Mixture of Diisopropyl ether + Acetic acid, butyl ester

Excel

Diisopropyl ether

Name
Diisopropyl ether
InChI
InChI=1S/C6H14O/c1-5(2)7-6(3)4/h5-6H,1-4H3
InChI Key
ZAFNJMIOTHYJRJ-UHFFFAOYSA-N
Formula
C6H14O
SMILES
CC(C)OC(C)C
Mol. Weight (g/mol)
102.17
CAS
108-20-3

Acetic acid, butyl ester

Name
Acetic acid, butyl ester
InChI
InChI=1S/C6H12O2/c1-3-4-5-8-6(2)7/h3-5H2,1-2H3
InChI Key
DKPFZGUDAPQIHT-UHFFFAOYSA-N
Formula
C6H12O2
SMILES
CCCCOC(C)=O
Mol. Weight (g/mol)
116.16
CAS
123-86-4
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Datasets

  1. Mole fraction (2)
  2. Tboil - Boiling temperature at pressure P, K (2)

Mole fraction of Diisopropyl ether (1) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Diisopropyl ether (1) - Liquid Mole fraction of Diisopropyl ether (1) - Gas
0.8534 0.9717
0.7013 0.9315
0.5720 0.8830
0.4794 0.8351
0.4207 0.7984
0.3721 0.7682
0.3095 0.7159
0.2269 0.6395
0.1596 0.5456
0.1164 0.4601
0.0817 0.3757
0.0435 0.2654
0.0182 0.1338

Mole fraction of Diisopropyl ether (1) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Diisopropyl ether (1) - Liquid Mole fraction of Diisopropyl ether (1) - Gas
0.8534 0.9717
0.7013 0.9315
0.5720 0.8830
0.4794 0.8351
0.4207 0.7984
0.3721 0.7682
0.3095 0.7159
0.2269 0.6395
0.1596 0.5456
0.1164 0.4601
0.0817 0.3757
0.0435 0.2654
0.0182 0.1338

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Diisopropyl ether (1) - Liquid Boiling temperature at pressure P, K - Liquid
0.8534 345.68
0.7013 350.65
0.5720 355.57
0.4794 359.70
0.4207 362.66
0.3721 365.20
0.3095 368.95
0.2269 373.42
0.1596 378.41
0.1164 382.89
0.0817 386.27
0.0435 390.25
0.0182 394.88
0.0000 399.26
1.0000 341.77

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Diisopropyl ether (1) - Liquid Boiling temperature at pressure P, K - Liquid
0.8534 345.68
0.7013 350.65
0.5720 355.57
0.4794 359.70
0.4207 362.66
0.3721 365.20
0.3095 368.95
0.2269 373.42
0.1596 378.41
0.1164 382.89
0.0817 386.27
0.0435 390.25
0.0182 394.88
0.0000 399.26
1.0000 341.77

Sources