Mixture of Diethyl malonate + 1-Propanol, 2-methyl-

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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

1-Propanol, 2-methyl-

Name
1-Propanol, 2-methyl-
InChI
InChI=1S/C4H10O/c1-4(2)3-5/h4-5H,3H2,1-2H3
InChI Key
ZXEKIIBDNHEJCQ-UHFFFAOYSA-N
Formula
C4H10O
SMILES
CC(C)CO
Mol. Weight (g/mol)
74.12
CAS
78-83-1
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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 (1) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
288.15 0.0502 0.6110
288.15 0.0983 1.054
288.15 0.1494 1.397
288.15 0.2006 1.681
288.15 0.2484 1.89
288.15 0.2989 2.06
288.15 0.3486 2.183
288.15 0.3972 2.265
288.15 0.4484 2.314
288.15 0.4981 2.342
288.15 0.5504 2.316
288.15 0.6006 2.23
288.15 0.6485 2.135
288.15 0.6985 1.992
288.15 0.7508 1.767
288.15 0.8000 1.531
288.15 0.8514 1.233
288.15 0.8990 0.8370
288.15 0.9485 0.4810
298.15 0.0502 0.6110
298.15 0.0983 1.108
298.15 0.1494 1.499
298.15 0.2006 1.773
298.15 0.2484 2.053
298.15 0.2989 2.247
298.15 0.3486 2.358
298.15 0.3972 2.463
298.15 0.4484 2.504
298.15 0.4981 2.542
298.15 0.5504 2.49
298.15 0.6006 2.401
298.15 0.6485 2.29
298.15 0.6985 2.104
298.15 0.7508 1.907
298.15 0.8000 1.634
298.15 0.8514 1.298
298.15 0.8990 0.9120
298.15 0.9485 0.4660
313.15 0.0502 0.6900
313.15 0.0983 1.224
313.15 0.1494 1.657
313.15 0.2006 2.002
313.15 0.2484 2.271
313.15 0.2989 2.46
313.15 0.3486 2.605
313.15 0.3972 2.709
313.15 0.4484 2.737
313.15 0.4981 2.725
313.15 0.5504 2.664
313.15 0.6006 2.57
313.15 0.6485 2.427
313.15 0.6985 2.251
313.15 0.7508 1.998
313.15 0.8000 1.701
313.15 0.8514 1.358
313.15 0.8990 0.9870
313.15 0.9485 0.5550
328.15 0.0502 0.7040
328.15 0.0983 1.256
328.15 0.1494 1.674
328.15 0.2006 2.086
328.15 0.2484 2.314
328.15 0.2989 2.565
328.15 0.3486 2.723
328.15 0.3972 2.77
328.15 0.4484 2.825
328.15 0.4981 2.811
328.15 0.5504 2.739
328.15 0.6006 2.604
328.15 0.6485 2.453
328.15 0.6985 2.24
328.15 0.7508 1.971
328.15 0.8000 1.662
328.15 0.8514 1.31
328.15 0.8990 0.9030
328.15 0.9485 0.4960
338.15 0.0502 0.6940
338.15 0.0983 1.245
338.15 0.1494 1.701
338.15 0.2006 2.089
338.15 0.2484 2.338
338.15 0.2989 2.55
338.15 0.3486 2.71
338.15 0.3972 2.798
338.15 0.4484 2.82
338.15 0.4981 2.803
338.15 0.5504 2.735
338.15 0.6006 2.585
338.15 0.6485 2.439
338.15 0.6985 2.201
338.15 0.7508 1.927
338.15 0.8000 1.624
338.15 0.8514 1.274
338.15 0.8990 0.9380
338.15 0.9485 0.5190
348.15 0.0502 0.6660
348.15 0.0983 1.239
348.15 0.1494 1.696
348.15 0.2006 2.07
348.15 0.2484 2.334
348.15 0.2989 2.561
348.15 0.3486 2.701
348.15 0.3972 2.782
348.15 0.4484 2.812
348.15 0.4981 2.784
348.15 0.5504 2.699
348.15 0.6006 2.582
348.15 0.6485 2.415
348.15 0.6985 2.206
348.15 0.7508 1.934
348.15 0.8000 1.609
348.15 0.8514 1.241
348.15 0.8990 0.8820
348.15 0.9485 0.4850

