Mixture of Ethyl acetoacetate + Methyl Alcohol

Excel

Ethyl acetoacetate

Name
Ethyl acetoacetate
InChI
InChI=1S/C6H10O3/c1-3-9-6(8)4-5(2)7/h3-4H2,1-2H3
InChI Key
XYIBRDXRRQCHLP-UHFFFAOYSA-N
Formula
C6H10O3
SMILES
CCOC(=O)CC(C)=O
Mol. Weight (g/mol)
130.14
CAS
141-97-9

Methyl Alcohol

Name
Methyl Alcohol
InChI
InChI=1S/CH4O/c1-2/h2H,1H3
InChI Key
OKKJLVBELUTLKV-UHFFFAOYSA-N
Formula
CH4O
SMILES
CO
Mol. Weight (g/mol)
32.04
CAS
67-56-1
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Datasets

  1. Excess molar enthalpy (molar enthalpy (2)

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

Fixed Measured
Temperature, K - Liquid Pressure, kPa - Liquid Mole fraction of Ethyl acetoacetate (1) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
298.15 100.00 0.0998 0.5032
298.15 100.00 0.2002 0.8451
298.15 100.00 0.2994 1.0708
298.15 100.00 0.3505 1.1472
298.15 100.00 0.3995 1.2001
298.15 100.00 0.4495 1.2328
298.15 100.00 0.4998 1.2452
298.15 100.00 0.5495 1.2366
298.15 100.00 0.5997 1.2068
298.15 100.00 0.6500 1.1513
298.15 100.00 0.6995 1.0741
298.15 100.00 0.7994 0.8324
298.15 100.00 0.8982 0.4647
298.15 10000.00 0.0996 0.4843
298.15 10000.00 0.1999 0.8222
298.15 10000.00 0.2990 1.0357
298.15 10000.00 0.3500 1.1086
298.15 10000.00 0.3990 1.1567
298.15 10000.00 0.4490 1.1844
298.15 10000.00 0.4993 1.1955
298.15 10000.00 0.5489 1.1837
298.15 10000.00 0.5992 1.1485
298.15 10000.00 0.6495 1.094
298.15 10000.00 0.6990 1.0123
298.15 10000.00 0.7990 0.7600
298.15 10000.00 0.8980 0.4125
313.15 100.00 0.0998 0.5630
313.15 100.00 0.2002 0.9487
313.15 100.00 0.2994 1.1909
313.15 100.00 0.3505 1.2762
313.15 100.00 0.3995 1.3298
313.15 100.00 0.4495 1.3639
313.15 100.00 0.4998 1.3798
313.15 100.00 0.5495 1.3625
313.15 100.00 0.5997 1.3307
313.15 100.00 0.6500 1.27
313.15 100.00 0.6995 1.1667
313.15 100.00 0.7994 0.8837
313.15 100.00 0.8982 0.4793
313.15 10000.00 0.0996 0.5554
313.15 10000.00 0.1999 0.9408
313.15 10000.00 0.2990 1.1838
313.15 10000.00 0.3500 1.2696
313.15 10000.00 0.3990 1.3272
313.15 10000.00 0.4490 1.3606
313.15 10000.00 0.4993 1.3749
313.15 10000.00 0.5489 1.3577
313.15 10000.00 0.5992 1.3248
313.15 10000.00 0.6495 1.2586
313.15 10000.00 0.6990 1.1412
313.15 10000.00 0.7990 0.8755
313.15 10000.00 0.8980 0.4717
328.15 100.00 0.0998 0.6122
328.15 100.00 0.2002 1.0216
328.15 100.00 0.2994 1.2948
328.15 100.00 0.3505 1.3872
328.15 100.00 0.3995 1.4483
328.15 100.00 0.4495 1.4822
328.15 100.00 0.4998 1.4922
328.15 100.00 0.5495 1.474
328.15 100.00 0.5997 1.4285
328.15 100.00 0.6500 1.3527
328.15 100.00 0.6995 1.2493
328.15 100.00 0.7994 0.9365
328.15 100.00 0.8982 0.5020
328.15 10000.00 0.0996 0.6055
328.15 10000.00 0.1999 1.02
328.15 10000.00 0.2990 1.2911
328.15 10000.00 0.3500 1.383
328.15 10000.00 0.3990 1.4457
328.15 10000.00 0.4490 1.4814
328.15 10000.00 0.4993 1.4908
328.15 10000.00 0.5489 1.4725
328.15 10000.00 0.5992 1.4248
328.15 10000.00 0.6495 1.3468
328.15 10000.00 0.6990 1.2409
328.15 10000.00 0.7990 0.9306
328.15 10000.00 0.8980 0.4953

