Mixture of 1-Butanol + Water

Datasets

1. Activity coefficient (8)
2. Mole fraction (102)
3. Molar enthalpy (2)
4. Interfacial tension, N/m (2)
5. n₀ - Refractive index (Na D-line) (2)
6. ρ_l - Mass density, kg/m3 (12)
7. c_sound,fluid - Speed of Sound, m/s (6)
8. γ - Surface tension liquid-gas, N/m (4)
9. T_boil - Boiling temperature at pressure P, K (6)
10. Vapor Liquid Equilibrium at Constant Pressure (2)
11. Vapor Liquid Equilibrium at Constant Temperature
12. Vapor or sublimation pressure, kPa (2)

Activity coefficient of 1-Butanol (1) [ref]

Operational condition: Mole fraction = 0 (Liquid)

Temperature, K - Liquid	Activity coefficient of 1-Butanol (1) - Liquid
273.35	32.6
283.15	40.4
293.15	48.4
323.15	58.7
323.15	59.4

Activity coefficient of 1-Butanol (1) [ref]

Operational condition: Mole fraction = 0 (Liquid)

Temperature, K - Liquid	Activity coefficient of 1-Butanol (1) - Liquid
303.15	53.4
308.15	57.2
313.15	58.9
318.15	60.2
323.15	61.5
328.15	62.8
333.15	63.4

Activity coefficient of 1-Butanol (1) [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1-Butanol (1) - Liquid	Activity coefficient of 1-Butanol (1) - Liquid
372.15	0.0000	56.1

Activity coefficient of 1-Butanol (1) [ref]

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Mole fraction = 0 (Liquid)

Temperature, K - Liquid	Activity coefficient of 1-Butanol (1) - Liquid
303.15	52.0
308.15	57.0
313.15	58.0
318.15	64.0
323.15	69.0
328.15	72.0
333.15	80.0
338.15	78.0

Activity coefficient of 1-Butanol (1) [ref]

Operational condition: Mole fraction = 0 (Liquid)

Temperature, K - Liquid	Activity coefficient of 1-Butanol (1) - Liquid
273.35	32.6
283.15	40.4
293.15	48.4
323.15	58.7
323.15	59.4

Activity coefficient of 1-Butanol (1) [ref]

Operational condition: Mole fraction = 0 (Liquid)

Temperature, K - Liquid	Activity coefficient of 1-Butanol (1) - Liquid
303.15	53.4
308.15	57.2
313.15	58.9
318.15	60.2
323.15	61.5
328.15	62.8
333.15	63.4

Activity coefficient of 1-Butanol (1) [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1-Butanol (1) - Liquid	Activity coefficient of 1-Butanol (1) - Liquid
372.15	0.0000	56.1

Activity coefficient of 1-Butanol (1) [ref]

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Mole fraction = 0 (Liquid)

Temperature, K - Liquid	Activity coefficient of 1-Butanol (1) - Liquid
303.15	52.0
308.15	57.0
313.15	58.0
318.15	64.0
323.15	69.0
328.15	72.0
333.15	80.0
338.15	78.0

Mole fraction of 1-Butanol (1) [ref]

Fixed		Measured
Temperature, K - Liquid mixture 1	Pressure, kPa - Liquid mixture 1	Mole fraction of 1-Butanol (1) - Liquid mixture 1
303.15	101.33	0.0181

Mole fraction of 1-Butanol (1) [ref]

Fixed		Measured
Temperature, K - Liquid mixture 2	Pressure, kPa - Liquid mixture 2	Mole fraction of 1-Butanol (1) - Liquid mixture 2
303.15	101.33	0.4802

Mole fraction of 1-Butanol (1) [ref]

Operational condition: Pressure, kPa = 101 (Liquid mixture 2)

Temperature, K - Liquid mixture 2	Mole fraction of 1-Butanol (1) - Liquid mixture 2
288.15	0.0198
318.15	0.0166

Mole fraction of 1-Butanol (1) [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid mixture 1)

Temperature, K - Liquid mixture 2	Mole fraction of 1-Butanol (1) - Liquid mixture 1
288.15	0.5018
318.15	0.4769

Mass fraction of Water (2) [ref]

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

Temperature, K - Liquid mixture 1	Mass fraction of Water (2) - Liquid mixture 1
298.15	0.2030
298.15	0.9200
308.15	0.2110
308.15	0.9305
318.15	0.2242
318.15	0.9320

Mole fraction of 1-Butanol (1) [ref]

Fixed		Measured
Temperature, K - Liquid mixture 1	Pressure, kPa - Liquid mixture 1	Mole fraction of 1-Butanol (1) - Liquid mixture 1
298.20	101.00	0.0189

Mole fraction of Water (2) [ref]

Fixed		Measured
Temperature, K - Liquid mixture 1	Pressure, kPa - Liquid mixture 1	Mole fraction of Water (2) - Liquid mixture 1
298.20	101.00	0.5105

Mass fraction of Water (2) [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid mixture 1)
• Pressure, kPa = 101 (Liquid mixture 1)

Mass fraction of Water (2) - Liquid mixture 1
0.1657
0.9376

Mole fraction of 1-Butanol (1) [ref]

Fixed		Measured
Temperature, K - Liquid mixture 1	Pressure, kPa - Liquid mixture 1	Mole fraction of 1-Butanol (1) - Liquid mixture 1
303.15	101.00	0.4880

Mole fraction of 1-Butanol (1) [ref]

Fixed		Measured
Temperature, K - Liquid mixture 1	Pressure, kPa - Liquid mixture 1	Mole fraction of 1-Butanol (1) - Liquid mixture 2
303.15	101.00	0.0190

Mole fraction of Water (2) [ref]

Operational condition: Pressure, kPa = 95 (Liquid mixture 1)

Temperature, K - Liquid mixture 1	Mole fraction of Water (2) - Liquid mixture 1
293.20	0.5064
293.20	0.9798
313.20	0.5304
313.20	0.9829

Mole fraction of 1-Butanol (1) [ref]

Fixed		Measured
Temperature, K - Liquid mixture 1	Pressure, kPa - Liquid mixture 1	Mole fraction of 1-Butanol (1) - Liquid mixture 1
318.15	101.30	0.4690

Mole fraction of 1-Butanol (1) [ref]

Fixed		Measured
Temperature, K - Liquid mixture 1	Pressure, kPa - Liquid mixture 1	Mole fraction of 1-Butanol (1) - Liquid mixture 2
318.15	101.30	0.0210

Mole fraction of Water (2) [ref]

Fixed		Measured
Pressure, kPa - Liquid mixture 1	Temperature, K - Liquid mixture 1	Mole fraction of Water (2) - Liquid mixture 1
101.00	308.20	0.9800

Molality, mol/kg of 1-Butanol (1) [ref]

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

Temperature, K - Liquid mixture 1	Molality, mol/kg of 1-Butanol (1) - Liquid mixture 1
283.15	1.1148
288.15	1.0975
293.15	1.0418
298.15	1.0089
303.15	0.9475

Molality, mol/kg of Water (2) [ref]

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

Temperature, K - Liquid mixture 1	Molality, mol/kg of Water (2) - Liquid mixture 2
293.15	11.555
298.15	10.478

Mole fraction of Water (2) [ref]

Fixed		Measured
Temperature, K - Liquid mixture 1	Pressure, kPa - Liquid mixture 1	Mole fraction of Water (2) - Liquid mixture 2
308.15	101.00	0.4780

Mole fraction of Water (2) [ref]

Fixed		Measured
Temperature, K - Liquid mixture 1	Pressure, kPa - Liquid mixture 1	Mole fraction of Water (2) - Liquid mixture 1
308.15	101.00	0.9820

Mole fraction of 1-Butanol (1) [ref]

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

Temperature, K - Liquid mixture 1	Mole fraction of 1-Butanol (1) - Liquid mixture 2
313.15	0.0190
365.85	0.0210

Mole fraction of 1-Butanol (1) [ref]

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

Temperature, K - Liquid mixture 1	Mole fraction of 1-Butanol (1) - Liquid mixture 1
313.15	0.4840
365.85	0.3620

Mole fraction of 1-Butanol (1) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of 1-Butanol (1) - Liquid	Mole fraction of 1-Butanol (1) - Gas
0.3620	0.2460
0.0210	0.2460

Mole fraction of Water (2) [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Water (2) - Liquid	Mole fraction of Water (2) - Gas
283.20	0.0320	0.5880
283.20	0.0520	0.6090
283.20	0.0990	0.7050
283.20	0.1460	0.7660
283.20	0.1810	0.7800
283.20	0.2110	0.7950
283.20	0.2630	0.8190
283.20	0.3220	0.8320
283.20	0.4070	0.8370
283.20	0.6380	0.8430
283.20	0.9420	0.8430
283.20	0.9730	0.8420
283.20	0.9810	0.8590
283.20	0.9870	0.8870
283.20	0.9940	0.9290
283.20	0.9970	0.9630
283.20	0.9990	0.9910
298.20	0.0320	0.4210
298.20	0.0520	0.5060
298.20	0.0990	0.6590
298.20	0.1460	0.7080
298.20	0.1810	0.7330
298.20	0.2110	0.7550
298.20	0.2630	0.7830
298.20	0.3220	0.7990
298.20	0.4070	0.8160
298.20	0.6380	0.8180
298.20	0.9420	0.8200
298.20	0.9730	0.8200
298.20	0.9810	0.8230
298.20	0.9870	0.8510
298.20	0.9940	0.9000
298.20	0.9970	0.9410
298.20	0.9990	0.9780

