Mixture of Acetophenone + Water

Excel

Acetophenone

Name
Acetophenone
InChI
InChI=1S/C8H8O/c1-7(9)8-5-3-2-4-6-8/h2-6H,1H3
InChI Key
KWOLFJPFCHCOCG-UHFFFAOYSA-N
Formula
C8H8O
SMILES
CC(=O)c1ccccc1
Mol. Weight (g/mol)
120.15
CAS
98-86-2

Water

Name
Water
InChI
InChI=1S/H2O/h1H2
InChI Key
XLYOFNOQVPJJNP-UHFFFAOYSA-N
Formula
H2O
SMILES
O
Mol. Weight (g/mol)
18.02
CAS
7732-18-5
Cheméo is a service of Céondo GmbH, since 2007, we provide simulation, modelling and software development services for the industry. Do not hesitate to contact us for your projects.

Datasets

  1. Henry's Law constant (molality scale), kPa*kg/mol (6)
  2. Excess molar enthalpy (molar enthalpy (2)

Henry's Law constant (molality scale), kPa*kg/mol of Acetophenone (1) [ref]

Operational condition: Mole fraction = 0 (Liquid)

Temperature, K - Liquid Henry's Law constant (molality scale), kPa*kg/mol of Acetophenone (1) - Liquid
274.15 0.1284
294.65 0.8810
294.65 0.7380
296.15 1.6015
310.15 2.4845
320.15 4.5991
331.15 8.8708

Mass fraction of Water (2) [ref]

Operational condition: Pressure, kPa = 100 (Liquid mixture 2)

Temperature, K - Liquid mixture 2 Mass fraction of Water (2) - Liquid mixture 1
298.20 0.9934
318.20 0.9924
328.20 0.9918
308.20 0.9925

Mass fraction of Water (2) [ref]

Operational condition: Pressure, kPa = 100 (Liquid mixture 2)

Temperature, K - Liquid mixture 2 Mass fraction of Water (2) - Liquid mixture 2
298.20 0.0900
318.20 0.0731
328.20 0.0698
308.20 0.0810

Henry's Law constant (molality scale), kPa*kg/mol of Acetophenone (1) [ref]

Operational condition: Mole fraction = 0 (Liquid)

Temperature, K - Liquid Henry's Law constant (molality scale), kPa*kg/mol of Acetophenone (1) - Liquid
274.15 0.1284
294.65 0.8810
294.65 0.7380
296.15 1.6015
310.15 2.4845
320.15 4.5991
331.15 8.8708

Mass fraction of Water (2) [ref]

Operational condition: Pressure, kPa = 100 (Liquid mixture 2)

Temperature, K - Liquid mixture 2 Mass fraction of Water (2) - Liquid mixture 1
298.20 0.9934
318.20 0.9924
328.20 0.9918
308.20 0.9925

Mass fraction of Water (2) [ref]

Operational condition: Pressure, kPa = 100 (Liquid mixture 2)

Temperature, K - Liquid mixture 2 Mass fraction of Water (2) - Liquid mixture 2
298.20 0.0900
318.20 0.0731
328.20 0.0698
308.20 0.0810

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 Acetophenone (1) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
298.20 0.1002 0.0707
298.20 0.1997 0.1379
298.20 0.3001 0.2059
298.20 0.3991 0.2730
298.20 0.5003 0.3413
298.20 0.5991 0.4078
298.20 0.6986 0.4747
298.20 0.7987 0.5414
298.20 0.8515 0.5757
298.20 0.8967 0.5882
298.20 0.9534 0.3006
313.20 0.1002 0.0906
313.20 0.1997 0.1775
313.20 0.3001 0.2661
313.20 0.3991 0.3538
313.20 0.5003 0.4432
313.20 0.5991 0.5306
313.20 0.6986 0.6189
313.20 0.7987 0.7047
313.20 0.8515 0.7323
313.20 0.8967 0.6698
313.20 0.9534 0.3317
328.20 0.1002 0.1308
328.20 0.1997 0.2478
328.20 0.3001 0.3664
328.20 0.3991 0.4854
328.20 0.5003 0.6065
328.20 0.5991 0.7243
328.20 0.6986 0.8419
328.20 0.7987 0.9599
328.20 0.8515 1.0034
328.20 0.8967 0.7887
328.20 0.9534 0.3874
338.20 0.1002 0.1430
338.20 0.1997 0.2544
338.20 0.3001 0.3976
338.20 0.3991 0.5178
338.20 0.5003 0.6542
338.20 0.5991 0.7878
338.20 0.6986 0.9237
338.20 0.7987 1.0601
338.20 0.8515 1.0241
338.20 0.8967 0.8023
338.20 0.9534 0.3920
348.20 0.1002 0.1671
348.20 0.1997 0.3230
348.20 0.3001 0.4832
348.20 0.3991 0.6392
348.20 0.5003 0.8047
348.20 0.5991 0.9630
348.20 0.6986 1.1246
348.20 0.7987 1.2868
348.20 0.8515 1.1459
348.20 0.8967 0.8551
348.20 0.9534 0.4186

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 Acetophenone (1) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
298.20 0.1002 0.0707
298.20 0.1997 0.1379
298.20 0.3001 0.2059
298.20 0.3991 0.2730
298.20 0.5003 0.3413
298.20 0.5991 0.4078
298.20 0.6986 0.4747
298.20 0.7987 0.5414
298.20 0.8515 0.5757
298.20 0.8967 0.5882
298.20 0.9534 0.3006
313.20 0.1002 0.0906
313.20 0.1997 0.1775
313.20 0.3001 0.2661
313.20 0.3991 0.3538
313.20 0.5003 0.4432
313.20 0.5991 0.5306
313.20 0.6986 0.6189
313.20 0.7987 0.7047
313.20 0.8515 0.7323
313.20 0.8967 0.6698
313.20 0.9534 0.3317
328.20 0.1002 0.1308
328.20 0.1997 0.2478
328.20 0.3001 0.3664
328.20 0.3991 0.4854
328.20 0.5003 0.6065
328.20 0.5991 0.7243
328.20 0.6986 0.8419
328.20 0.7987 0.9599
328.20 0.8515 1.0034
328.20 0.8967 0.7887
328.20 0.9534 0.3874
338.20 0.1002 0.1430
338.20 0.1997 0.2544
338.20 0.3001 0.3976
338.20 0.3991 0.5178
338.20 0.5003 0.6542
338.20 0.5991 0.7878
338.20 0.6986 0.9237
338.20 0.7987 1.0601
338.20 0.8515 1.0241
338.20 0.8967 0.8023
338.20 0.9534 0.3920
348.20 0.1002 0.1671
348.20 0.1997 0.3230
348.20 0.3001 0.4832
348.20 0.3991 0.6392
348.20 0.5003 0.8047
348.20 0.5991 0.9630
348.20 0.6986 1.1246
348.20 0.7987 1.2868
348.20 0.8515 1.1459
348.20 0.8967 0.8551
348.20 0.9534 0.4186

Sources