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

Fixed Measured
Temperature, K - Liquid Pressure, kPa - Liquid Mole fraction of Ethyl acetoacetate (1) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
298.15 100.00 0.0998 0.5032
298.15 100.00 0.2002 0.8451
298.15 100.00 0.2994 1.0708
298.15 100.00 0.3505 1.1472
298.15 100.00 0.3995 1.2001
298.15 100.00 0.4495 1.2328
298.15 100.00 0.4998 1.2452
298.15 100.00 0.5495 1.2366
298.15 100.00 0.5997 1.2068
298.15 100.00 0.6500 1.1513
298.15 100.00 0.6995 1.0741
298.15 100.00 0.7994 0.8324
298.15 100.00 0.8982 0.4647
298.15 10000.00 0.0996 0.4843
298.15 10000.00 0.1999 0.8222
298.15 10000.00 0.2990 1.0357
298.15 10000.00 0.3500 1.1086
298.15 10000.00 0.3990 1.1567
298.15 10000.00 0.4490 1.1844
298.15 10000.00 0.4993 1.1955
298.15 10000.00 0.5489 1.1837
298.15 10000.00 0.5992 1.1485
298.15 10000.00 0.6495 1.094
298.15 10000.00 0.6990 1.0123
298.15 10000.00 0.7990 0.7600
298.15 10000.00 0.8980 0.4125
313.15 100.00 0.0998 0.5630
313.15 100.00 0.2002 0.9487
313.15 100.00 0.2994 1.1909
313.15 100.00 0.3505 1.2762
313.15 100.00 0.3995 1.3298
313.15 100.00 0.4495 1.3639
313.15 100.00 0.4998 1.3798
313.15 100.00 0.5495 1.3625
313.15 100.00 0.5997 1.3307
313.15 100.00 0.6500 1.27
313.15 100.00 0.6995 1.1667
313.15 100.00 0.7994 0.8837
313.15 100.00 0.8982 0.4793
313.15 10000.00 0.0996 0.5554
313.15 10000.00 0.1999 0.9408
313.15 10000.00 0.2990 1.1838
313.15 10000.00 0.3500 1.2696
313.15 10000.00 0.3990 1.3272
313.15 10000.00 0.4490 1.3606
313.15 10000.00 0.4993 1.3749
313.15 10000.00 0.5489 1.3577
313.15 10000.00 0.5992 1.3248
313.15 10000.00 0.6495 1.2586
313.15 10000.00 0.6990 1.1412
313.15 10000.00 0.7990 0.8755
313.15 10000.00 0.8980 0.4717
328.15 100.00 0.0998 0.6122
328.15 100.00 0.2002 1.0216
328.15 100.00 0.2994 1.2948
328.15 100.00 0.3505 1.3872
328.15 100.00 0.3995 1.4483
328.15 100.00 0.4495 1.4822
328.15 100.00 0.4998 1.4922
328.15 100.00 0.5495 1.474
328.15 100.00 0.5997 1.4285
328.15 100.00 0.6500 1.3527
328.15 100.00 0.6995 1.2493
328.15 100.00 0.7994 0.9365
328.15 100.00 0.8982 0.5020
328.15 10000.00 0.0996 0.6055
328.15 10000.00 0.1999 1.02
328.15 10000.00 0.2990 1.2911
328.15 10000.00 0.3500 1.383
328.15 10000.00 0.3990 1.4457
328.15 10000.00 0.4490 1.4814
328.15 10000.00 0.4993 1.4908
328.15 10000.00 0.5489 1.4725
328.15 10000.00 0.5992 1.4248
328.15 10000.00 0.6495 1.3468
328.15 10000.00 0.6990 1.2409
328.15 10000.00 0.7990 0.9306
328.15 10000.00 0.8980 0.4953

Sources