Mixture of Propene + Dimethyl ether

Excel

Propene

Name
Propene
InChI
InChI=1S/C3H6/c1-3-2/h3H,1H2,2H3
InChI Key
QQONPFPTGQHPMA-UHFFFAOYSA-N
Formula
C3H6
SMILES
C=CC
Mol. Weight (g/mol)
42.08
CAS
115-07-1

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. Mole fraction (2)
  2. Excess molar enthalpy (molar enthalpy (2)
  3. Pvap - Vapor or sublimation pressure, kPa (6)

Mole fraction of Propene (1) [ref]

Operational condition: Temperature, K = 313.32 (Liquid)

Mole fraction of Propene (1) - Liquid Mole fraction of Propene (1) - Gas
0.0000 0.0000
0.0307 0.0568
0.0830 0.1432
0.1125 0.1884
0.1353 0.2202
0.1845 0.2858
0.2687 0.3875
0.3753 0.4977
0.4971 0.6113
0.5986 0.6961
0.6823 0.7645
0.6890 0.7680
0.7365 0.8055
0.7618 0.8247
0.7769 0.8360
0.7987 0.8521
0.8213 0.8690
0.8593 0.8967
0.8925 0.9210
0.9175 0.9395
0.9224 0.9432
0.9294 0.9482
0.9321 0.9502
0.9398 0.9558
0.9479 0.9618
0.9568 0.9683
0.9600 0.9708
0.9648 0.9743
0.9707 0.9786
0.9781 0.9840
0.9907 0.9932
0.9949 0.9963
1.0000 1.0000

Mole fraction of Propene (1) [ref]

Operational condition: Temperature, K = 313.32 (Liquid)

Mole fraction of Propene (1) - Liquid Mole fraction of Propene (1) - Gas
0.0000 0.0000
0.0307 0.0568
0.0830 0.1432
0.1125 0.1884
0.1353 0.2202
0.1845 0.2858
0.2687 0.3875
0.3753 0.4977
0.4971 0.6113
0.5986 0.6961
0.6823 0.7645
0.6890 0.7680
0.7365 0.8055
0.7618 0.8247
0.7769 0.8360
0.7987 0.8521
0.8213 0.8690
0.8593 0.8967
0.8925 0.9210
0.9175 0.9395
0.9224 0.9432
0.9294 0.9482
0.9321 0.9502
0.9398 0.9558
0.9479 0.9618
0.9568 0.9683
0.9600 0.9708
0.9648 0.9743
0.9707 0.9786
0.9781 0.9840
0.9907 0.9932
0.9949 0.9963
1.0000 1.0000

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

Operational conditions:

Mole fraction of Propene (1) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0427 0.0240
0.0861 0.0470
0.1301 0.0650
0.1748 0.0840
0.2203 0.1010
0.2664 0.1170
0.3133 0.1280
0.3610 0.1390
0.4095 0.1480
0.4587 0.1540
0.5088 0.1560
0.5597 0.1550
0.6115 0.1520
0.6641 0.1450
0.7177 0.1330
0.7722 0.1160
0.8277 0.0930
0.8841 0.0670
0.9415 0.0330

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

Operational conditions:

Mole fraction of Propene (1) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0427 0.0240
0.0861 0.0470
0.1301 0.0650
0.1748 0.0840
0.2203 0.1010
0.2664 0.1170
0.3133 0.1280
0.3610 0.1390
0.4095 0.1480
0.4587 0.1540
0.5088 0.1560
0.5597 0.1550
0.6115 0.1520
0.6641 0.1450
0.7177 0.1330
0.7722 0.1160
0.8277 0.0930
0.8841 0.0670
0.9415 0.0330

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 313.1 (Liquid)

Mole fraction of Propene (1) - Liquid Vapor or sublimation pressure, kPa - Liquid
0.0000 891.60
0.0068 899.18
0.0542 945.55
0.1057 994.33
0.1680 1050.90
0.2325 1107.20
0.2940 1158.60
0.3546 1207.50
0.4032 1246.60
0.4169 1256.10
0.4696 1296.00
0.4856 1307.00
0.5286 1339.60
0.5793 1373.80
0.6740 1439.10
0.7633 1498.90
0.8379 1547.60
0.8967 1585.20
0.9419 1613.50
0.9704 1630.80
0.9833 1638.30
0.9952 1644.80
1.0000 1647.30

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 313.32 (Liquid)