Mole fraction of Water (2) [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Water (2) - Liquid	Mole fraction of Water (2) - Gas
313.20	0.0520	0.4410
313.20	0.0970	0.5870
313.20	0.1480	0.6720
313.20	0.1480	0.6750
313.20	0.1810	0.7080
313.20	0.2110	0.7380
313.20	0.2110	0.7290
313.20	0.2670	0.7580
313.20	0.3220	0.7760
313.20	0.4070	0.7910
313.20	0.5100	0.7940
313.20	0.9420	0.7920
313.20	0.9730	0.7970
313.20	0.9810	0.7980
313.20	0.9870	0.8060
313.20	0.9940	0.8710
313.20	0.9970	0.9150
313.20	0.9990	0.9640
313.20	0.9990	0.9660
323.20	0.0520	0.4450
323.20	0.0970	0.5890
323.20	0.1480	0.6870
323.20	0.1810	0.7100
323.20	0.1810	0.7170
323.20	0.2110	0.7420
323.20	0.2670	0.7720
323.20	0.3220	0.7760
323.20	0.4070	0.7870
323.20	0.5100	0.7950
323.20	0.6380	0.7910
323.20	0.9730	0.7860
323.20	0.9810	0.7880
323.20	0.9870	0.8060
323.20	0.9940	0.8490
323.20	0.9970	0.9030
323.20	0.9990	0.9560

Mass fraction of Water (2) [ref]

Fixed		Measured
Temperature, K - Liquid mixture 2	Pressure, kPa - Liquid mixture 2	Mass fraction of Water (2) - Liquid mixture 2
298.15	101.30	0.2040

Mass fraction of Water (2) [ref]

Fixed		Measured
Temperature, K - Liquid mixture 2	Pressure, kPa - Liquid mixture 2	Mass fraction of Water (2) - Liquid mixture 1
298.15	101.30	0.9230

Mole fraction of 1-Butanol (1) [ref]

Fixed		Measured
Temperature, K - Liquid mixture 2	Pressure, kPa - Liquid mixture 2	Mole fraction of 1-Butanol (1) - Liquid mixture 1
298.15	100.00	0.0190

Mole fraction of 1-Butanol (1) [ref]

Fixed		Measured
Pressure, kPa - Liquid mixture 2	Temperature, K - Liquid mixture 2	Mole fraction of 1-Butanol (1) - Liquid mixture 2
100.00	298.15	0.4860

Mass fraction of 1-Butanol (1) [ref]

Fixed		Measured
Temperature, K - Liquid mixture 1	Pressure, kPa - Liquid mixture 2	Mass fraction of 1-Butanol (1) - Liquid mixture 2
365.72	101.30	0.7003

Mass fraction of 1-Butanol (1) [ref]

Fixed		Measured
Temperature, K - Liquid mixture 1	Pressure, kPa - Liquid mixture 2	Mass fraction of 1-Butanol (1) - Liquid mixture 1
365.72	101.30	0.0812

Mole fraction of 1-Butanol (1) [ref]

Fixed		Measured
Temperature, K - Liquid mixture 1	Pressure, kPa - Liquid mixture 1	Mole fraction of 1-Butanol (1) - Liquid mixture 2
298.15	100.00	0.4873

Mole fraction of 1-Butanol (1) [ref]

Fixed		Measured
Temperature, K - Liquid mixture 1	Pressure, kPa - Liquid mixture 1	Mole fraction of 1-Butanol (1) - Liquid mixture 1
298.15	100.00	0.0187

Mass fraction of Water (2) [ref]

Operational conditions:

• Temperature, K = 298.2 (Liquid mixture 1)
• Pressure, kPa = 100 (Liquid mixture 1)

Mass fraction of Water (2) - Liquid mixture 1
0.2058
0.9265

Mole fraction of Water (2) [ref]

Fixed		Measured
Temperature, K - Liquid mixture 1	Pressure, kPa - Liquid mixture 2	Mole fraction of Water (2) - Liquid mixture 2
303.15	101.30	0.9830

Mole fraction of Water (2) [ref]

Fixed		Measured
Temperature, K - Liquid mixture 1	Pressure, kPa - Liquid mixture 2	Mole fraction of Water (2) - Liquid mixture 1
303.15	101.30	0.5040

Mole fraction of 1-Butanol (1) [ref]

Fixed		Measured
Temperature, K - Liquid mixture 2	Pressure, kPa - Liquid mixture 2	Mole fraction of 1-Butanol (1) - Liquid mixture 2
328.15	101.00	0.4340

Mole fraction of 1-Butanol (1) [ref]

Fixed		Measured
Temperature, K - Liquid mixture 2	Pressure, kPa - Liquid mixture 2	Mole fraction of 1-Butanol (1) - Liquid mixture 1
328.15	101.00	0.0200

Mole fraction of 1-Butanol (1) [ref]

Temperature, K - Liquid mixture 1	Mole fraction of 1-Butanol (1) - Liquid mixture 2
366.23	0.0198

Mole fraction of 1-Butanol (1) [ref]

Temperature, K - Liquid mixture 1	Mole fraction of 1-Butanol (1) - Liquid mixture 1
366.23	0.3666

Mole fraction of 1-Butanol (1) [ref]

Temperature, K - Liquid mixture 1	Mole fraction of 1-Butanol (1) - Gas
366.23	0.2495

Mass fraction of 1-Butanol (1) [ref]

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

Temperature, K - Liquid mixture 2	Mass fraction of 1-Butanol (1) - Liquid mixture 1
293.15	0.8144
323.15	0.7699
308.15	0.7879

Mass fraction of 1-Butanol (1) [ref]

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

Temperature, K - Liquid mixture 2	Mass fraction of 1-Butanol (1) - Liquid mixture 2
293.15	0.0689
323.15	0.0618
308.15	0.0623

Mass fraction of Water (2) [ref]

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

Temperature, K - Liquid mixture 1	Mass fraction of Water (2) - Liquid mixture 2
288.20	0.9223
303.20	0.9294
318.20	0.9334

Mass fraction of Water (2) [ref]

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

Temperature, K - Liquid mixture 1	Mass fraction of Water (2) - Liquid mixture 1
288.20	0.2033
303.20	0.2067
318.20	0.2182

Mass fraction of 1-Butanol (1) [ref]

Fixed		Measured
Temperature, K - Liquid mixture 1	Pressure, kPa - Liquid mixture 1	Mass fraction of 1-Butanol (1) - Liquid mixture 1
323.15	97.00	0.7772

Mole fraction of Water (2) [ref]

Fixed		Measured
Temperature, K - Liquid mixture 1	Pressure, kPa - Liquid mixture 1	Mole fraction of Water (2) - Liquid mixture 1
313.15	101.00	0.5160

Mole fraction of Water (2) [ref]

Fixed		Measured
Temperature, K - Liquid mixture 1	Pressure, kPa - Liquid mixture 1	Mole fraction of Water (2) - Liquid mixture 2
313.15	101.00	0.9810

Mole fraction of Water (2) [ref]

Operational condition: Pressure, kPa = 101 (Liquid mixture 2)

Temperature, K - Liquid mixture 2	Mole fraction of Water (2) - Liquid mixture 1
303.20	0.5110
323.20	0.5430
343.20	0.5810

Mole fraction of Water (2) [ref]

Operational condition: Pressure, kPa = 101 (Liquid mixture 2)

Temperature, K - Liquid mixture 2	Mole fraction of Water (2) - Liquid mixture 2
303.20	0.9780
323.20	0.9820
343.20	0.9840

Mole fraction of 1-Butanol (1) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of 1-Butanol (1) - Liquid	Mole fraction of 1-Butanol (1) - Gas
0.0000	0.0000
0.0050	0.1200
0.0060	0.1480
0.0090	0.1910
0.5580	0.2480
0.5920	0.2530
0.6300	0.2710
0.6870	0.3040
0.7350	0.3420
0.7600	0.3660
0.8030	0.4160
0.8450	0.4800
0.8810	0.5500
0.9180	0.6450
0.9550	0.7730
0.9890	0.9330
1.0000	1.0000

Mole fraction of 1-Butanol (1) [ref]

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

Temperature, K - Liquid mixture 1	Mole fraction of 1-Butanol (1) - Liquid mixture 1
323.15	0.4574
333.15	0.4387
343.15	0.4189
353.15	0.3965
362.45	0.3673

Mole fraction of 1-Butanol (1) [ref]

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

Temperature, K - Liquid mixture 2	Mole fraction of 1-Butanol (1) - Liquid mixture 2
323.15	0.0167
333.15	0.0162
343.15	0.0172
353.15	0.0181
362.45	0.0187

Mole fraction of 1-Butanol (1) [ref]

Fixed		Measured
Temperature, K - Liquid mixture 1	Pressure, kPa - Liquid mixture 1	Mole fraction of 1-Butanol (1) - Liquid mixture 1
303.15	101.33	0.0181

Mole fraction of 1-Butanol (1) [ref]

Fixed		Measured
Temperature, K - Liquid mixture 2	Pressure, kPa - Liquid mixture 2	Mole fraction of 1-Butanol (1) - Liquid mixture 2
303.15	101.33	0.4802

Mole fraction of 1-Butanol (1) [ref]

Operational condition: Pressure, kPa = 101 (Liquid mixture 2)

Temperature, K - Liquid mixture 2	Mole fraction of 1-Butanol (1) - Liquid mixture 2
288.15	0.0198
318.15	0.0166

Mole fraction of 1-Butanol (1) [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid mixture 1)

Temperature, K - Liquid mixture 2	Mole fraction of 1-Butanol (1) - Liquid mixture 1
288.15	0.5018
318.15	0.4769

Mass fraction of Water (2) [ref]

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

Temperature, K - Liquid mixture 1	Mass fraction of Water (2) - Liquid mixture 1
298.15	0.2030
298.15	0.9200
308.15	0.2110
308.15	0.9305
318.15	0.2242
318.15	0.9320

