Mixture of Isopropyl Alcohol + Diethyl malonate

Excel

Isopropyl Alcohol

Name
Isopropyl Alcohol
InChI
InChI=1S/C3H8O/c1-3(2)4/h3-4H,1-2H3
InChI Key
KFZMGEQAYNKOFK-UHFFFAOYSA-N
Formula
C3H8O
SMILES
CC(C)O
Mol. Weight (g/mol)
60.09
CAS
67-63-0

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 0.0511 0.6070
288.20 0.1001 1.022
288.20 0.1511 1.347
288.20 0.2012 1.619
288.20 0.2494 1.803
288.20 0.3015 1.965
288.20 0.3507 2.091
288.20 0.3998 2.161
288.20 0.4484 2.188
288.20 0.5003 2.193
288.20 0.5513 2.173
288.20 0.6007 2.097
288.20 0.6478 2.019
288.20 0.6977 1.88
288.20 0.7508 1.667
288.20 0.8007 1.444
288.20 0.8468 1.196
288.20 0.9023 0.7730
288.20 0.9537 0.4030
298.20 0.0511 0.6320
298.20 0.1001 1.102
298.20 0.1511 1.465
298.20 0.2012 1.753
298.20 0.2494 1.955
298.20 0.3015 2.134
298.20 0.3507 2.266
298.20 0.3998 2.344
298.20 0.4484 2.38
298.20 0.5003 2.369
298.20 0.5513 2.342
298.20 0.6007 2.257
298.20 0.6478 2.175
298.20 0.6977 2.015
298.20 0.7508 1.804
298.20 0.8007 1.584
298.20 0.8468 1.292
298.20 0.9023 0.9180
298.20 0.9537 0.4650
313.20 0.0511 0.6590
313.20 0.1001 1.16
313.20 0.1511 1.581
313.20 0.2012 1.877
313.20 0.2494 2.134
313.20 0.3015 2.329
313.20 0.3507 2.451
313.20 0.3998 2.534
313.20 0.4484 2.578
313.20 0.5003 2.556
313.20 0.5513 2.51
313.20 0.6007 2.433
313.20 0.6478 2.321
313.20 0.6977 2.137
313.20 0.7508 1.888
313.20 0.8007 1.636
313.20 0.8468 1.339
313.20 0.9023 0.8920
313.20 0.9537 0.4360
328.20 0.0511 0.6810
328.20 0.1001 1.22
328.20 0.1511 1.631
328.20 0.2012 1.977
328.20 0.2494 2.223
328.20 0.3015 2.412
328.20 0.3507 2.555
328.20 0.3998 2.636
328.20 0.4484 2.674
328.20 0.5003 2.664
328.20 0.5513 2.595
328.20 0.6007 2.496
328.20 0.6478 2.348
328.20 0.6977 2.161
328.20 0.7508 1.901
328.20 0.8007 1.618
328.20 0.8468 1.264
328.20 0.9023 0.8450
328.20 0.9537 0.3910

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 0.0511 0.6070
288.20 0.1001 1.022
288.20 0.1511 1.347
288.20 0.2012 1.619
288.20 0.2494 1.803
288.20 0.3015 1.965
288.20 0.3507 2.091
288.20 0.3998 2.161
288.20 0.4484 2.188
288.20 0.5003 2.193
288.20 0.5513 2.173
288.20 0.6007 2.097
288.20 0.6478 2.019
288.20 0.6977 1.88
288.20 0.7508 1.667
288.20 0.8007 1.444
288.20 0.8468 1.196
288.20 0.9023 0.7730
288.20 0.9537 0.4030
298.20 0.0511 0.6320
298.20 0.1001 1.102
298.20 0.1511 1.465
298.20 0.2012 1.753
298.20 0.2494 1.955
298.20 0.3015 2.134
298.20 0.3507 2.266
298.20 0.3998 2.344
298.20 0.4484 2.38
298.20 0.5003 2.369
298.20 0.5513 2.342
298.20 0.6007 2.257
298.20 0.6478 2.175
298.20 0.6977 2.015
298.20 0.7508 1.804
298.20 0.8007 1.584
298.20 0.8468 1.292
298.20 0.9023 0.9180
298.20 0.9537 0.4650
313.20 0.0511 0.6590
313.20 0.1001 1.16
313.20 0.1511 1.581
313.20 0.2012 1.877
313.20 0.2494 2.134
313.20 0.3015 2.329
313.20 0.3507 2.451
313.20 0.3998 2.534
313.20 0.4484 2.578
313.20 0.5003 2.556
313.20 0.5513 2.51
313.20 0.6007 2.433
313.20 0.6478 2.321
313.20 0.6977 2.137
313.20 0.7508 1.888
313.20 0.8007 1.636
313.20 0.8468 1.339
313.20 0.9023 0.8920
313.20 0.9537 0.4360
328.20 0.0511 0.6810
328.20 0.1001 1.22
328.20 0.1511 1.631
328.20 0.2012 1.977
328.20 0.2494 2.223
328.20 0.3015 2.412
328.20 0.3507 2.555
328.20 0.3998 2.636
328.20 0.4484 2.674
328.20 0.5003 2.664
328.20 0.5513 2.595
328.20 0.6007 2.496
328.20 0.6478 2.348
328.20 0.6977 2.161
328.20 0.7508 1.901
328.20 0.8007 1.618
328.20 0.8468 1.264
328.20 0.9023 0.8450
328.20 0.9537 0.3910

