2520 196.76
318.41 0.4980 318.06
318.41 0.5480 339.46
318.41 0.8460 464.65
318.41 0.8970 487.55
318.41 0.9480 511.65

Vapor or sublimation pressure, kPa [ref]

Fixed Measured
Temperature, K - Liquid Mole fraction of 1-Propene, 2-methyl- (1) - Liquid Vapor or sublimation pressure, kPa - Liquid
318.40 0.0130 41.57
318.40 0.0330 56.67
318.40 0.0560 73.57
318.40 0.1020 104.87
318.40 0.1510 136.57
318.40 0.2020 167.67
318.40 0.3020 224.56
318.40 0.3530 250.66
318.40 0.4040 275.46
318.40 0.4550 299.06
318.40 0.5060 321.96
318.40 0.5970 360.35
318.40 0.6470 381.05
318.40 0.6970 401.65
318.40 0.7460 421.95
318.40 0.7960 442.95
318.40 0.9690 521.85
318.40 0.9880 532.05
318.40 1.0000 538.15
318.41 0.0000 31.37
318.41 0.2520 196.76
318.41 0.4980 318.06
318.41 0.5480 339.46
318.41 0.8460 464.65
318.41 0.8970 487.55
318.41 0.9480 511.65

Sources