Mole fraction of 1-Butanol (1) [ref]

Fixed		Measured
Temperature, K - Liquid mixture 1	Pressure, kPa - Liquid mixture 1	Mole fraction of 1-Butanol (1) - Liquid mixture 1
298.20	101.00	0.0189

Mole fraction of Water (2) [ref]

Fixed		Measured
Temperature, K - Liquid mixture 1	Pressure, kPa - Liquid mixture 1	Mole fraction of Water (2) - Liquid mixture 1
298.20	101.00	0.5105

Mass fraction of Water (2) [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid mixture 1)
• Pressure, kPa = 101 (Liquid mixture 1)

Mass fraction of Water (2) - Liquid mixture 1
0.1657
0.9376

Mole fraction of 1-Butanol (1) [ref]

Fixed		Measured
Temperature, K - Liquid mixture 1	Pressure, kPa - Liquid mixture 1	Mole fraction of 1-Butanol (1) - Liquid mixture 1
303.15	101.00	0.4880

Mole fraction of 1-Butanol (1) [ref]

Fixed		Measured
Temperature, K - Liquid mixture 1	Pressure, kPa - Liquid mixture 1	Mole fraction of 1-Butanol (1) - Liquid mixture 2
303.15	101.00	0.0190

Mole fraction of Water (2) [ref]

Operational condition: Pressure, kPa = 95 (Liquid mixture 1)

Temperature, K - Liquid mixture 1	Mole fraction of Water (2) - Liquid mixture 1
293.20	0.5064
293.20	0.9798
313.20	0.5304
313.20	0.9829

Mole fraction of 1-Butanol (1) [ref]

Fixed		Measured
Temperature, K - Liquid mixture 1	Pressure, kPa - Liquid mixture 1	Mole fraction of 1-Butanol (1) - Liquid mixture 1
318.15	101.30	0.4690

Mole fraction of 1-Butanol (1) [ref]

Fixed		Measured
Temperature, K - Liquid mixture 1	Pressure, kPa - Liquid mixture 1	Mole fraction of 1-Butanol (1) - Liquid mixture 2
318.15	101.30	0.0210

Mole fraction of Water (2) [ref]

Fixed		Measured
Pressure, kPa - Liquid mixture 1	Temperature, K - Liquid mixture 1	Mole fraction of Water (2) - Liquid mixture 1
101.00	308.20	0.9800

Molality, mol/kg of 1-Butanol (1) [ref]

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

Temperature, K - Liquid mixture 1	Molality, mol/kg of 1-Butanol (1) - Liquid mixture 1
283.15	1.1148
288.15	1.0975
293.15	1.0418
298.15	1.0089
303.15	0.9475

Molality, mol/kg of Water (2) [ref]

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

Temperature, K - Liquid mixture 1	Molality, mol/kg of Water (2) - Liquid mixture 2
293.15	11.555
298.15	10.478

Mole fraction of Water (2) [ref]

Fixed		Measured
Temperature, K - Liquid mixture 1	Pressure, kPa - Liquid mixture 1	Mole fraction of Water (2) - Liquid mixture 2
308.15	101.00	0.4780

Mole fraction of Water (2) [ref]

Fixed		Measured
Temperature, K - Liquid mixture 1	Pressure, kPa - Liquid mixture 1	Mole fraction of Water (2) - Liquid mixture 1
308.15	101.00	0.9820

Mole fraction of 1-Butanol (1) [ref]

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

Temperature, K - Liquid mixture 1	Mole fraction of 1-Butanol (1) - Liquid mixture 2
313.15	0.0190
365.85	0.0210

Mole fraction of 1-Butanol (1) [ref]

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

Temperature, K - Liquid mixture 1	Mole fraction of 1-Butanol (1) - Liquid mixture 1
313.15	0.4840
365.85	0.3620

Mole fraction of 1-Butanol (1) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of 1-Butanol (1) - Liquid	Mole fraction of 1-Butanol (1) - Gas
0.3620	0.2460
0.0210	0.2460

Mole fraction of Water (2) [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Water (2) - Liquid	Mole fraction of Water (2) - Gas
283.20	0.0320	0.5880
283.20	0.0520	0.6090
283.20	0.0990	0.7050
283.20	0.1460	0.7660
283.20	0.1810	0.7800
283.20	0.2110	0.7950
283.20	0.2630	0.8190
283.20	0.3220	0.8320
283.20	0.4070	0.8370
283.20	0.6380	0.8430
283.20	0.9420	0.8430
283.20	0.9730	0.8420
283.20	0.9810	0.8590
283.20	0.9870	0.8870
283.20	0.9940	0.9290
283.20	0.9970	0.9630
283.20	0.9990	0.9910
298.20	0.0320	0.4210
298.20	0.0520	0.5060
298.20	0.0990	0.6590
298.20	0.1460	0.7080
298.20	0.1810	0.7330
298.20	0.2110	0.7550
298.20	0.2630	0.7830
298.20	0.3220	0.7990
298.20	0.4070	0.8160
298.20	0.6380	0.8180
298.20	0.9420	0.8200
298.20	0.9730	0.8200
298.20	0.9810	0.8230
298.20	0.9870	0.8510
298.20	0.9940	0.9000
298.20	0.9970	0.9410
298.20	0.9990	0.9780

Mole fraction of Water (2) [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Water (2) - Liquid	Mole fraction of Water (2) - Gas
313.20	0.0520	0.4410
313.20	0.0970	0.5870
313.20	0.1480	0.6720
313.20	0.1480	0.6750
313.20	0.1810	0.7080
313.20	0.2110	0.7380
313.20	0.2110	0.7290
313.20	0.2670	0.7580
313.20	0.3220	0.7760
313.20	0.4070	0.7910
313.20	0.5100	0.7940
313.20	0.9420	0.7920
313.20	0.9730	0.7970
313.20	0.9810	0.7980
313.20	0.9870	0.8060
313.20	0.9940	0.8710
313.20	0.9970	0.9150
313.20	0.9990	0.9640
313.20	0.9990	0.9660
323.20	0.0520	0.4450
323.20	0.0970	0.5890
323.20	0.1480	0.6870
323.20	0.1810	0.7100
323.20	0.1810	0.7170
323.20	0.2110	0.7420
323.20	0.2670	0.7720
323.20	0.3220	0.7760
323.20	0.4070	0.7870
323.20	0.5100	0.7950
323.20	0.6380	0.7910
323.20	0.9730	0.7860
323.20	0.9810	0.7880
323.20	0.9870	0.8060
323.20	0.9940	0.8490
323.20	0.9970	0.9030
323.20	0.9990	0.9560

Mass fraction of Water (2) [ref]

Fixed		Measured
Temperature, K - Liquid mixture 2	Pressure, kPa - Liquid mixture 2	Mass fraction of Water (2) - Liquid mixture 2
298.15	101.30	0.2040

Mass fraction of Water (2) [ref]

Fixed		Measured
Temperature, K - Liquid mixture 2	Pressure, kPa - Liquid mixture 2	Mass fraction of Water (2) - Liquid mixture 1
298.15	101.30	0.9230

Mole fraction of 1-Butanol (1) [ref]

Fixed		Measured
Temperature, K - Liquid mixture 2	Pressure, kPa - Liquid mixture 2	Mole fraction of 1-Butanol (1) - Liquid mixture 1
298.15	100.00	0.0190

Mole fraction of 1-Butanol (1) [ref]

Fixed		Measured
Pressure, kPa - Liquid mixture 2	Temperature, K - Liquid mixture 2	Mole fraction of 1-Butanol (1) - Liquid mixture 2
100.00	298.15	0.4860

Mass fraction of 1-Butanol (1) [ref]

Fixed		Measured
Temperature, K - Liquid mixture 1	Pressure, kPa - Liquid mixture 2	Mass fraction of 1-Butanol (1) - Liquid mixture 2
365.72	101.30	0.7003

Mass fraction of 1-Butanol (1) [ref]

Fixed		Measured
Temperature, K - Liquid mixture 1	Pressure, kPa - Liquid mixture 2	Mass fraction of 1-Butanol (1) - Liquid mixture 1
365.72	101.30	0.0812

Mole fraction of 1-Butanol (1) [ref]

Fixed		Measured
Temperature, K - Liquid mixture 1	Pressure, kPa - Liquid mixture 1	Mole fraction of 1-Butanol (1) - Liquid mixture 2
298.15	100.00	0.4873

Mole fraction of 1-Butanol (1) [ref]

Fixed		Measured
Temperature, K - Liquid mixture 1	Pressure, kPa - Liquid mixture 1	Mole fraction of 1-Butanol (1) - Liquid mixture 1
298.15	100.00	0.0187

Mass fraction of Water (2) [ref]

Operational conditions:

• Temperature, K = 298.2 (Liquid mixture 1)
• Pressure, kPa = 100 (Liquid mixture 1)

Mass fraction of Water (2) - Liquid mixture 1
0.2058
0.9265

Mole fraction of Water (2) [ref]

Fixed		Measured
Temperature, K - Liquid mixture 1	Pressure, kPa - Liquid mixture 2	Mole fraction of Water (2) - Liquid mixture 2
303.15	101.30	0.9830

Mole fraction of Water (2) [ref]

Fixed		Measured
Temperature, K - Liquid mixture 1	Pressure, kPa - Liquid mixture 2	Mole fraction of Water (2) - Liquid mixture 1
303.15	101.30	0.5040

Mole fraction of 1-Butanol (1) [ref]

Fixed		Measured
Temperature, K - Liquid mixture 2	Pressure, kPa - Liquid mixture 2	Mole fraction of 1-Butanol (1) - Liquid mixture 2
328.15	101.00	0.4340