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 0.0502 0.6110
288.15 0.0983 1.054
288.15 0.1494 1.397
288.15 0.2006 1.681
288.15 0.2484 1.89
288.15 0.2989 2.06
288.15 0.3486 2.183
288.15 0.3972 2.265
288.15 0.4484 2.314
288.15 0.4981 2.342
288.15 0.5504 2.316
288.15 0.6006 2.23
288.15 0.6485 2.135
288.15 0.6985 1.992
288.15 0.7508 1.767
288.15 0.8000 1.531
288.15 0.8514 1.233
288.15 0.8990 0.8370
288.15 0.9485 0.4810
298.15 0.0502 0.6110
298.15 0.0983 1.108
298.15 0.1494 1.499
298.15 0.2006 1.773
298.15 0.2484 2.053
298.15 0.2989 2.247
298.15 0.3486 2.358
298.15 0.3972 2.463
298.15 0.4484 2.504
298.15 0.4981 2.542
298.15 0.5504 2.49
298.15 0.6006 2.401
298.15 0.6485 2.29
298.15 0.6985 2.104
298.15 0.7508 1.907
298.15 0.8000 1.634
298.15 0.8514 1.298
298.15 0.8990 0.9120
298.15 0.9485 0.4660
313.15 0.0502 0.6900
313.15 0.0983 1.224
313.15 0.1494 1.657
313.15 0.2006 2.002
313.15 0.2484 2.271
313.15 0.2989 2.46
313.15 0.3486 2.605
313.15 0.3972 2.709
313.15 0.4484 2.737
313.15 0.4981 2.725
313.15 0.5504 2.664
313.15 0.6006 2.57
313.15 0.6485 2.427
313.15 0.6985 2.251
313.15 0.7508 1.998
313.15 0.8000 1.701
313.15 0.8514 1.358
313.15 0.8990 0.9870
313.15 0.9485 0.5550
328.15 0.0502 0.7040
328.15 0.0983 1.256
328.15 0.1494 1.674
328.15 0.2006 2.086
328.15 0.2484 2.314
328.15 0.2989 2.565
328.15 0.3486 2.723
328.15 0.3972 2.77
328.15 0.4484 2.825
328.15 0.4981 2.811
328.15 0.5504 2.739
328.15 0.6006 2.604
328.15 0.6485 2.453
328.15 0.6985 2.24
328.15 0.7508 1.971
328.15 0.8000 1.662
328.15 0.8514 1.31
328.15 0.8990 0.9030
328.15 0.9485 0.4960
338.15 0.0502 0.6940
338.15 0.0983 1.245
338.15 0.1494 1.701
338.15 0.2006 2.089
338.15 0.2484 2.338
338.15 0.2989 2.55
338.15 0.3486 2.71
338.15 0.3972 2.798
338.15 0.4484 2.82
338.15 0.4981 2.803
338.15 0.5504 2.735
338.15 0.6006 2.585
338.15 0.6485 2.439
338.15 0.6985 2.201
338.15 0.7508 1.927
338.15 0.8000 1.624
338.15 0.8514 1.274
338.15 0.8990 0.9380
338.15 0.9485 0.5190
348.15 0.0502 0.6660
348.15 0.0983 1.239
348.15 0.1494 1.696
348.15 0.2006 2.07
348.15 0.2484 2.334
348.15 0.2989 2.561
348.15 0.3486 2.701
348.15 0.3972 2.782
348.15 0.4484 2.812
348.15 0.4981 2.784
348.15 0.5504 2.699
348.15 0.6006 2.582
348.15 0.6485 2.415
348.15 0.6985 2.206
348.15 0.7508 1.934
348.15 0.8000 1.609
348.15 0.8514 1.241
348.15 0.8990 0.8820
348.15 0.9485 0.4850

