Mixture of Diethyl malonate + Heptane

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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

Heptane

Name
Heptane
InChI
InChI=1S/C7H16/c1-3-5-7-6-4-2/h3-7H2,1-2H3
InChI Key
IMNFDUFMRHMDMM-UHFFFAOYSA-N
Formula
C7H16
SMILES
CCCCCCC
Mol. Weight (g/mol)
100.20
CAS
142-82-5
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Datasets

  1. Excess molar enthalpy (molar enthalpy (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 (1) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
288.15 0.0581 0.4380
288.15 0.1086 0.7500
288.15 0.1476 0.9430
288.15 0.1984 1.151
288.15 0.2495 1.31
288.15 0.3007 1.48
288.15 0.3481 1.531
288.15 0.3997 1.584
288.15 0.4474 1.594
288.15 0.4993 1.601
288.15 0.5474 1.596
288.15 0.5997 1.571
288.15 0.6481 1.517
288.15 0.7008 1.45
288.15 0.7495 1.352
288.15 0.7985 1.2
288.15 0.8476 0.9900
288.15 0.9009 0.6990
288.15 0.9504 0.3710
298.15 0.0581 0.4190
298.15 0.1008 0.7160
298.15 0.1476 0.9700
298.15 0.1984 1.222
298.15 0.2495 1.456
298.15 0.3007 1.618
298.15 0.3481 1.733
298.15 0.3997 1.786
298.15 0.4474 1.815
298.15 0.4993 1.819
298.15 0.5474 1.81
298.15 0.5997 1.758
298.15 0.6481 1.696
298.15 0.7008 1.565
298.15 0.7495 1.442
298.15 0.7985 1.256
298.15 0.8476 1.022
298.15 0.9009 0.6970
298.15 0.9504 0.3730
313.15 0.0581 0.4310
313.15 0.1008 0.7170
313.15 0.1476 0.9970
313.15 0.1984 1.28
313.15 0.2495 1.514
313.15 0.3007 1.728
313.15 0.3481 1.856
313.15 0.3997 1.934
313.15 0.4474 1.962
313.15 0.4993 1.975
313.15 0.5474 1.948
313.15 0.5997 1.889
313.15 0.6481 1.812
313.15 0.7008 1.67
313.15 0.7495 1.496
313.15 0.7985 1.26
313.15 0.8476 1.029
313.15 0.9009 0.6910
313.15 0.9504 0.3710
328.15 0.0503 0.3750
328.15 0.1008 0.7470
328.15 0.1476 1.018
328.15 0.1984 1.311
328.15 0.2495 1.568
328.15 0.3007 1.766
328.15 0.3481 1.919
328.15 0.3997 2.02
328.15 0.4474 2.043
328.15 0.4993 2.049
328.15 0.5474 2.024
328.15 0.5997 1.954
328.15 0.6481 1.854
328.15 0.7008 1.727
328.15 0.7495 1.545
328.15 0.7985 1.348
328.15 0.8476 1.063
328.15 0.9009 0.7520
328.15 0.9504 0.4340
338.15 0.0503 0.3670
338.15 0.1008 0.7270
338.15 0.1476 1.032
338.15 0.1984 1.315
338.15 0.2495 1.548
338.15 0.3007 1.792
338.15 0.3481 1.895
338.15 0.3997 2.026
338.15 0.4474 2.068
338.15 0.4993 2.08
338.15 0.5474 2.054
338.15 0.5997 2.0
338.15 0.6481 1.884
338.15 0.7008 1.736
338.15 0.7495 1.539
338.15 0.7985 1.331
338.15 0.8476 1.074
338.15 0.9009 0.7430
338.15 0.9504 0.3930
348.15 0.0503 0.3780
348.15 0.1008 0.7260
348.15 0.1476 1.014
348.15 0.1984 1.286
348.15 0.2495 1.526
348.15 0.3007 1.726
348.15 0.3481 1.89
348.15 0.3997 1.984
348.15 0.4474 2.04
348.15 0.4993 2.055
348.15 0.5474 2.013
348.15 0.5997 1.934
348.15 0.6481 1.84
348.15 0.7008 1.673
348.15 0.7495 1.51
348.15 0.7985 1.299
348.15 0.8476 1.03
348.15 0.9009 0.7110
348.15 0.9504 0.3660