Mole fraction of 1-Butanol (1) [ref]

Fixed		Measured
Temperature, K - Liquid mixture 2	Pressure, kPa - Liquid mixture 2	Mole fraction of 1-Butanol (1) - Liquid mixture 1
328.15	101.00	0.0200

Mole fraction of 1-Butanol (1) [ref]

Temperature, K - Liquid mixture 1	Mole fraction of 1-Butanol (1) - Liquid mixture 2
366.23	0.0198

Mole fraction of 1-Butanol (1) [ref]

Temperature, K - Liquid mixture 1	Mole fraction of 1-Butanol (1) - Liquid mixture 1
366.23	0.3666

Mole fraction of 1-Butanol (1) [ref]

Temperature, K - Liquid mixture 1	Mole fraction of 1-Butanol (1) - Gas
366.23	0.2495

Mass fraction of 1-Butanol (1) [ref]

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

Temperature, K - Liquid mixture 2	Mass fraction of 1-Butanol (1) - Liquid mixture 1
293.15	0.8144
323.15	0.7699
308.15	0.7879

Mass fraction of 1-Butanol (1) [ref]

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

Temperature, K - Liquid mixture 2	Mass fraction of 1-Butanol (1) - Liquid mixture 2
293.15	0.0689
323.15	0.0618
308.15	0.0623

Mass fraction of Water (2) [ref]

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

Temperature, K - Liquid mixture 1	Mass fraction of Water (2) - Liquid mixture 2
288.20	0.9223
303.20	0.9294
318.20	0.9334

Mass fraction of Water (2) [ref]

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

Temperature, K - Liquid mixture 1	Mass fraction of Water (2) - Liquid mixture 1
288.20	0.2033
303.20	0.2067
318.20	0.2182

Mass fraction of 1-Butanol (1) [ref]

Fixed		Measured
Temperature, K - Liquid mixture 1	Pressure, kPa - Liquid mixture 1	Mass fraction of 1-Butanol (1) - Liquid mixture 1
323.15	97.00	0.7772

Mole fraction of Water (2) [ref]

Fixed		Measured
Temperature, K - Liquid mixture 1	Pressure, kPa - Liquid mixture 1	Mole fraction of Water (2) - Liquid mixture 1
313.15	101.00	0.5160

Mole fraction of Water (2) [ref]

Fixed		Measured
Temperature, K - Liquid mixture 1	Pressure, kPa - Liquid mixture 1	Mole fraction of Water (2) - Liquid mixture 2
313.15	101.00	0.9810

Mole fraction of Water (2) [ref]

Operational condition: Pressure, kPa = 101 (Liquid mixture 2)

Temperature, K - Liquid mixture 2	Mole fraction of Water (2) - Liquid mixture 1
303.20	0.5110
323.20	0.5430
343.20	0.5810

Mole fraction of Water (2) [ref]

Operational condition: Pressure, kPa = 101 (Liquid mixture 2)

Temperature, K - Liquid mixture 2	Mole fraction of Water (2) - Liquid mixture 2
303.20	0.9780
323.20	0.9820
343.20	0.9840

Mole fraction of 1-Butanol (1) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of 1-Butanol (1) - Liquid	Mole fraction of 1-Butanol (1) - Gas
0.0000	0.0000
0.0050	0.1200
0.0060	0.1480
0.0090	0.1910
0.5580	0.2480
0.5920	0.2530
0.6300	0.2710
0.6870	0.3040
0.7350	0.3420
0.7600	0.3660
0.8030	0.4160
0.8450	0.4800
0.8810	0.5500
0.9180	0.6450
0.9550	0.7730
0.9890	0.9330
1.0000	1.0000

Mole fraction of 1-Butanol (1) [ref]

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

Temperature, K - Liquid mixture 1	Mole fraction of 1-Butanol (1) - Liquid mixture 1
323.15	0.4574
333.15	0.4387
343.15	0.4189
353.15	0.3965
362.45	0.3673

Mole fraction of 1-Butanol (1) [ref]

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

Temperature, K - Liquid mixture 2	Mole fraction of 1-Butanol (1) - Liquid mixture 2
323.15	0.0167
333.15	0.0162
343.15	0.0172
353.15	0.0181
362.45	0.0187

Molar enthalpy of dilution, kJ/mol [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 101.325 (Liquid)

Fixed		Measured
Initial molality of solute, mol/kg - Liquid	Final molality of solute, mol/kg - Liquid	Molar enthalpy of dilution, kJ/mol - Liquid
0.1861	0.0921	-0.1073
0.3033	0.1460	-0.1713
0.3805	0.1829	-0.2131
0.5006	0.2403	-0.2685
0.5066	0.2431	-0.2870
0.5130	0.2462	-0.3001
0.5649	0.2710	-0.3242
0.5661	0.2788	-0.3372
0.6772	0.3243	-0.4404
0.6796	0.3254	-0.4264
0.7521	0.3601	-0.5337
0.7526	0.3603	-0.5081
0.8401	0.4016	-0.5728
0.8837	0.4225	-0.6154
0.9408	0.4492	-0.6912
1.0923	0.5208	-0.8484

Molar enthalpy of dilution, kJ/mol [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 101.325 (Liquid)

Fixed		Measured
Initial molality of solute, mol/kg - Liquid	Final molality of solute, mol/kg - Liquid	Molar enthalpy of dilution, kJ/mol - Liquid
0.1861	0.0921	-0.1073
0.3033	0.1460	-0.1713
0.3805	0.1829	-0.2131
0.5006	0.2403	-0.2685
0.5066	0.2431	-0.2870
0.5130	0.2462	-0.3001
0.5649	0.2710	-0.3242
0.5661	0.2788	-0.3372
0.6772	0.3243	-0.4404
0.6796	0.3254	-0.4264
0.7521	0.3601	-0.5337
0.7526	0.3603	-0.5081
0.8401	0.4016	-0.5728
0.8837	0.4225	-0.6154
0.9408	0.4492	-0.6912
1.0923	0.5208	-0.8484

Interfacial tension, N/m [ref]

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

Temperature, K - Liquid mixture 1	Interfacial tension, N/m - Liquid mixture 1
278.15	0.0015
288.15	0.0016
298.15	0.0017
308.15	0.0017
318.15	0.0016
328.15	0.0015
338.15	0.0014
348.15	0.0012
358.15	0.0010

Interfacial tension, N/m [ref]

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

Temperature, K - Liquid mixture 1	Interfacial tension, N/m - Liquid mixture 1
278.15	0.0015
288.15	0.0016
298.15	0.0017
308.15	0.0017
318.15	0.0016
328.15	0.0015
338.15	0.0014
348.15	0.0012
358.15	0.0010

Refractive index (Na D-line) [ref]

Operational conditions:

• Temperature, K = 298.2 (Liquid)
• Pressure, kPa = 100 (Liquid)

Mass fraction of Water (2) - Liquid	Refractive index (Na D-line) - Liquid
0.2058	1.3885
0.9265	1.3402

Refractive index (Na D-line) [ref]

Operational conditions:

• Temperature, K = 298.2 (Liquid)
• Pressure, kPa = 100 (Liquid)

Mass fraction of Water (2) - Liquid	Refractive index (Na D-line) - Liquid
0.2058	1.3885
0.9265	1.3402

Mass density, kg/m3 [ref]

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

Temperature, K - Liquid mixture 1	Mass density, kg/m3 - Liquid mixture 1
278.15	988.19
288.15	987.76
298.15	985.96
308.15	983.25
318.15	979.33
328.15	974.57
338.15	968.9
348.15	962.62
358.15	954.7

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid mixture 2)

Temperature, K - Liquid mixture 2	Mass density, kg/m3 - Liquid mixture 2
278.15	858.05
288.15	851.15
298.15	844.37
308.15	837.78
318.15	831.37
328.15	825.62
338.15	820.53
348.15	815.68
358.15	809.77

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 84.5 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Molality, mol/kg of 1-Butanol (1) - Liquid	Mass density, kg/m3 - Liquid
288.15	0.0134	998.939
288.15	0.0270	998.774
288.15	0.0405	998.614
288.15	0.0543	998.455
288.15	0.0677	998.296
288.15	0.0813	998.137
288.15	0.1063	997.846
288.15	0.1358	997.518
293.15	0.0134	998.039
293.15	0.0270	997.873
293.15	0.0405	997.712
293.15	0.0543	997.552
293.15	0.0677	997.389
293.15	0.0813	997.231
293.15	0.1063	996.934
293.15	0.1358	996.602
298.15	0.0134	996.876
298.15	0.0270	996.708
298.15	0.0405	996.547
298.15	0.0543	996.384
298.15	0.0677	996.218
298.15	0.0813	996.058
298.15	0.1063	995.757
298.15	0.1358	995.417
303.15	0.0134	995.476
303.15	0.0270	995.306
303.15	0.0405	995.143
303.15	0.0543	994.976
303.15	0.0677	994.809
303.15	0.0813	994.647
303.15	0.1063	994.341
303.15	0.1358	993.998
308.15	0.0134	993.859
308.15	0.0270	993.686
308.15	0.0405	993.508
308.15	0.0543	993.352
308.15	0.0677	993.182
308.15	0.0813	992.992
308.15	0.1063	992.707
308.15	0.1358	992.357

Mass density, kg/m3 [ref]

Operational conditions:

• Temperature, K = 298.2 (Liquid)
• Pressure, kPa = 100 (Liquid)

Mass fraction of Water (2) - Liquid	Mass density, kg/m3 - Liquid
0.2058	844.74
0.9265	986.16

