Mixture of 1-Butanol + Dimethyl ether

Excel

1-Butanol

Name
1-Butanol
InChI
InChI=1S/C4H10O/c1-2-3-4-5/h5H,2-4H2,1H3
InChI Key
LRHPLDYGYMQRHN-UHFFFAOYSA-N
Formula
C4H10O
SMILES
CCCCO
Mol. Weight (g/mol)
74.12
CAS
71-36-3

Dimethyl ether

Name
Dimethyl ether
InChI
InChI=1S/C2H6O/c1-3-2/h1-2H3
InChI Key
LCGLNKUTAGEVQW-UHFFFAOYSA-N
Formula
C2H6O
SMILES
COC
Mol. Weight (g/mol)
46.07
CAS
115-10-6
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Datasets

  1. Activity coefficient (2)
  2. Henry's Law constant (mole fraction scale), kPa (2)
  3. Excess molar enthalpy (molar enthalpy (2)
  4. Pvap - Vapor or sublimation pressure, kPa (2)

Activity coefficient of Dimethyl ether (2) [ref]

Operational condition: Mole fraction = 0 (Liquid)

Temperature, K - Liquid Activity coefficient of Dimethyl ether (2) - Liquid
249.96 2.05
269.94 1.84
289.99 1.7
309.99 1.58
330.01 1.44

Activity coefficient of Dimethyl ether (2) [ref]

Operational condition: Mole fraction = 0 (Liquid)

Temperature, K - Liquid Activity coefficient of Dimethyl ether (2) - Liquid
249.96 2.05
269.94 1.84
289.99 1.7
309.99 1.58
330.01 1.44

Henry's Law constant (mole fraction scale), kPa of Dimethyl ether (2) [ref]

Operational condition: Mole fraction = 0 (Liquid)

Temperature, K - Liquid Henry's Law constant (mole fraction scale), kPa of Dimethyl ether (2) - Liquid
249.96 215.0
269.94 413.0
289.99 710.0
309.99 1120.0
330.01 1590.0

Henry's Law constant (mole fraction scale), kPa of Dimethyl ether (2) [ref]

Operational condition: Mole fraction = 0 (Liquid)

Temperature, K - Liquid Henry's Law constant (mole fraction scale), kPa of Dimethyl ether (2) - Liquid
249.96 215.0
269.94 413.0
289.99 710.0
309.99 1120.0
330.01 1590.0

Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]

Operational condition: Temperature, K = 323.15 (Liquid)

Mole fraction of Dimethyl ether (2) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0655 0.1820
0.1290 0.3370
0.1904 0.4760
0.2499 0.5900
0.3076 0.6750
0.3635 0.7490
0.4178 0.8000
0.4705 0.8320
0.5216 0.8500
0.5713 0.8520
0.6196 0.8320
0.6666 0.8020
0.7122 0.7600
0.7567 0.7000
0.7999 0.6260
0.8420 0.5380
0.8831 0.4310
0.9230 0.3050
0.9620 0.1620

Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]

Operational condition: Temperature, K = 323.15 (Liquid)

Mole fraction of Dimethyl ether (2) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0655 0.1820
0.1290 0.3370
0.1904 0.4760
0.2499 0.5900
0.3076 0.6750
0.3635 0.7490
0.4178 0.8000
0.4705 0.8320
0.5216 0.8500
0.5713 0.8520
0.6196 0.8320
0.6666 0.8020
0.7122 0.7600
0.7567 0.7000
0.7999 0.6260
0.8420 0.5380
0.8831 0.4310
0.9230 0.3050
0.9620 0.1620

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 323.15 (Liquid)

Mole fraction of Dimethyl ether (2) - Liquid Vapor or sublimation pressure, kPa - Liquid
0.0000 4.61
0.0472 68.28
0.0751 105.80
0.1035 143.80
0.1323 181.70
0.1490 204.00
0.1707 231.90
0.1892 256.10
0.2588 344.00
0.3186 416.80
0.3744 482.40
0.4036 515.80
0.4501 567.90
0.4775 597.70
0.5021 624.00
0.5182 642.10
0.5251 648.30
0.5489 673.00
0.5590 682.00
0.6006 722.10
0.6433 762.30
0.6859 802.00
0.7279 841.10
0.7685 879.20
0.8074 916.40
0.8433 951.80
0.8761 985.90
0.9026 1014.90
0.9255 1041.20
0.9445 1064.50
0.9596 1084.00
0.9716 1100.20
0.9797 1111.70
0.9853 1119.90
0.9890 1125.30
0.9926 1130.90
0.9963 1136.70
0.9982 1139.80
1.0000 1143.20

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 323.15 (Liquid)

Mole fraction of Dimethyl ether (2) - Liquid Vapor or sublimation pressure, kPa - Liquid
0.0000 4.61
0.0472 68.28
0.0751 105.80
0.1035 143.80
0.1323 181.70
0.1490 204.00
0.1707 231.90
0.1892 256.10
0.2588 344.00
0.3186 416.80
0.3744 482.40
0.4036 515.80
0.4501 567.90
0.4775 597.70
0.5021 624.00
0.5182 642.10
0.5251 648.30
0.5489 673.00
0.5590 682.00
0.6006 722.10
0.6433 762.30
0.6859 802.00
0.7279 841.10
0.7685 879.20
0.8074 916.40
0.8433 951.80
0.8761 985.90
0.9026 1014.90
0.9255 1041.20
0.9445 1064.50
0.9596 1084.00
0.9716 1100.20
0.9797 1111.70
0.9853 1119.90
0.9890 1125.30
0.9926 1130.90
0.9963 1136.70
0.9982 1139.80
1.0000 1143.20

Sources