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 (1) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
288.15 0.0581 0.4380
288.15 0.1086 0.7500
288.15 0.1476 0.9430
288.15 0.1984 1.151
288.15 0.2495 1.31
288.15 0.3007 1.48
288.15 0.3481 1.531
288.15 0.3997 1.584
288.15 0.4474 1.594
288.15 0.4993 1.601
288.15 0.5474 1.596
288.15 0.5997 1.571
288.15 0.6481 1.517
288.15 0.7008 1.45
288.15 0.7495 1.352
288.15 0.7985 1.2
288.15 0.8476 0.9900
288.15 0.9009 0.6990
288.15 0.9504 0.3710
298.15 0.0581 0.4190
298.15 0.1008 0.7160
298.15 0.1476 0.9700
298.15 0.1984 1.222
298.15 0.2495 1.456
298.15 0.3007 1.618
298.15 0.3481 1.733
298.15 0.3997 1.786
298.15 0.4474 1.815
298.15 0.4993 1.819
298.15 0.5474 1.81
298.15 0.5997 1.758
298.15 0.6481 1.696
298.15 0.7008 1.565
298.15 0.7495 1.442
298.15 0.7985 1.256
298.15 0.8476 1.022
298.15 0.9009 0.6970
298.15 0.9504 0.3730
313.15 0.0581 0.4310
313.15 0.1008 0.7170
313.15 0.1476 0.9970
313.15 0.1984 1.28
313.15 0.2495 1.514
313.15 0.3007 1.728
313.15 0.3481 1.856
313.15 0.3997 1.934
313.15 0.4474 1.962
313.15 0.4993 1.975
313.15 0.5474 1.948
313.15 0.5997 1.889
313.15 0.6481 1.812
313.15 0.7008 1.67
313.15 0.7495 1.496
313.15 0.7985 1.26
313.15 0.8476 1.029
313.15 0.9009 0.6910
313.15 0.9504 0.3710
328.15 0.0503 0.3750
328.15 0.1008 0.7470
328.15 0.1476 1.018
328.15 0.1984 1.311
328.15 0.2495 1.568
328.15 0.3007 1.766
328.15 0.3481 1.919
328.15 0.3997 2.02
328.15 0.4474 2.043
328.15 0.4993 2.049
328.15 0.5474 2.024
328.15 0.5997 1.954
328.15 0.6481 1.854
328.15 0.7008 1.727
328.15 0.7495 1.545
328.15 0.7985 1.348
328.15 0.8476 1.063
328.15 0.9009 0.7520
328.15 0.9504 0.4340
338.15 0.0503 0.3670
338.15 0.1008 0.7270
338.15 0.1476 1.032
338.15 0.1984 1.315
338.15 0.2495 1.548
338.15 0.3007 1.792
338.15 0.3481 1.895
338.15 0.3997 2.026
338.15 0.4474 2.068
338.15 0.4993 2.08
338.15 0.5474 2.054
338.15 0.5997 2.0
338.15 0.6481 1.884
338.15 0.7008 1.736
338.15 0.7495 1.539
338.15 0.7985 1.331
338.15 0.8476 1.074
338.15 0.9009 0.7430
338.15 0.9504 0.3930
348.15 0.0503 0.3780
348.15 0.1008 0.7260
348.15 0.1476 1.014
348.15 0.1984 1.286
348.15 0.2495 1.526
348.15 0.3007 1.726
348.15 0.3481 1.89
348.15 0.3997 1.984
348.15 0.4474 2.04
348.15 0.4993 2.055
348.15 0.5474 2.013
348.15 0.5997 1.934
348.15 0.6481 1.84
348.15 0.7008 1.673
348.15 0.7495 1.51
348.15 0.7985 1.299
348.15 0.8476 1.03
348.15 0.9009 0.7110
348.15 0.9504 0.3660

Sources