Mole fraction of Propene (1) - Liquid Vapor or sublimation pressure, kPa - Liquid
0.0000 896.20
0.0307 927.90
0.0830 977.10
0.1125 1004.60
0.1353 1024.50
0.1845 1065.60
0.2687 1139.10
0.3753 1227.50
0.4971 1324.00
0.5986 1399.10
0.6823 1458.40
0.6890 1463.00
0.7365 1493.80
0.7618 1510.20
0.7769 1520.00
0.7987 1534.00
0.8213 1548.20
0.8593 1571.50
0.8925 1591.60
0.9175 1606.50
0.9224 1610.80
0.9294 1614.70
0.9321 1616.30
0.9398 1620.10
0.9479 1625.00
0.9568 1630.00
0.9600 1634.00
0.9648 1636.00
0.9707 1639.50
0.9781 1643.50
0.9907 1651.00
0.9949 1653.50
1.0000 1656.40

Vapor or sublimation pressure, kPa [ref]

Fixed Measured
Temperature, K - Liquid Mole fraction of Dimethyl ether (2) - Liquid Vapor or sublimation pressure, kPa - Liquid
253.05 0.0000 307.20
253.05 0.0527 299.50
253.05 0.1317 287.60
253.05 0.2501 269.80
253.05 0.3571 252.80
253.05 0.4134 243.00
253.05 0.4638 234.80
253.05 0.4683 233.90
253.05 0.5620 218.40
253.05 0.5639 217.00
253.05 0.6165 208.00
253.05 0.6766 195.50
253.05 0.7735 176.30
253.05 0.8522 159.50
253.05 0.9366 140.50
253.05 1.0000 125.00
293.15 0.0000 1015.90
293.15 0.0533 993.90
293.15 0.1330 960.50
293.15 0.2520 909.80
293.15 0.3589 861.20
293.15 0.4136 834.90
293.15 0.4653 811.30
293.15 0.4689 809.60
293.15 0.5629 763.20
293.15 0.5652 761.50
293.15 0.6171 735.80
293.15 0.6786 702.20
293.15 0.7756 648.10
293.15 0.8540 601.60
293.15 0.9376 549.20
293.15 1.0000 508.10

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 313.1 (Liquid)

Mole fraction of Propene (1) - Liquid Vapor or sublimation pressure, kPa - Liquid
0.0000 891.60
0.0068 899.18
0.0542 945.55
0.1057 994.33
0.1680 1050.90
0.2325 1107.20
0.2940 1158.60
0.3546 1207.50
0.4032 1246.60
0.4169 1256.10
0.4696 1296.00
0.4856 1307.00
0.5286 1339.60
0.5793 1373.80
0.6740 1439.10
0.7633 1498.90
0.8379 1547.60
0.8967 1585.20
0.9419 1613.50
0.9704 1630.80
0.9833 1638.30
0.9952 1644.80
1.0000 1647.30

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 313.32 (Liquid)

Mole fraction of Propene (1) - Liquid Vapor or sublimation pressure, kPa - Liquid
0.0000 896.20
0.0307 927.90
0.0830 977.10
0.1125 1004.60
0.1353 1024.50
0.1845 1065.60
0.2687 1139.10
0.3753 1227.50
0.4971 1324.00
0.5986 1399.10
0.6823 1458.40
0.6890 1463.00
0.7365 1493.80
0.7618 1510.20
0.7769 1520.00
0.7987 1534.00
0.8213 1548.20
0.8593 1571.50
0.8925 1591.60
0.9175 1606.50
0.9224 1610.80
0.9294 1614.70
0.9321 1616.30
0.9398 1620.10
0.9479 1625.00
0.9568 1630.00
0.9600 1634.00
0.9648 1636.00
0.9707 1639.50
0.9781 1643.50
0.9907 1651.00
0.9949 1653.50
1.0000 1656.40

Vapor or sublimation pressure, kPa [ref]

Fixed Measured
Temperature, K - Liquid Mole fraction of Dimethyl ether (2) - Liquid Vapor or sublimation pressure, kPa - Liquid
253.05 0.0000 307.20
253.05 0.0527 299.50
253.05 0.1317 287.60
253.05 0.2501 269.80
253.05 0.3571 252.80
253.05 0.4134 243.00
253.05 0.4638 234.80
253.05 0.4683 233.90
253.05 0.5620 218.40
253.05 0.5639 217.00
253.05 0.6165 208.00
253.05 0.6766 195.50
253.05 0.7735 176.30
253.05 0.8522 159.50
253.05 0.9366 140.50
253.05 1.0000 125.00
293.15 0.0000 1015.90
293.15 0.0533 993.90
293.15 0.1330 960.50
293.15 0.2520 909.80
293.15 0.3589 861.20
293.15 0.4136 834.90
293.15 0.4653 811.30
293.15 0.4689 809.60
293.15 0.5629 763.20
293.15 0.5652 761.50
293.15 0.6171 735.80
293.15 0.6786 702.20
293.15 0.7756 648.10
293.15 0.8540 601.60
293.15 0.9376 549.20
293.15 1.0000 508.10

Sources