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1-Butanol (1) - Liquid	Mass density, kg/m3 - Liquid
283.15	0.0000	999.7
283.15	0.0018	998.53
283.15	0.0019	998.45
283.15	0.0041	997.14
283.15	0.0059	996.09
283.15	0.0076	995.23
283.15	0.0098	993.91
283.15	0.0118	992.99
283.15	0.0127	992.46
283.15	0.0141	991.8
283.15	0.0151	991.47
283.15	0.0167	990.74
283.15	0.5009	854.08
283.15	0.5472	849.08
283.15	0.5710	846.7
283.15	0.5930	844.63
283.15	0.6495	839.7
283.15	0.6908	836.38
283.15	0.7249	833.87
283.15	0.7543	831.84
283.15	0.7929	829.22
283.15	0.8478	825.73
283.15	0.9322	820.77
283.15	0.9488	819.84
283.15	0.9959	817.41
283.15	1.0000	817.18
288.15	0.0000	999.1
288.15	0.0018	997.9
288.15	0.0019	997.84
288.15	0.0041	996.5
288.15	0.0059	995.42
288.15	0.0076	994.55
288.15	0.0098	993.17
288.15	0.0118	992.22
288.15	0.0127	991.65
288.15	0.0141	990.95
288.15	0.0151	990.63
288.15	0.0167	989.83
288.15	0.5009	850.29
288.15	0.5472	845.25
288.15	0.5710	842.85
288.15	0.5930	840.77
288.15	0.6495	835.82
288.15	0.6908	832.49
288.15	0.7249	829.97
288.15	0.7543	827.94
288.15	0.7929	825.33
288.15	0.8478	821.84
288.15	0.9322	816.94
288.15	0.9488	816.03
288.15	0.9959	813.63
288.15	1.0000	813.4
293.15	0.0000	998.2
293.15	0.0018	996.98
293.15	0.0019	996.93
293.15	0.0041	995.57
293.15	0.0059	994.46
293.15	0.0076	993.56
293.15	0.0098	992.14
293.15	0.0118	991.14
293.15	0.0127	990.55
293.15	0.0141	989.81
293.15	0.0151	989.47
293.15	0.0167	988.62
293.15	0.5009	846.45
293.15	0.5472	841.38
293.15	0.5710	838.96
293.15	0.5930	836.87
293.15	0.6495	831.9
293.15	0.6908	828.56
293.15	0.7249	826.04
293.15	0.7543	824.01
293.15	0.7929	821.4
293.15	0.8478	817.94
293.15	0.9322	813.08
293.15	0.9488	812.19
293.15	0.9959	809.82
293.15	1.0000	809.6
298.15	0.0000	997.04
298.15	0.0018	995.81
298.15	0.0019	995.75
298.15	0.0041	994.37
298.15	0.0059	993.24
298.15	0.0076	992.31
298.15	0.0098	990.84
298.15	0.0118	989.8
298.15	0.0127	989.19
298.15	0.0141	988.4
298.15	0.0151	988.05
298.15	0.0167	987.15
298.15	0.5009	842.56
298.15	0.5472	837.46
298.15	0.5710	835.03
298.15	0.5930	832.93
298.15	0.6495	827.94
298.15	0.6908	824.6
298.15	0.7249	822.07
298.15	0.7543	820.05
298.15	0.7929	817.45
298.15	0.8478	814.0
298.15	0.9322	809.2
298.15	0.9488	808.33
298.15	0.9959	806.0
298.15	1.0000	805.78
303.15	0.0000	995.65
303.15	0.0018	994.41
303.15	0.0019	994.34
303.15	0.0041	992.93
303.15	0.0059	991.77
303.15	0.0076	990.82
303.15	0.0098	989.29
303.15	0.0118	988.21
303.15	0.0127	987.58
303.15	0.0141	986.76
303.15	0.0151	986.38
303.15	0.0167	985.44
303.15	0.5009	838.64
303.15	0.5472	833.5
303.15	0.5710	831.05
303.15	0.5930	828.95
303.15	0.6495	823.94
303.15	0.6908	820.59
303.15	0.7249	818.07
303.15	0.7543	816.04
303.15	0.7929	813.46
303.15	0.8478	810.03
303.15	0.9322	805.28
303.15	0.9488	804.44
303.15	0.9959	802.14
303.15	1.0000	801.94

Mass density, kg/m3 [ref]

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Temperature, K = 298.15 (Liquid)

Molality, mol/kg of Water (2) - Liquid	Mass density, kg/m3 - Liquid
0.0000	806.024
0.1588	806.701
0.2034	806.906
0.2526	807.034
0.3019	807.215
0.3998	807.558
0.5007	807.906
0.6011	808.262
0.7050	808.615
0.8032	808.946
0.9017	809.283

Mass density, kg/m3 [ref]

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

Temperature, K - Liquid mixture 1	Mass density, kg/m3 - Liquid mixture 1
278.15	988.19
288.15	987.76
298.15	985.96
308.15	983.25
318.15	979.33
328.15	974.57
338.15	968.9
348.15	962.62
358.15	954.7

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid mixture 2)

Temperature, K - Liquid mixture 2	Mass density, kg/m3 - Liquid mixture 2
278.15	858.05
288.15	851.15
298.15	844.37
308.15	837.78
318.15	831.37
328.15	825.62
338.15	820.53
348.15	815.68
358.15	809.77

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 84.5 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Molality, mol/kg of 1-Butanol (1) - Liquid	Mass density, kg/m3 - Liquid
288.15	0.0134	998.939
288.15	0.0270	998.774
288.15	0.0405	998.614
288.15	0.0543	998.455
288.15	0.0677	998.296
288.15	0.0813	998.137
288.15	0.1063	997.846
288.15	0.1358	997.518
293.15	0.0134	998.039
293.15	0.0270	997.873
293.15	0.0405	997.712
293.15	0.0543	997.552
293.15	0.0677	997.389
293.15	0.0813	997.231
293.15	0.1063	996.934
293.15	0.1358	996.602
298.15	0.0134	996.876
298.15	0.0270	996.708
298.15	0.0405	996.547
298.15	0.0543	996.384
298.15	0.0677	996.218
298.15	0.0813	996.058
298.15	0.1063	995.757
298.15	0.1358	995.417
303.15	0.0134	995.476
303.15	0.0270	995.306
303.15	0.0405	995.143
303.15	0.0543	994.976
303.15	0.0677	994.809
303.15	0.0813	994.647
303.15	0.1063	994.341
303.15	0.1358	993.998
308.15	0.0134	993.859
308.15	0.0270	993.686
308.15	0.0405	993.508
308.15	0.0543	993.352
308.15	0.0677	993.182
308.15	0.0813	992.992
308.15	0.1063	992.707
308.15	0.1358	992.357

Mass density, kg/m3 [ref]

Operational conditions:

• Temperature, K = 298.2 (Liquid)
• Pressure, kPa = 100 (Liquid)

Mass fraction of Water (2) - Liquid	Mass density, kg/m3 - Liquid
0.2058	844.74
0.9265	986.16

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1-Butanol (1) - Liquid	Mass density, kg/m3 - Liquid
283.15	0.0000	999.7
283.15	0.0018	998.53
283.15	0.0019	998.45
283.15	0.0041	997.14
283.15	0.0059	996.09
283.15	0.0076	995.23
283.15	0.0098	993.91
283.15	0.0118	992.99
283.15	0.0127	992.46
283.15	0.0141	991.8
283.15	0.0151	991.47
283.15	0.0167	990.74
283.15	0.5009	854.08
283.15	0.5472	849.08
283.15	0.5710	846.7
283.15	0.5930	844.63
283.15	0.6495	839.7
283.15	0.6908	836.38
283.15	0.7249	833.87
283.15	0.7543	831.84
283.15	0.7929	829.22
283.15	0.8478	825.73
283.15	0.9322	820.77
283.15	0.9488	819.84
283.15	0.9959	817.41
283.15	1.0000	817.18
288.15	0.0000	999.1
288.15	0.0018	997.9
288.15	0.0019	997.84
288.15	0.0041	996.5
288.15	0.0059	995.42
288.15	0.0076	994.55
288.15	0.0098	993.17
288.15	0.0118	992.22
288.15	0.0127	991.65
288.15	0.0141	990.95
288.15	0.0151	990.63
288.15	0.0167	989.83
288.15	0.5009	850.29
288.15	0.5472	845.25
288.15	0.5710	842.85
288.15	0.5930	840.77
288.15	0.6495	835.82
288.15	0.6908	832.49
288.15	0.7249	829.97
288.15	0.7543	827.94
288.15	0.7929	825.33
288.15	0.8478	821.84
288.15	0.9322	816.94
288.15	0.9488	816.03
288.15	0.9959	813.63
288.15	1.0000	813.4
293.15	0.0000	998.2
293.15	0.0018	996.98
293.15	0.0019	996.93
293.15	0.0041	995.57
293.15	0.0059	994.46
293.15	0.0076	993.56
293.15	0.0098	992.14
293.15	0.0118	991.14
293.15	0.0127	990.55
293.15	0.0141	989.81
293.15	0.0151	989.47
293.15	0.0167	988.62
293.15	0.5009	846.45
293.15	0.5472	841.38
293.15	0.5710	838.96
293.15	0.5930	836.87
293.15	0.6495	831.9
293.15	0.6908	828.56
293.15	0.7249	826.04
293.15	0.7543	824.01
293.15	0.7929	821.4
293.15	0.8478	817.94
293.15	0.9322	813.08
293.15	0.9488	812.19
293.15	0.9959	809.82
293.15	1.0000	809.6
298.15	0.0000	997.04
298.15	0.0018	995.81
298.15	0.0019	995.75
298.15	0.0041	994.37
298.15	0.0059	993.24
298.15	0.0076	992.31
298.15	0.0098	990.84
298.15	0.0118	989.8
298.15	0.0127	989.19
298.15	0.0141	988.4
298.15	0.0151	988.05
298.15	0.0167	987.15
298.15	0.5009	842.56
298.15	0.5472	837.46
298.15	0.5710	835.03
298.15	0.5930	832.93
298.15	0.6495	827.94
298.15	0.6908	824.6
298.15	0.7249	822.07
298.15	0.7543	820.05
298.15	0.7929	817.45
298.15	0.8478	814.0
298.15	0.9322	809.2
298.15	0.9488	808.33
298.15	0.9959	806.0
298.15	1.0000	805.78
303.15	0.0000	995.65
303.15	0.0018	994.41
303.15	0.0019	994.34
303.15	0.0041	992.93
303.15	0.0059	991.77
303.15	0.0076	990.82
303.15	0.0098	989.29
303.15	0.0118	988.21
303.15	0.0127	987.58
303.15	0.0141	986.76
303.15	0.0151	986.38
303.15	0.0167	985.44
303.15	0.5009	838.64
303.15	0.5472	833.5
303.15	0.5710	831.05
303.15	0.5930	828.95
303.15	0.6495	823.94
303.15	0.6908	820.59
303.15	0.7249	818.07
303.15	0.7543	816.04
303.15	0.7929	813.46
303.15	0.8478	810.03
303.15	0.9322	805.28
303.15	0.9488	804.44
303.15	0.9959	802.14
303.15	1.0000	801.94

