Mixture of Ethylbenzene + Water

Datasets

1. Mole fraction (22)
2. P_vap - Vapor or sublimation pressure, kPa (2)

Mole fraction of Ethylbenzene (1) [ref]

Operational condition: Pressure, kPa = 101 (Liquid mixture 1)

Temperature, K - Liquid mixture 1	Mole fraction of Ethylbenzene (1) - Liquid mixture 1
312.95	0.0000
313.15	0.0000
313.25	0.0000
313.85	0.0000
314.05	0.0000

Mole fraction of Ethylbenzene (1) [ref]

Fixed		Measured
Temperature, K - Liquid mixture 1	Pressure, kPa - Liquid mixture 1	Mole fraction of Ethylbenzene (1) - Liquid mixture 1
297.65	501.70	0.0000
298.13	6898.00	0.0000
313.20	503.40	0.0000
343.10	6873.00	0.0000
343.13	500.90	0.0000
373.09	504.50	0.0001
393.21	511.00	0.0001
393.25	6851.00	0.0001

Mass fraction of Water (2) [ref]

Operational condition: Pressure, kPa = 101.32 (Liquid mixture 1)

Temperature, K - Liquid mixture 1	Mass fraction of Water (2) - Liquid mixture 1
298.15	0.0008
298.15	0.9997
308.15	0.0009
308.15	0.9996
318.15	0.0009
318.15	0.9994

Mole fraction of Water (2) [ref]

Operational condition: Pressure, kPa = 100.5 (Liquid mixture 2)

Temperature, K - Liquid mixture 1	Mole fraction of Water (2) - Liquid mixture 2
303.15	1.0000
323.15	0.9999

Mole fraction of Water (2) [ref]

Operational condition: Pressure, kPa = 100.5 (Liquid mixture 2)

Temperature, K - Liquid mixture 1	Mole fraction of Water (2) - Liquid mixture 1
303.15	0.0033
323.15	0.0053

Mole fraction of Ethylbenzene (1) [ref]

Operational condition: Pressure, kPa = 5000 (Liquid mixture 1)

Temperature, K - Liquid mixture 1	Mole fraction of Ethylbenzene (1) - Liquid mixture 1
298.00	0.0000
323.00	0.0000
373.00	0.0001
423.00	0.0002
473.00	0.0008

Mole fraction of Ethylbenzene (1) [ref]

Operational condition: Pressure, kPa = 101 (Liquid mixture 1)

Temperature, K - Liquid mixture 1	Mole fraction of Ethylbenzene (1) - Liquid mixture 1
280.25	0.0000
290.09	0.0000
299.90	0.0000
309.71	0.0000
319.65	0.0000
329.89	0.0000
339.80	0.0000

Mole fraction of Water (2) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid mixture 1)

Temperature, K - Liquid mixture 1	Mole fraction of Water (2) - Liquid mixture 1
313.15	0.0046
318.15	0.0053
323.15	0.0059
328.15	0.0067
333.15	0.0075
338.15	0.0087

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

Operational condition: Molality, mol/kg = 0 (Liquid)

Temperature, K - Liquid	Henry's Law constant (molality scale), kPa*kg/mol of Ethylbenzene (1) - Liquid
274.15	162.03
294.65	472.47
294.65	488.42
296.15	533.03
310.15	342.67
313.15	1288.2
326.15	2315.7
331.15	1832.7

Mass fraction of Ethylbenzene (1) [ref]

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

Temperature, K - Liquid mixture 2	Mass fraction of Ethylbenzene (1) - Liquid mixture 1
308.20	0.0005
318.20	0.0005
298.20	0.0004
328.20	0.0006

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
308.20	0.0021
318.20	0.0006
298.20	0.0025
328.20	0.0004

Mole fraction of Ethylbenzene (1) [ref]

Operational condition: Pressure, kPa = 101 (Liquid mixture 1)

Temperature, K - Liquid mixture 1	Mole fraction of Ethylbenzene (1) - Liquid mixture 1
312.95	0.0000
313.15	0.0000
313.25	0.0000
313.85	0.0000
314.05	0.0000

Mole fraction of Ethylbenzene (1) [ref]

Fixed		Measured
Temperature, K - Liquid mixture 1	Pressure, kPa - Liquid mixture 1	Mole fraction of Ethylbenzene (1) - Liquid mixture 1
297.65	501.70	0.0000
298.13	6898.00	0.0000
313.20	503.40	0.0000
343.10	6873.00	0.0000
343.13	500.90	0.0000
373.09	504.50	0.0001
393.21	511.00	0.0001
393.25	6851.00	0.0001

Mass fraction of Water (2) [ref]

Operational condition: Pressure, kPa = 101.32 (Liquid mixture 1)

Temperature, K - Liquid mixture 1	Mass fraction of Water (2) - Liquid mixture 1
298.15	0.0008
298.15	0.9997
308.15	0.0009
308.15	0.9996
318.15	0.0009
318.15	0.9994

