Mixture of 1-Propanol + Diethyl malonate

Excel

1-Propanol

Name
1-Propanol
InChI
InChI=1S/C3H8O/c1-2-3-4/h4H,2-3H2,1H3
InChI Key
BDERNNFJNOPAEC-UHFFFAOYSA-N
Formula
C3H8O
SMILES
CCCO
Mol. Weight (g/mol)
60.09
CAS
71-23-8

Diethyl malonate

Name
Diethyl malonate
InChI
InChI=1S/C7H12O4/c1-3-10-6(8)5-7(9)11-4-2/h3-5H2,1-2H3
InChI Key
IYXGSMUGOJNHAZ-UHFFFAOYSA-N
Formula
C7H12O4
SMILES
CCOC(=O)CC(=O)OCC
Mol. Weight (g/mol)
160.17
CAS
105-53-3
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Datasets

  1. Excess molar enthalpy (molar enthalpy (2)
  2. ρl - Mass density, kg/m3 (2)

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

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Diethyl malonate (2) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
288.20 0.0499 0.4870
288.20 0.1004 0.8660
288.20 0.2513 1.595
288.20 0.3000 1.738
288.20 0.3491 1.853
288.20 0.3982 1.935
288.20 0.4510 1.976
288.20 0.4990 1.998
288.20 0.5503 1.982
288.20 0.6002 1.932
288.20 0.6479 1.862
288.20 0.6986 1.755
288.20 0.7525 1.575
288.20 0.7970 1.399
288.20 0.8506 1.126
288.20 0.9003 0.8210
288.20 0.9527 0.4380
298.20 0.0499 0.5340
298.20 0.1004 0.9410
298.20 0.1588 1.315
298.20 0.2090 1.575
298.20 0.2513 1.751
298.20 0.3000 1.908
298.20 0.3491 2.029
298.20 0.3982 2.11
298.20 0.4510 2.156
298.20 0.4990 2.175
298.20 0.5503 2.142
298.20 0.6002 2.08
298.20 0.6479 1.992
298.20 0.6986 1.872
298.20 0.7525 1.669
298.20 0.7970 1.473
298.20 0.8506 1.173
298.20 0.9003 0.8260
298.20 0.9527 0.4350
313.20 0.0499 0.5780
313.20 0.1004 1.045
313.20 0.1588 1.444
313.20 0.2090 1.738
313.20 0.2513 1.915
313.20 0.3000 2.094
313.20 0.3491 2.231
313.20 0.3982 2.32
313.20 0.4510 2.363
313.20 0.4990 2.371
313.20 0.5503 2.338
313.20 0.6002 2.256
313.20 0.6479 2.14
313.20 0.6986 1.967
313.20 0.7525 1.747
313.20 0.7970 1.511
313.20 0.8506 1.188
313.20 0.9003 0.8560
313.20 0.9527 0.4320
328.20 0.0499 0.5970
328.20 0.1004 1.112
328.20 0.1588 1.554
328.20 0.2090 1.872
328.20 0.2513 2.054
328.20 0.3000 2.244
328.20 0.3491 2.387
328.20 0.3982 2.482
328.20 0.4510 2.525
328.20 0.4990 2.517
328.20 0.5503 2.477
328.20 0.6002 2.374
328.20 0.6479 2.255
328.20 0.6986 2.064
328.20 0.7525 1.817
328.20 0.7970 1.569
328.20 0.8506 1.23
328.20 0.9003 0.8540
328.20 0.9527 0.4180

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

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Diethyl malonate (2) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
288.20 0.0499 0.4870
288.20 0.1004 0.8660
288.20 0.2513 1.595
288.20 0.3000 1.738
288.20 0.3491 1.853
288.20 0.3982 1.935
288.20 0.4510 1.976
288.20 0.4990 1.998
288.20 0.5503 1.982
288.20 0.6002 1.932
288.20 0.6479 1.862
288.20 0.6986 1.755
288.20 0.7525 1.575
288.20 0.7970 1.399
288.20 0.8506 1.126
288.20 0.9003 0.8210
288.20 0.9527 0.4380
298.20 0.0499 0.5340
298.20 0.1004 0.9410
298.20 0.1588 1.315
298.20 0.2090 1.575
298.20 0.2513 1.751
298.20 0.3000 1.908
298.20 0.3491 2.029
298.20 0.3982 2.11
298.20 0.4510 2.156
298.20 0.4990 2.175
298.20 0.5503 2.142
298.20 0.6002 2.08
298.20 0.6479 1.992
298.20 0.6986 1.872
298.20 0.7525 1.669
298.20 0.7970 1.473
298.20 0.8506 1.173
298.20 0.9003 0.8260
298.20 0.9527 0.4350
313.20 0.0499 0.5780
313.20 0.1004 1.045
313.20 0.1588 1.444
313.20 0.2090 1.738
313.20 0.2513 1.915
313.20 0.3000 2.094
313.20 0.3491 2.231
313.20 0.3982 2.32
313.20 0.4510 2.363
313.20 0.4990 2.371
313.20 0.5503 2.338
313.20 0.6002 2.256
313.20 0.6479 2.14
313.20 0.6986 1.967
313.20 0.7525 1.747
313.20 0.7970 1.511
313.20 0.8506 1.188
313.20 0.9003 0.8560
313.20 0.9527 0.4320
328.20 0.0499 0.5970
328.20 0.1004 1.112
328.20 0.1588 1.554
328.20 0.2090 1.872
328.20 0.2513 2.054
328.20 0.3000 2.244
328.20 0.3491 2.387
328.20 0.3982 2.482
328.20 0.4510 2.525
328.20 0.4990 2.517
328.20 0.5503 2.477
328.20 0.6002 2.374
328.20 0.6479 2.255
328.20 0.6986 2.064
328.20 0.7525 1.817
328.20 0.7970 1.569
328.20 0.8506 1.23
328.20 0.9003 0.8540
328.20 0.9527 0.4180