Mass density, kg/m3 [ref]

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Temperature, K = 298.15 (Liquid)

Molality, mol/kg of Water (2) - Liquid	Mass density, kg/m3 - Liquid
0.0000	806.024
0.1588	806.701
0.2034	806.906
0.2526	807.034
0.3019	807.215
0.3998	807.558
0.5007	807.906
0.6011	808.262
0.7050	808.615
0.8032	808.946
0.9017	809.283

Speed of sound, m/s [ref]

Operational conditions:

• Pressure, kPa = 84.5 (Liquid)
• Frequency, MHz = 3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Molality, mol/kg of 1-Butanol (1) - Liquid	Speed of sound, m/s - Liquid
288.15	0.0134	1467.59
288.15	0.0270	1468.74
288.15	0.0405	1469.9
288.15	0.0543	1470.97
288.15	0.0677	1472.07
288.15	0.0813	1473.12
288.15	0.1063	1475.12
288.15	0.1358	1477.39
293.15	0.0134	1483.6
293.15	0.0270	1484.66
293.15	0.0405	1485.68
293.15	0.0543	1486.67
293.15	0.0677	1487.67
293.15	0.0813	1488.64
293.15	0.1063	1490.46
293.15	0.1358	1492.53
298.15	0.0134	1497.73
298.15	0.0270	1498.67
298.15	0.0405	1499.62
298.15	0.0543	1500.51
298.15	0.0677	1501.4
298.15	0.0813	1502.28
298.15	0.1063	1503.97
298.15	0.1358	1505.8
303.15	0.0134	1510.0
303.15	0.0270	1510.86
303.15	0.0405	1511.69
303.15	0.0543	1512.51
303.15	0.0677	1513.34
303.15	0.0813	1514.14
303.15	0.1063	1515.66
303.15	0.1358	1517.36
308.15	0.0134	1520.58
308.15	0.0270	1521.35
308.15	0.0405	1522.15
308.15	0.0543	1522.87
308.15	0.0677	1523.59
308.15	0.0813	1524.39
308.15	0.1063	1525.68
308.15	0.1358	1527.22

Speed of sound, m/s [ref]

Operational conditions:

• Pressure, kPa = 100 (Liquid)
• Frequency, MHz = 3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1-Butanol (1) - Liquid	Speed of sound, m/s - Liquid
283.15	0.0000	1447.6
283.15	0.0018	1455.4
283.15	0.0019	1457.5
283.15	0.0041	1469.4
283.15	0.0059	1476.0
283.15	0.0076	1485.2
283.15	0.0098	1495.2
283.15	0.0118	1504.7
283.15	0.0127	1506.8
283.15	0.0141	1513.7
283.15	0.0151	1517.2
283.15	0.0167	1523.4
283.15	0.5009	1342.2
283.15	0.5472	1336.8
283.15	0.5710	1334.0
283.15	0.5930	1331.6
283.15	0.6495	1326.1
283.15	0.6908	1320.1
283.15	0.7249	1319.3
283.15	0.7543	1315.8
283.15	0.7929	1312.1
283.15	0.8478	1306.7
283.15	0.9488	1295.9
283.15	0.9959	1294.5
283.15	1.0000	1292.2
288.15	0.0000	1466.3
288.15	0.0018	1475.8
288.15	0.0019	1475.6
288.15	0.0041	1486.3
288.15	0.0059	1492.9
288.15	0.0076	1500.1
288.15	0.0098	1509.6
288.15	0.0118	1517.4
288.15	0.0127	1520.5
288.15	0.0141	1525.7
288.15	0.0151	1528.5
288.15	0.0167	1534.1
288.15	0.5009	1328.5
288.15	0.5472	1322.6
288.15	0.5710	1319.6
288.15	0.5930	1317.1
288.15	0.6495	1311.1
288.15	0.6908	1305.1
288.15	0.7249	1303.8
288.15	0.7543	1300.5
288.15	0.7929	1296.6
288.15	0.8478	1290.8
288.15	0.9488	1279.7
288.15	0.9959	1277.6
288.15	1.0000	1275.5
293.15	0.0000	1482.7
293.15	0.0018	1492.5
293.15	0.0019	1490.7
293.15	0.0041	1499.9
293.15	0.0059	1506.6
293.15	0.0076	1512.6
293.15	0.0098	1521.2
293.15	0.0118	1527.7
293.15	0.0127	1531.4
293.15	0.0141	1535.5
293.15	0.0151	1537.9
293.15	0.0167	1542.7
293.15	0.5009	1313.5
293.15	0.5472	1307.4
293.15	0.5710	1304.2
293.15	0.5930	1301.6
293.15	0.6495	1295.2
293.15	0.6908	1288.9
293.15	0.7249	1287.4
293.15	0.7543	1284.3
293.15	0.7929	1279.9
293.15	0.8478	1274.2
293.15	0.9488	1262.7
293.15	0.9959	1259.1
293.15	1.0000	1257.5
298.15	0.0000	1497.0
298.15	0.0018	1506.5
298.15	0.0019	1504.0
298.15	0.0041	1512.1
298.15	0.0059	1518.6
298.15	0.0076	1523.8
298.15	0.0098	1531.6
298.15	0.0118	1537.2
298.15	0.0127	1540.5
298.15	0.0141	1543.9
298.15	0.0151	1545.9
298.15	0.0167	1549.9
298.15	0.5009	1298.5
298.15	0.5472	1292.1
298.15	0.5710	1288.7
298.15	0.5930	1285.9
298.15	0.6495	1279.2
298.15	0.6908	1273.2
298.15	0.7249	1270.8
298.15	0.7543	1268.4
298.15	0.7929	1263.4
298.15	0.8478	1257.4
298.15	0.9488	1245.6
298.15	0.9959	1240.5
298.15	1.0000	1239.3
303.15	0.0000	1509.4
303.15	0.0018	1518.3
303.15	0.0019	1515.7
303.15	0.0041	1522.9
303.15	0.0059	1528.6
303.15	0.0076	1533.6
303.15	0.0098	1540.4
303.15	0.0118	1545.2
303.15	0.0127	1548.2
303.15	0.0141	1550.8
303.15	0.0151	1552.4
303.15	0.0167	1555.6
303.15	0.5009	1283.8
303.15	0.5472	1276.9
303.15	0.5710	1273.2
303.15	0.5930	1270.2
303.15	0.6495	1263.1
303.15	0.6908	1257.8
303.15	0.7249	1254.3
303.15	0.7543	1252.8
303.15	0.7929	1246.7
303.15	0.8478	1240.6
303.15	0.9488	1228.7
303.15	0.9959	1223.5
303.15	1.0000	1222.4

Speed of sound, m/s [ref]

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Temperature, K = 298.15 (Liquid)

Molality, mol/kg of Water (2) - Liquid	Speed of sound, m/s - Liquid
0.0000	1241.6
0.1588	1242.9
0.2034	1243.3
0.2526	1243.2
0.3019	1243.6
0.3998	1244.5
0.5007	1246.2
0.6011	1247.0
0.7050	1248.0
0.8032	1248.8
0.9017	1249.7

Speed of sound, m/s [ref]

Operational conditions:

• Pressure, kPa = 84.5 (Liquid)
• Frequency, MHz = 3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Molality, mol/kg of 1-Butanol (1) - Liquid	Speed of sound, m/s - Liquid
288.15	0.0134	1467.59
288.15	0.0270	1468.74
288.15	0.0405	1469.9
288.15	0.0543	1470.97
288.15	0.0677	1472.07
288.15	0.0813	1473.12
288.15	0.1063	1475.12
288.15	0.1358	1477.39
293.15	0.0134	1483.6
293.15	0.0270	1484.66
293.15	0.0405	1485.68
293.15	0.0543	1486.67
293.15	0.0677	1487.67
293.15	0.0813	1488.64
293.15	0.1063	1490.46
293.15	0.1358	1492.53
298.15	0.0134	1497.73
298.15	0.0270	1498.67
298.15	0.0405	1499.62
298.15	0.0543	1500.51
298.15	0.0677	1501.4
298.15	0.0813	1502.28
298.15	0.1063	1503.97
298.15	0.1358	1505.8
303.15	0.0134	1510.0
303.15	0.0270	1510.86
303.15	0.0405	1511.69
303.15	0.0543	1512.51
303.15	0.0677	1513.34
303.15	0.0813	1514.14
303.15	0.1063	1515.66
303.15	0.1358	1517.36
308.15	0.0134	1520.58
308.15	0.0270	1521.35
308.15	0.0405	1522.15
308.15	0.0543	1522.87
308.15	0.0677	1523.59
308.15	0.0813	1524.39
308.15	0.1063	1525.68
308.15	0.1358	1527.22

