Mixture of Diisopropyl ether + Ethanol, 2-ethoxy-

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

Ethanol, 2-ethoxy-

Name
Ethanol, 2-ethoxy-
InChI
InChI=1S/C4H10O2/c1-2-6-4-3-5/h5H,2-4H2,1H3
InChI Key
ZNQVEEAIQZEUHB-UHFFFAOYSA-N
Formula
C4H10O2
SMILES
CCOCCO
Mol. Weight (g/mol)
90.12
CAS
110-80-5
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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
0.8648 0.9771
0.6907 0.9469
0.5435 0.9107
0.4333 0.8741
0.2788 0.7988
0.1945 0.7305
0.1324 0.6479
0.0917 0.5440
0.0675 0.4636
0.0536 0.4099
0.0417 0.3502
0.0348 0.3161
0.0237 0.2338
0.0092 0.1070

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
0.8648 0.9771
0.6907 0.9469
0.5435 0.9107
0.4333 0.8741
0.2788 0.7988
0.1945 0.7305
0.1324 0.6479
0.0917 0.5440
0.0675 0.4636
0.0536 0.4099
0.0417 0.3502
0.0348 0.3161
0.0237 0.2338
0.0092 0.1070

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
0.8648 345.23
0.6907 349.59
0.5435 354.50
0.4333 359.25
0.2788 368.00
0.1945 374.22
0.1324 380.80
0.0917 386.92
0.0675 390.96
0.0536 393.40
0.0417 395.98
0.0348 397.35
0.0237 400.57
0.0092 405.02
0.0000 408.19
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
0.8648 345.23
0.6907 349.59
0.5435 354.50
0.4333 359.25
0.2788 368.00
0.1945 374.22
0.1324 380.80
0.0917 386.92
0.0675 390.96
0.0536 393.40
0.0417 395.98
0.0348 397.35
0.0237 400.57
0.0092 405.02
0.0000 408.19
1.0000 341.77

Sources