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Diethyl malonate (2) - Liquid Mass density, kg/m3 - Liquid
288.15 0.0000 809.009
288.15 0.1001 854.156
288.15 0.2000 891.858
288.15 0.2999 923.874
288.15 0.3501 938.229
288.15 0.4001 951.433
288.15 0.4499 963.765
288.15 0.4999 975.313
288.15 0.5446 985.016
288.15 0.5997 996.235
288.15 0.7003 1014.958
288.15 0.7998 1031.529
288.15 0.8997 1046.546
288.15 1.0000 1060.326
298.15 0.0000 800.973
298.15 0.1001 845.431
298.15 0.2000 882.638
298.15 0.2999 914.254
298.15 0.3501 928.438
298.15 0.4001 941.51
298.15 0.4499 953.71
298.15 0.4999 965.148
298.15 0.5446 974.758
298.15 0.5997 985.888
298.15 0.7003 1004.461
298.15 0.7998 1020.939
298.15 0.8997 1035.873
298.15 1.0000 1049.603
313.15 0.0000 788.687
313.15 0.1001 832.128
313.15 0.2000 868.577
313.15 0.2999 899.629
313.15 0.3501 913.567
313.15 0.4001 926.45
313.15 0.4499 938.475
313.15 0.4999 949.737
313.15 0.5446 959.257
313.15 0.5997 970.245
313.15 0.7003 988.638
313.15 0.7998 1004.987
313.15 0.8997 1019.842
313.15 1.0000 1033.498
328.15 0.0000 775.974
328.15 0.1001 818.439
328.15 0.2000 854.173
328.15 0.2999 884.69
328.15 0.3501 898.431
328.15 0.4001 911.123
328.15 0.4499 922.986
328.15 0.4999 934.134
328.15 0.5446 943.524
328.15 0.5997 954.437
328.15 0.7003 972.67
328.15 0.7998 988.923
328.15 0.8997 1003.721
328.15 1.0000 1017.336

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Diethyl malonate (2) - Liquid Mass density, kg/m3 - Liquid
288.15 0.0000 809.009
288.15 0.1001 854.156
288.15 0.2000 891.858
288.15 0.2999 923.874
288.15 0.3501 938.229
288.15 0.4001 951.433
288.15 0.4499 963.765
288.15 0.4999 975.313
288.15 0.5446 985.016
288.15 0.5997 996.235
288.15 0.7003 1014.958
288.15 0.7998 1031.529
288.15 0.8997 1046.546
288.15 1.0000 1060.326
298.15 0.0000 800.973
298.15 0.1001 845.431
298.15 0.2000 882.638
298.15 0.2999 914.254
298.15 0.3501 928.438
298.15 0.4001 941.51
298.15 0.4499 953.71
298.15 0.4999 965.148
298.15 0.5446 974.758
298.15 0.5997 985.888
298.15 0.7003 1004.461
298.15 0.7998 1020.939
298.15 0.8997 1035.873
298.15 1.0000 1049.603
313.15 0.0000 788.687
313.15 0.1001 832.128
313.15 0.2000 868.577
313.15 0.2999 899.629
313.15 0.3501 913.567
313.15 0.4001 926.45
313.15 0.4499 938.475
313.15 0.4999 949.737
313.15 0.5446 959.257
313.15 0.5997 970.245
313.15 0.7003 988.638
313.15 0.7998 1004.987
313.15 0.8997 1019.842
313.15 1.0000 1033.498
328.15 0.0000 775.974
328.15 0.1001 818.439
328.15 0.2000 854.173
328.15 0.2999 884.69
328.15 0.3501 898.431
328.15 0.4001 911.123
328.15 0.4499 922.986
328.15 0.4999 934.134
328.15 0.5446 943.524
328.15 0.5997 954.437
328.15 0.7003 972.67
328.15 0.7998 988.923
328.15 0.8997 1003.721
328.15 1.0000 1017.336

Sources