Speed of sound, m/s [ref]

Operational conditions:

• Pressure, kPa = 100 (Liquid)
• Frequency, MHz = 3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1-Butanol (1) - Liquid	Speed of sound, m/s - Liquid
283.15	0.0000	1447.6
283.15	0.0018	1455.4
283.15	0.0019	1457.5
283.15	0.0041	1469.4
283.15	0.0059	1476.0
283.15	0.0076	1485.2
283.15	0.0098	1495.2
283.15	0.0118	1504.7
283.15	0.0127	1506.8
283.15	0.0141	1513.7
283.15	0.0151	1517.2
283.15	0.0167	1523.4
283.15	0.5009	1342.2
283.15	0.5472	1336.8
283.15	0.5710	1334.0
283.15	0.5930	1331.6
283.15	0.6495	1326.1
283.15	0.6908	1320.1
283.15	0.7249	1319.3
283.15	0.7543	1315.8
283.15	0.7929	1312.1
283.15	0.8478	1306.7
283.15	0.9488	1295.9
283.15	0.9959	1294.5
283.15	1.0000	1292.2
288.15	0.0000	1466.3
288.15	0.0018	1475.8
288.15	0.0019	1475.6
288.15	0.0041	1486.3
288.15	0.0059	1492.9
288.15	0.0076	1500.1
288.15	0.0098	1509.6
288.15	0.0118	1517.4
288.15	0.0127	1520.5
288.15	0.0141	1525.7
288.15	0.0151	1528.5
288.15	0.0167	1534.1
288.15	0.5009	1328.5
288.15	0.5472	1322.6
288.15	0.5710	1319.6
288.15	0.5930	1317.1
288.15	0.6495	1311.1
288.15	0.6908	1305.1
288.15	0.7249	1303.8
288.15	0.7543	1300.5
288.15	0.7929	1296.6
288.15	0.8478	1290.8
288.15	0.9488	1279.7
288.15	0.9959	1277.6
288.15	1.0000	1275.5
293.15	0.0000	1482.7
293.15	0.0018	1492.5
293.15	0.0019	1490.7
293.15	0.0041	1499.9
293.15	0.0059	1506.6
293.15	0.0076	1512.6
293.15	0.0098	1521.2
293.15	0.0118	1527.7
293.15	0.0127	1531.4
293.15	0.0141	1535.5
293.15	0.0151	1537.9
293.15	0.0167	1542.7
293.15	0.5009	1313.5
293.15	0.5472	1307.4
293.15	0.5710	1304.2
293.15	0.5930	1301.6
293.15	0.6495	1295.2
293.15	0.6908	1288.9
293.15	0.7249	1287.4
293.15	0.7543	1284.3
293.15	0.7929	1279.9
293.15	0.8478	1274.2
293.15	0.9488	1262.7
293.15	0.9959	1259.1
293.15	1.0000	1257.5
298.15	0.0000	1497.0
298.15	0.0018	1506.5
298.15	0.0019	1504.0
298.15	0.0041	1512.1
298.15	0.0059	1518.6
298.15	0.0076	1523.8
298.15	0.0098	1531.6
298.15	0.0118	1537.2
298.15	0.0127	1540.5
298.15	0.0141	1543.9
298.15	0.0151	1545.9
298.15	0.0167	1549.9
298.15	0.5009	1298.5
298.15	0.5472	1292.1
298.15	0.5710	1288.7
298.15	0.5930	1285.9
298.15	0.6495	1279.2
298.15	0.6908	1273.2
298.15	0.7249	1270.8
298.15	0.7543	1268.4
298.15	0.7929	1263.4
298.15	0.8478	1257.4
298.15	0.9488	1245.6
298.15	0.9959	1240.5
298.15	1.0000	1239.3
303.15	0.0000	1509.4
303.15	0.0018	1518.3
303.15	0.0019	1515.7
303.15	0.0041	1522.9
303.15	0.0059	1528.6
303.15	0.0076	1533.6
303.15	0.0098	1540.4
303.15	0.0118	1545.2
303.15	0.0127	1548.2
303.15	0.0141	1550.8
303.15	0.0151	1552.4
303.15	0.0167	1555.6
303.15	0.5009	1283.8
303.15	0.5472	1276.9
303.15	0.5710	1273.2
303.15	0.5930	1270.2
303.15	0.6495	1263.1
303.15	0.6908	1257.8
303.15	0.7249	1254.3
303.15	0.7543	1252.8
303.15	0.7929	1246.7
303.15	0.8478	1240.6
303.15	0.9488	1228.7
303.15	0.9959	1223.5
303.15	1.0000	1222.4

Speed of sound, m/s [ref]

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Temperature, K = 298.15 (Liquid)

Molality, mol/kg of Water (2) - Liquid	Speed of sound, m/s - Liquid
0.0000	1241.6
0.1588	1242.9
0.2034	1243.3
0.2526	1243.2
0.3019	1243.6
0.3998	1244.5
0.5007	1246.2
0.6011	1247.0
0.7050	1248.0
0.8032	1248.8
0.9017	1249.7

Surface tension liquid-gas, N/m [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1-Butanol (1) - Liquid	Surface tension liquid-gas, N/m - Liquid
295.15	1.0000	0.0243
300.15	1.0000	0.0239
305.15	1.0000	0.0236
310.15	1.0000	0.0231
315.15	1.0000	0.0228
295.15	0.0800	0.0276
300.15	0.0800	0.0273
305.15	0.0800	0.0270
310.15	0.0800	0.0266
315.15	0.0800	0.0262
295.15	0.0700	0.0288
300.15	0.0700	0.0286
305.15	0.0700	0.0282
310.15	0.0700	0.0278
315.15	0.0700	0.0273
295.15	0.0600	0.0314
300.15	0.0600	0.0310
305.15	0.0600	0.0306
310.15	0.0600	0.0303
315.15	0.0600	0.0300
295.15	0.0500	0.0338
300.15	0.0500	0.0347
305.15	0.0500	0.0330
310.15	0.0500	0.0326
315.15	0.0500	0.0323
295.15	0.0400	0.0368
300.15	0.0400	0.0383
305.15	0.0400	0.0378
310.15	0.0400	0.0373
315.15	0.0400	0.0369
295.15	0.0300	0.0368
300.15	0.0300	0.0402
305.15	0.0300	0.0397
310.15	0.0300	0.0393
315.15	0.0300	0.0390
295.15	0.0200	0.0408
300.15	0.0200	0.0440
305.15	0.0200	0.0436
310.15	0.0200	0.0434
315.15	0.0200	0.0431
295.15	0.0100	0.0540
300.15	0.0100	0.0533
305.15	0.0100	0.0528
310.15	0.0100	0.0523
315.15	0.0100	0.0518
295.15	0.0000	0.0724
300.15	0.0000	0.0715
305.15	0.0000	0.0708
310.15	0.0000	0.0700
315.15	0.0000	0.0695

Surface tension liquid-gas, N/m [ref]

Operational condition: Temperature, K = 298.15 (Liquid)

Mole fraction of 1-Butanol (1) - Liquid	Surface tension liquid-gas, N/m - Liquid
0.0001	0.0694
0.0002	0.0688
0.0003	0.0681
0.0004	0.0669
0.0006	0.0644
0.0008	0.0625
0.0010	0.0604
0.0015	0.0565
0.0020	0.0539
0.0029	0.0492
0.0039	0.0458
0.0060	0.0407
0.0068	0.0383
0.0082	0.0364
0.0101	0.0337
0.0120	0.0311
0.0129	0.0299
0.0141	0.0291

Surface tension liquid-gas, N/m [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1-Butanol (1) - Liquid	Surface tension liquid-gas, N/m - Liquid
295.15	1.0000	0.0243
300.15	1.0000	0.0239
305.15	1.0000	0.0236
310.15	1.0000	0.0231
315.15	1.0000	0.0228
295.15	0.0800	0.0276
300.15	0.0800	0.0273
305.15	0.0800	0.0270
310.15	0.0800	0.0266
315.15	0.0800	0.0262
295.15	0.0700	0.0288
300.15	0.0700	0.0286
305.15	0.0700	0.0282
310.15	0.0700	0.0278
315.15	0.0700	0.0273
295.15	0.0600	0.0314
300.15	0.0600	0.0310
305.15	0.0600	0.0306
310.15	0.0600	0.0303
315.15	0.0600	0.0300
295.15	0.0500	0.0338
300.15	0.0500	0.0347
305.15	0.0500	0.0330
310.15	0.0500	0.0326
315.15	0.0500	0.0323
295.15	0.0400	0.0368
300.15	0.0400	0.0383
305.15	0.0400	0.0378
310.15	0.0400	0.0373
315.15	0.0400	0.0369
295.15	0.0300	0.0368
300.15	0.0300	0.0402
305.15	0.0300	0.0397
310.15	0.0300	0.0393
315.15	0.0300	0.0390
295.15	0.0200	0.0408
300.15	0.0200	0.0440
305.15	0.0200	0.0436
310.15	0.0200	0.0434
315.15	0.0200	0.0431
295.15	0.0100	0.0540
300.15	0.0100	0.0533
305.15	0.0100	0.0528
310.15	0.0100	0.0523
315.15	0.0100	0.0518
295.15	0.0000	0.0724
300.15	0.0000	0.0715
305.15	0.0000	0.0708
310.15	0.0000	0.0700
315.15	0.0000	0.0695