Mole fraction of Water (2) [ref]

Operational condition: Pressure, kPa = 100.5 (Liquid mixture 2)

Temperature, K - Liquid mixture 1	Mole fraction of Water (2) - Liquid mixture 2
303.15	1.0000
323.15	0.9999

Mole fraction of Water (2) [ref]

Operational condition: Pressure, kPa = 100.5 (Liquid mixture 2)

Temperature, K - Liquid mixture 1	Mole fraction of Water (2) - Liquid mixture 1
303.15	0.0033
323.15	0.0053

Mole fraction of Ethylbenzene (1) [ref]

Operational condition: Pressure, kPa = 5000 (Liquid mixture 1)

Temperature, K - Liquid mixture 1	Mole fraction of Ethylbenzene (1) - Liquid mixture 1
298.00	0.0000
323.00	0.0000
373.00	0.0001
423.00	0.0002
473.00	0.0008

Mole fraction of Ethylbenzene (1) [ref]

Operational condition: Pressure, kPa = 101 (Liquid mixture 1)

Temperature, K - Liquid mixture 1	Mole fraction of Ethylbenzene (1) - Liquid mixture 1
280.25	0.0000
290.09	0.0000
299.90	0.0000
309.71	0.0000
319.65	0.0000
329.89	0.0000
339.80	0.0000

Mole fraction of Water (2) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid mixture 1)

Temperature, K - Liquid mixture 1	Mole fraction of Water (2) - Liquid mixture 1
313.15	0.0046
318.15	0.0053
323.15	0.0059
328.15	0.0067
333.15	0.0075
338.15	0.0087

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

Operational condition: Molality, mol/kg = 0 (Liquid)

Temperature, K - Liquid	Henry's Law constant (molality scale), kPa*kg/mol of Ethylbenzene (1) - Liquid
274.15	162.03
294.65	472.47
294.65	488.42
296.15	533.03
310.15	342.67
313.15	1288.2
326.15	2315.7
331.15	1832.7

Mass fraction of Ethylbenzene (1) [ref]

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

Temperature, K - Liquid mixture 2	Mass fraction of Ethylbenzene (1) - Liquid mixture 1
308.20	0.0005
318.20	0.0005
298.20	0.0004
328.20	0.0006

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
308.20	0.0021
318.20	0.0006
298.20	0.0025
328.20	0.0004

Vapor or sublimation pressure, kPa [ref]

Temperature, K - Liquid mixture 1	Vapor or sublimation pressure, kPa - Liquid mixture 1
297.97	4.00
302.65	5.50
307.61	7.20
312.61	9.50
312.65	9.60
317.64	12.70
322.53	16.30
322.56	16.30
327.54	20.90
332.55	26.50
337.56	33.30
342.56	41.40
347.58	50.40
352.61	62.60
357.64	76.20
362.64	92.70
367.66	111.60
372.69	133.60
377.72	158.70
382.73	186.30
387.77	220.10
392.76	259.70
397.84	302.20
402.87	353.60

Vapor or sublimation pressure, kPa [ref]

Temperature, K - Liquid mixture 1	Vapor or sublimation pressure, kPa - Liquid mixture 1
297.97	4.00
302.65	5.50
307.61	7.20
312.61	9.50
312.65	9.60
317.64	12.70
322.53	16.30
322.56	16.30
327.54	20.90
332.55	26.50
337.56	33.30
342.56	41.40
347.58	50.40
352.61	62.60
357.64	76.20
362.64	92.70
367.66	111.60
372.69	133.60
377.72	158.70
382.73	186.30
387.77	220.10
392.76	259.70
397.84	302.20
402.87	353.60

Sources

• Thermodynamics of dissolution for 1-naphtol N-methylcarbamate in pure, mineral and Mediterranean sea water by dynamic saturation method
• Solubility of ethylbenzene and xylene in pure water and aqueous alkanolamine solutions
• Experimental and correlational study of phase equilibria in aqueous mixtures of phosphoric acid with aromatic hydrocarbons at various temperatures
• Liquid-liquid equilibria for the ternary system of water + furfural + solvents at 303.15 and 323.15 K under atmospheric pressure
• Solubility of Alkylbenzenes and a Model for Predicting the Solubility of Liquid Organics in High-Temperature Water
• Solubility of Hexafluorobenzene in Aqueous Salt Solutions from (280 to 340) K
• Liquid-Liquid Equilibria in Ternary Systems of Aromatic Hydrocarbons (Toluene or Ethylbenzene) + Phenols + Water
• Determination of Henry's Law Constants Using Internal Standards with Benchmark Values
• Liquid-Liquid Equilibrium for the Ternary System Water + Ethylbenzene + Acetophenone and Water + Ethylbenzene + 1-Phenylethanol