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 789.342
288.15 0.1001 836.917
288.15 0.2000 877.015
288.15 0.3000 911.283
288.15 0.3501 926.715
288.15 0.4000 940.924
288.15 0.4550 955.561
288.15 0.4999 966.784
288.15 0.5501 978.638
288.15 0.5999 989.637
288.15 0.6499 1000.133
288.15 0.7001 1010.027
288.15 0.8000 1028.364
288.15 0.8995 1044.944
288.15 1.0000 1060.326
298.15 0.0000 780.99
298.15 0.1001 827.809
298.15 0.2000 867.404
298.15 0.3000 901.308
298.15 0.3501 916.6
298.15 0.4000 930.696
298.15 0.4550 945.23
298.15 0.4999 956.373
298.15 0.5501 968.162
298.15 0.5999 979.111
298.15 0.6499 989.567
298.15 0.7001 999.417
298.15 0.8000 1017.693
298.15 0.8995 1034.258
298.15 1.0000 1049.603
313.15 0.0000 767.922
313.15 0.1001 813.707
313.15 0.2000 852.617
313.15 0.3000 886.063
313.15 0.3501 901.155
313.15 0.4000 915.119
313.15 0.4550 929.523
313.15 0.4999 940.573
313.15 0.5501 952.282
313.15 0.5999 963.18
313.15 0.6499 973.566
313.15 0.7001 983.39
313.15 0.8000 1001.629
313.15 0.8995 1018.177
313.15 1.0000 1033.498
328.15 0.0000 754.001
328.15 0.1001 798.938
328.15 0.2000 837.294
328.15 0.3000 870.365
328.15 0.3501 885.344
328.15 0.4000 899.194
328.15 0.4550 913.507
328.15 0.4999 924.508
328.15 0.5501 936.171
328.15 0.5999 947.033
328.15 0.6499 957.417
328.15 0.7001 967.228
328.15 0.8000 985.453
328.15 0.8995 1002.012
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 789.342
288.15 0.1001 836.917
288.15 0.2000 877.015
288.15 0.3000 911.283
288.15 0.3501 926.715
288.15 0.4000 940.924
288.15 0.4550 955.561
288.15 0.4999 966.784
288.15 0.5501 978.638
288.15 0.5999 989.637
288.15 0.6499 1000.133
288.15 0.7001 1010.027
288.15 0.8000 1028.364
288.15 0.8995 1044.944
288.15 1.0000 1060.326
298.15 0.0000 780.99
298.15 0.1001 827.809
298.15 0.2000 867.404
298.15 0.3000 901.308
298.15 0.3501 916.6
298.15 0.4000 930.696
298.15 0.4550 945.23
298.15 0.4999 956.373
298.15 0.5501 968.162
298.15 0.5999 979.111
298.15 0.6499 989.567
298.15 0.7001 999.417
298.15 0.8000 1017.693
298.15 0.8995 1034.258
298.15 1.0000 1049.603
313.15 0.0000 767.922
313.15 0.1001 813.707
313.15 0.2000 852.617
313.15 0.3000 886.063
313.15 0.3501 901.155
313.15 0.4000 915.119
313.15 0.4550 929.523
313.15 0.4999 940.573
313.15 0.5501 952.282
313.15 0.5999 963.18
313.15 0.6499 973.566
313.15 0.7001 983.39
313.15 0.8000 1001.629
313.15 0.8995 1018.177
313.15 1.0000 1033.498
328.15 0.0000 754.001
328.15 0.1001 798.938
328.15 0.2000 837.294
328.15 0.3000 870.365
328.15 0.3501 885.344
328.15 0.4000 899.194
328.15 0.4550 913.507
328.15 0.4999 924.508
328.15 0.5501 936.171
328.15 0.5999 947.033
328.15 0.6499 957.417
328.15 0.7001 967.228
328.15 0.8000 985.453
328.15 0.8995 1002.012
328.15 1.0000 1017.336

Sources