Surface tension liquid-gas, N/m [ref]

Operational condition: Temperature, K = 298.15 (Liquid)

Mole fraction of 1-Butanol (1) - Liquid	Surface tension liquid-gas, N/m - Liquid
0.0001	0.0694
0.0002	0.0688
0.0003	0.0681
0.0004	0.0669
0.0006	0.0644
0.0008	0.0625
0.0010	0.0604
0.0015	0.0565
0.0020	0.0539
0.0029	0.0492
0.0039	0.0458
0.0060	0.0407
0.0068	0.0383
0.0082	0.0364
0.0101	0.0337
0.0120	0.0311
0.0129	0.0299
0.0141	0.0291

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of 1-Butanol (1) - Liquid	Boiling temperature at pressure P, K - Liquid
0.3620	365.85
0.0210	365.85

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mass fraction of 1-Butanol (1) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0812	365.72
0.7003	365.72

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of 1-Butanol (1) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	373.15
0.0050	369.71
0.0060	368.88
0.0090	367.53
0.5580	365.65
0.5920	365.87
0.6300	366.66
0.6870	368.20
0.7350	369.92
0.7600	370.97
0.8030	373.10
0.8450	375.61
0.8810	378.17
0.9180	381.37
0.9550	385.20
0.9890	389.44
1.0000	390.46

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of 1-Butanol (1) - Liquid	Boiling temperature at pressure P, K - Liquid
0.3620	365.85
0.0210	365.85

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mass fraction of 1-Butanol (1) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0812	365.72
0.7003	365.72

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of 1-Butanol (1) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	373.15
0.0050	369.71
0.0060	368.88
0.0090	367.53
0.5580	365.65
0.5920	365.87
0.6300	366.66
0.6870	368.20
0.7350	369.92
0.7600	370.97
0.8030	373.10
0.8450	375.61
0.8810	378.17
0.9180	381.37
0.9550	385.20
0.9890	389.44
1.0000	390.46

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 101.33 (VLE)

Fixed	Measured
T [K] - VLE	x1[mol/mol] of Water (2) - Liquid	y1[mol/mol] of Water (2) - Vapour
384.65	0.0390	0.2670
383.75	0.0470	0.2990
382.75	0.0550	0.3230
381.95	0.0700	0.3520
371.05	0.2570	0.6290
370.35	0.2750	0.6410
369.85	0.2920	0.6550
369.45	0.3050	0.6620
366.65	0.4960	0.7360
366.55	0.5060	0.7400
366.05	0.5520	0.7500
366.05	0.5640	0.7520
366.05	0.5710	0.7480
365.95	0.5770	0.7500
365.85	0.9750	0.7520
366.15	0.9800	0.7560
365.95	0.9820	0.7580
366.55	0.9850	0.7750
366.55	0.9860	0.7840
366.85	0.9880	0.8080
368.55	0.9920	0.8430
369.95	0.9940	0.8840
371.45	0.9970	0.9290
371.55	0.9980	0.9510
372.55	0.9990	0.9810

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 102.26 (VLE)

Fixed	Measured
T [K] - VLE	x1[mol/mol] of Water (2) - Liquid	y1[mol/mol] of Water (2) - Vapour
384.1	0.0500	0.2530
380.0	0.0920	0.3880
379.55	0.0970	0.4020
374.0	0.1810	0.5560
369.8	0.2910	0.6600
369.5	0.3030	0.6660
367.15	0.4170	0.7240
366.17	0.5460	0.7500
366.15	0.5500	0.7530
365.85	0.7520	0.7540
365.91	0.9020	0.7540
365.95	0.9800	0.7600
366.0	0.9810	0.7630
368.55	0.9910	0.8390
368.95	0.9920	0.8500

Vapor Liquid Equilibrium at Constant Temperature [ref]

Operational condition: Temperature, K = 298.15 (VLE)

Fixed	Measured
P [kPa] - VLE	x1[mol/mol] of Water (2) - Liquid	y1[mol/mol] of Water (2) - Vapour
0.9280	0.0000	0.0000
2.557	0.1500	0.6882
3.409	0.3000	0.7900
3.716	0.5124	0.8253
3.716	0.9812	0.8253
3.516	0.9900	0.8874

Vapor or sublimation pressure, kPa [ref]

Temperature, K - Liquid mixture 1	Vapor or sublimation pressure, kPa - Gas
366.23	101.30

Vapor or sublimation pressure, kPa [ref]

Temperature, K - Liquid mixture 1	Vapor or sublimation pressure, kPa - Gas
366.23	101.30

Sources

• Dortmund Data Bank Vapor-Liquid Equilibrium Data
• Revision of the volumetric method for measurements of liquid liquid equilibria in binary systems
• Measurement of infinite dilution activity coefficients of 1-alkanols (C1 C5) in water as a function of temperature (273 373 K)
• Liquid liquid equilibria of water + 1-butanol + methyl methacrylate or butyl methacrylate or isobutyl methacrylate at 288.15K and 318.15K
• Liquid liquid equilibria of water + 2,3-butanediol + 1-butanol at T = 298.15 K, T = 308.15K and T = 318.15K
• Experimental and calculated liquid-liquid equilibrium data for water + furfural + solvents
• Solubility and tie-line data for ternary aqueous mixtures of cyclopentanol with organic solvents at T = 298.2 K: Experiments and NRTL model
• Measurement of activity coefficient at infinite dilution for some bio-oil components in water and mass transfer study of bubbles in the dilutor.
• Atmospheric densities and interfacial tensions for 1- alkanol (1-butanol to 1-octanol) + water and ether (MTBE, ETBE, DIPE, TAME and THP) + water demixed mixtures.
• A model to calculate concentration-dependent surface tension of binary systems
• Liquid-liquid equilibrium and critical states for the quaternary system propionic acid-n-butanol-n-butyl propionate-water at 303.15 K
• Liquid-liquid equilibrium data and thermophysical properties for ternary systems composed of water, acetic acid and different solvents
• Quaternary liquid-liquid equilibrium, solubility and critical states: Acetic acid - n-butanol - n-butyl acetate - water at 318.15 K and atmospheric pressure
• Liquid phase equilibria of (water + phosphoric acid + 1-butanol or butyl acetate) ternary systems at T = 308.2 K
• Combined effects of salinity and temperature on the solubility of organic compounds
• Extraction of butan-1-ol from water with ionic liquids at T = 308.15 K
• Isothermal (liquid + liquid) equilibrium data at T = 313.15 K and isobaric (vapor + liquid + liquid) equilibrium data at 101.3 kPa for the ternary system (water + 1-butanol + p-xylene)
• VLE measurements using a static cell vapor phase manual sampling method accompanied with an empirical data consistency test
• Volumetric and compressibility behaviour of poly(propylene glycol) - Amino acid aqueous solutions at different temperatures
• Feasibility of bio-based lactate esters as extractant for biobutanol recovery: (Liquid + liquid) equilibria
• Ternary (liquid + liquid) equilibria of {bis(trifluoromethylsulfonyl)-amide based ionic liquids + butan-1-ol + water}
• Isobaric vapor-liquid-liquid-solid equilibrium of the water + NaCl + 1-butanol system at 101.3 kPa
• (Liquid + liquid) equilibria of four alcohol-water systems containing 1,8-cineole at T = 298.15 K
• Liquid-liquid equilibrium in systems used for the production of 5-hydroxymethylfurfural from biomass using alcohols as solvents
• Phase equilibria of the water + 1-butanol + 2-pentanol ternary system at 101.3 kPa
• Separation of water/butan-1-ol with ionic liquids in ternary liquid-liquid phase equilibrium
• Volumetric and sound speed study of aqueous 1-butanol liquid mixtures at different temperatures
• Enthalpies of dilution of aqueous solutions of n-butanol, butanediols, 1,2,4-butanetriol, and 1,2,3,4-butanetetrol at 298.15K
• Isobaric Vapor Liquid Liquid Phase Equilibria Measurements of Three Ternary Water + 2-Butanone + Aliphatic Alcohol (Ethanol, 1-Propanol, 2-Propanol) Systems at 101.3 kPa
• Liquid Liquid Equilibrium Data of Water + Butyric Acid + {Butanal or n-Butanol} Ternary Systems at 293.15, 308.15, and 323.15 K
• Measurement and Correlation of Liquid Liquid Equilibria for the Ternary Systems of Water + d-Fructose + 1-Butanol, Water + d-Glucose + 1-Butanol, and Water + d-Galactose + 1-Butanol at (288.2, 303.2 and 318.2) K
• Design of a Salt-Free Aqueous Two-Phase System Containing Butanol, n-Butylpyridine Dicyanamide, and Water: Equilibrium Data and Correlation
• Concentration Dependence of Surface Tension for Very Dilute Aqueous Solutions of Organic Non-Electrolytes
• Compressibility Studies of Binary Solutions Involving Water as a Solute in Nonaqueous Solvents at T ) 298.15 K
• Liquid Liquid, Vapor Liquid, and Vapor Liquid Liquid Equilibrium Data for the Water n-Butanol Cyclohexane System at Atmospheric Pressure: Experimental Determination and Correlation
• Ternary Liquid Liquid Equilibrium Data for the Water + Acetonitrile + {Butan-1-ol or 2-Methylpropan-1-ol} Systems at (303.2, 323.2, 343.2) K and 1 atm
• Phase Equilibrium for the Esterification Reaction of Acetic Acid + Butan-1-ol at 101.3 kPa