Mixture of 1-Propanol + Ethyl acetoacetate

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

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
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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 (2) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
298.15 100.00 0.1001 0.8692
298.15 100.00 0.1998 1.3555
298.15 100.00 0.3003 1.6572
298.15 100.00 0.3502 1.7573
298.15 100.00 0.3994 1.8248
298.15 100.00 0.4501 1.8678
298.15 100.00 0.4997 1.881
298.15 100.00 0.5505 1.8641
298.15 100.00 0.5997 1.8208
298.15 100.00 0.6497 1.7447
298.15 100.00 0.7007 1.6319
298.15 100.00 0.7996 1.2862
298.15 100.00 0.9004 0.7322
298.15 10000.00 0.1003 0.8543
298.15 10000.00 0.2001 1.3318
298.15 10000.00 0.3007 1.627
298.15 10000.00 0.3506 1.7233
298.15 10000.00 0.3998 1.7867
298.15 10000.00 0.4505 1.8261
298.15 10000.00 0.5001 1.8367
298.15 10000.00 0.5509 1.82
298.15 10000.00 0.6000 1.7776
298.15 10000.00 0.6501 1.7022
298.15 10000.00 0.7010 1.591
298.15 10000.00 0.7999 1.2565
298.15 10000.00 0.9005 0.7102
313.15 100.00 0.1001 0.9905
313.15 100.00 0.1998 1.5802
313.15 100.00 0.3003 1.9423
313.15 100.00 0.3502 2.0623
313.15 100.00 0.3994 2.1404
313.15 100.00 0.4501 2.1839
313.15 100.00 0.4997 2.1907
313.15 100.00 0.5505 2.1615
313.15 100.00 0.5997 2.0975
313.15 100.00 0.6497 1.9885
313.15 100.00 0.7007 1.8434
313.15 100.00 0.7996 1.4248
313.15 100.00 0.9004 0.7822
313.15 10000.00 0.1003 0.9565
313.15 10000.00 0.2001 1.5247
313.15 10000.00 0.3007 1.8824
313.15 10000.00 0.3506 1.9815
313.15 10000.00 0.3998 2.0572
313.15 10000.00 0.4505 2.0988
313.15 10000.00 0.5001 2.1052
313.15 10000.00 0.5509 2.0852
313.15 10000.00 0.6000 2.0188
313.15 10000.00 0.6501 1.9136
313.15 10000.00 0.7010 1.7617
313.15 10000.00 0.7999 1.3463
313.15 10000.00 0.9005 0.7472
328.15 100.00 0.1001 1.0716
328.15 100.00 0.1998 1.7301
328.15 100.00 0.3003 2.1283
328.15 100.00 0.3502 2.2538
328.15 100.00 0.3994 2.3326
328.15 100.00 0.4501 2.3644
328.15 100.00 0.4997 2.3617
328.15 100.00 0.5505 2.3134
328.15 100.00 0.5997 2.2261
328.15 100.00 0.6497 2.107
328.15 100.00 0.7007 1.9334
328.15 100.00 0.7996 1.4685
328.15 100.00 0.9004 0.8057
328.15 10000.00 0.1003 1.0624
328.15 10000.00 0.2001 1.7028
328.15 10000.00 0.3007 2.1047
328.15 10000.00 0.3506 2.2314
328.15 10000.00 0.3998 2.3111
328.15 10000.00 0.4505 2.3541
328.15 10000.00 0.5001 2.3539
328.15 10000.00 0.5509 2.3082
328.15 10000.00 0.6000 2.2162
328.15 10000.00 0.6501 2.1012
328.15 10000.00 0.7010 1.9279
328.15 10000.00 0.7999 1.4638
328.15 10000.00 0.9005 0.7968

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

Fixed Measured
Temperature, K - Liquid Pressure, kPa - Liquid Mole fraction of Ethyl acetoacetate (2) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
298.15 100.00 0.1001 0.8692
298.15 100.00 0.1998 1.3555
298.15 100.00 0.3003 1.6572
298.15 100.00 0.3502 1.7573
298.15 100.00 0.3994 1.8248
298.15 100.00 0.4501 1.8678
298.15 100.00 0.4997 1.881
298.15 100.00 0.5505 1.8641
298.15 100.00 0.5997 1.8208
298.15 100.00 0.6497 1.7447
298.15 100.00 0.7007 1.6319
298.15 100.00 0.7996 1.2862
298.15 100.00 0.9004 0.7322
298.15 10000.00 0.1003 0.8543
298.15 10000.00 0.2001 1.3318
298.15 10000.00 0.3007 1.627
298.15 10000.00 0.3506 1.7233
298.15 10000.00 0.3998 1.7867
298.15 10000.00 0.4505 1.8261
298.15 10000.00 0.5001 1.8367
298.15 10000.00 0.5509 1.82
298.15 10000.00 0.6000 1.7776
298.15 10000.00 0.6501 1.7022
298.15 10000.00 0.7010 1.591
298.15 10000.00 0.7999 1.2565
298.15 10000.00 0.9005 0.7102
313.15 100.00 0.1001 0.9905
313.15 100.00 0.1998 1.5802
313.15 100.00 0.3003 1.9423
313.15 100.00 0.3502 2.0623
313.15 100.00 0.3994 2.1404
313.15 100.00 0.4501 2.1839
313.15 100.00 0.4997 2.1907
313.15 100.00 0.5505 2.1615
313.15 100.00 0.5997 2.0975
313.15 100.00 0.6497 1.9885
313.15 100.00 0.7007 1.8434
313.15 100.00 0.7996 1.4248
313.15 100.00 0.9004 0.7822
313.15 10000.00 0.1003 0.9565
313.15 10000.00 0.2001 1.5247
313.15 10000.00 0.3007 1.8824
313.15 10000.00 0.3506 1.9815
313.15 10000.00 0.3998 2.0572
313.15 10000.00 0.4505 2.0988
313.15 10000.00 0.5001 2.1052
313.15 10000.00 0.5509 2.0852
313.15 10000.00 0.6000 2.0188
313.15 10000.00 0.6501 1.9136
313.15 10000.00 0.7010 1.7617
313.15 10000.00 0.7999 1.3463
313.15 10000.00 0.9005 0.7472
328.15 100.00 0.1001 1.0716
328.15 100.00 0.1998 1.7301
328.15 100.00 0.3003 2.1283
328.15 100.00 0.3502 2.2538
328.15 100.00 0.3994 2.3326
328.15 100.00 0.4501 2.3644
328.15 100.00 0.4997 2.3617
328.15 100.00 0.5505 2.3134
328.15 100.00 0.5997 2.2261
328.15 100.00 0.6497 2.107
328.15 100.00 0.7007 1.9334
328.15 100.00 0.7996 1.4685
328.15 100.00 0.9004 0.8057
328.15 10000.00 0.1003 1.0624
328.15 10000.00 0.2001 1.7028
328.15 10000.00 0.3007 2.1047
328.15 10000.00 0.3506 2.2314
328.15 10000.00 0.3998 2.3111
328.15 10000.00 0.4505 2.3541
328.15 10000.00 0.5001 2.3539
328.15 10000.00 0.5509 2.3082
328.15 10000.00 0.6000 2.2162
328.15 10000.00 0.6501 2.1012
328.15 10000.00 0.7010 1.9279
328.15 10000.00 0.7999 1.4638
328.15 10000.00 0.9005 0.7968

Sources