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Diethyl malonate (1) - Liquid Mass density, kg/m3 - Liquid
288.15 0.0000 805.6
288.15 0.1000 843.381
288.15 0.2000 877.394
288.15 0.3000 908.051
288.15 0.3500 922.305
288.15 0.3999 935.772
288.15 0.4495 948.602
288.15 0.5001 961.044
288.15 0.6001 984.156
288.15 0.6999 1005.333
288.15 0.8003 1025.057
288.15 0.9000 1043.277
288.15 1.0000 1060.326
298.15 0.0000 797.916
298.15 0.1000 835.034
298.15 0.2000 868.517
298.15 0.3000 898.746
298.15 0.3500 912.816
298.15 0.3999 926.126
298.15 0.4495 938.806
298.15 0.5001 951.116
298.15 0.6001 973.999
298.15 0.6999 995.001
298.15 0.8003 1014.571
298.15 0.9000 1032.669
298.15 1.0000 1049.603
313.15 0.0000 786.069
313.15 0.1000 822.221
313.15 0.2000 854.953
313.15 0.3000 884.583
313.15 0.3500 898.402
313.15 0.3999 911.47
313.15 0.4495 923.966
313.15 0.5001 936.085
313.15 0.6001 958.66
313.15 0.6999 979.414
313.15 0.8003 998.792
313.15 0.9000 1016.712
313.15 1.0000 1033.498
328.15 0.0000 773.692
328.15 0.1000 808.976
328.15 0.2000 841.015
328.15 0.3000 870.102
328.15 0.3500 885.344
328.15 0.3999 896.55
328.15 0.4495 908.867
328.15 0.5001 920.835
328.15 0.6001 943.14
328.15 0.6999 963.679
328.15 0.8003 982.885
328.15 0.9000 1000.67
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 (1) - Liquid Mass density, kg/m3 - Liquid
288.15 0.0000 805.6
288.15 0.1000 843.381
288.15 0.2000 877.394
288.15 0.3000 908.051
288.15 0.3500 922.305
288.15 0.3999 935.772
288.15 0.4495 948.602
288.15 0.5001 961.044
288.15 0.6001 984.156
288.15 0.6999 1005.333
288.15 0.8003 1025.057
288.15 0.9000 1043.277
288.15 1.0000 1060.326
298.15 0.0000 797.916
298.15 0.1000 835.034
298.15 0.2000 868.517
298.15 0.3000 898.746
298.15 0.3500 912.816
298.15 0.3999 926.126
298.15 0.4495 938.806
298.15 0.5001 951.116
298.15 0.6001 973.999
298.15 0.6999 995.001
298.15 0.8003 1014.571
298.15 0.9000 1032.669
298.15 1.0000 1049.603
313.15 0.0000 786.069
313.15 0.1000 822.221
313.15 0.2000 854.953
313.15 0.3000 884.583
313.15 0.3500 898.402
313.15 0.3999 911.47
313.15 0.4495 923.966
313.15 0.5001 936.085
313.15 0.6001 958.66
313.15 0.6999 979.414
313.15 0.8003 998.792
313.15 0.9000 1016.712
313.15 1.0000 1033.498
328.15 0.0000 773.692
328.15 0.1000 808.976
328.15 0.2000 841.015
328.15 0.3000 870.102
328.15 0.3500 885.344
328.15 0.3999 896.55
328.15 0.4495 908.867
328.15 0.5001 920.835
328.15 0.6001 943.14
328.15 0.6999 963.679
328.15 0.8003 982.885
328.15 0.9000 1000.67
328.15 1.0000 1017.336

Sources