Mixture of Ethanol + Pentane, 2,2,4-trimethyl-

Datasets

1. Mole fraction (16)
2. η - Viscosity, Pa*s (8)
3. Excess molar enthalpy (molar enthalpy (2)
4. n₀ - Refractive index (Na D-line) (10)
5. ρ_l - Mass density, kg/m3 (14)
6. c_sound,fluid - Speed of Sound, m/s (2)
7. γ - Surface tension liquid-gas, N/m (2)
8. T_boil - Boiling temperature at pressure P, K (10)
9. Azeotropic temperature, K (2)

Mole fraction of Ethanol (1) [ref]

Operational condition: Pressure, kPa = 101.32 (Liquid)

Mole fraction of Ethanol (1) - Liquid	Mole fraction of Ethanol (1) - Gas
0.0000	0.0000
0.0240	0.2510
0.0570	0.4300
0.0970	0.5340
0.1370	0.5660
0.2090	0.5860
0.2730	0.6000
0.3330	0.6080
0.4000	0.6180
0.4440	0.6210
0.5020	0.6260
0.5450	0.6310
0.5970	0.6400
0.6520	0.6480
0.7050	0.6570
0.7540	0.6650
0.8070	0.6790
0.8600	0.7130
0.9060	0.7630
0.9540	0.8490
1.0000	1.0000

Mole fraction of Ethanol (1) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Ethanol (1) - Liquid	Mole fraction of Ethanol (1) - Gas
0.0000	0.0000
0.0280	0.2870
0.0580	0.4300
0.0880	0.5200
0.1440	0.5800
0.2730	0.6000
0.3070	0.6030
0.3330	0.6080
0.4000	0.6180
0.4460	0.6200
0.5020	0.6260
0.5450	0.6310
0.5970	0.6400
0.6520	0.6480
0.7050	0.6570
0.7650	0.6770
0.8000	0.6890
0.8600	0.7130
0.9020	0.7560
0.9580	0.8300
1.0000	1.0000

Azeotropic composition: mole fraction of Ethanol (1) [ref]

Pressure, kPa - Liquid	Azeotropic composition: mole fraction of Ethanol (1) - Liquid
101.30	0.6460

Mole fraction of Ethanol (1) [ref]

Operational condition: Temperature, K = 333.15 (Gas)

Mole fraction of Ethanol (1) - Liquid	Mole fraction of Ethanol (1) - Gas
0.0196	0.3315
0.0589	0.4679
0.0791	0.4999
0.1189	0.5346
0.1676	0.5531
0.2292	0.5666
0.2904	0.5764
0.3486	0.5842
0.4102	0.5912
0.4702	0.5993
0.5303	0.6066
0.5897	0.6084
0.6499	0.6103
0.7099	0.6292
0.7705	0.6428
0.8300	0.6723
0.8803	0.7105
0.9198	0.7526
0.9399	0.7989
0.9602	0.8486
0.9799	0.9260

Mole fraction of Ethanol (1) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Ethanol (1) - Liquid	Mole fraction of Ethanol (1) - Gas
1.0000	1.0000
0.9960	0.9950
0.9840	0.9220
0.9820	0.9670
0.9660	0.9030
0.9660	0.8410
0.9570	0.8260
0.9350	0.7820
0.8640	0.7300
0.6740	0.6820
0.6180	0.6410
0.5910	0.6610
0.5640	0.6350
0.5320	0.6270
0.4940	0.6530
0.4620	0.6240
0.4190	0.6200
0.3530	0.6120
0.2550	0.5940
0.2510	0.5940
0.1840	0.5750
0.0381	0.3930
0.0000	0.0000

Mole fraction of Ethanol (1) [ref]

Fixed		Measured
Temperature, K - Gas	Mole fraction of Ethanol (1) - Liquid	Mole fraction of Ethanol (1) - Gas
308.15	0.0560	0.4360
308.15	0.1540	0.5000
308.15	0.1990	0.5100
308.15	0.2400	0.5190
308.15	0.3290	0.5270
308.15	0.4310	0.5320
308.15	0.5460	0.5400
308.15	0.6110	0.5480
308.15	0.6640	0.5570
308.15	0.7440	0.5850
308.15	0.7560	0.5880
308.15	0.7760	0.5970
308.15	0.7790	0.5920
308.15	0.8170	0.6110
308.15	0.8410	0.6300
308.15	0.8610	0.6480
308.15	0.8930	0.6690
308.15	0.9150	0.7010
308.15	0.9410	0.7480
308.15	0.9500	0.7730
308.15	0.9640	0.8110
308.15	0.9720	0.8360
308.15	0.9760	0.8580
308.15	0.9890	0.9220
313.15	0.0560	0.4440
313.15	0.1050	0.4840
313.15	0.1540	0.5040
313.15	0.1990	0.5150
313.15	0.2400	0.5250
313.15	0.2790	0.5300
313.15	0.3290	0.5410
313.15	0.4310	0.5440
313.15	0.4810	0.5480
313.15	0.5460	0.5560
313.15	0.6030	0.5590
313.15	0.6410	0.5670
313.15	0.7220	0.5860
313.15	0.7560	0.5900
313.15	0.7790	0.6100
313.15	0.8170	0.6230
313.15	0.8410	0.6400
313.15	0.8610	0.6440
313.15	0.8930	0.6820
313.15	0.9050	0.6970
313.15	0.9250	0.7270
313.15	0.9410	0.7610
313.15	0.9500	0.7790
313.15	0.9670	0.8280
313.15	0.9760	0.8650
313.15	0.9890	0.9300
318.15	0.0560	0.4320
318.15	0.1050	0.4910
318.15	0.1540	0.5140
318.15	0.1990	0.5260
318.15	0.2400	0.5350
318.15	0.2790	0.5410
318.15	0.3290	0.5480
318.15	0.4310	0.5570
318.15	0.4810	0.5620
318.15	0.5460	0.5660
318.15	0.6110	0.5770
318.15	0.6640	0.5820
318.15	0.6990	0.5820
318.15	0.7500	0.5960
318.15	0.7790	0.6100
318.15	0.8170	0.6390
318.15	0.8610	0.6660
318.15	0.8930	0.6910
318.15	0.9050	0.7140
318.15	0.9250	0.7390
318.15	0.9460	0.7790
318.15	0.9620	0.8210
318.15	0.9660	0.8340
318.15	0.9890	0.9320

Mole fraction of Ethanol (1) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Ethanol (1) - Liquid	Mole fraction of Ethanol (1) - Gas
0.0000	0.0000
0.1406	0.5971
0.1456	0.5813
0.1698	0.5920
0.1914	0.5986
0.2058	0.6056
0.2203	0.6007
0.2398	0.5988
0.2451	0.6087
0.2659	0.6103
0.2922	0.6112
0.2930	0.6100
0.2962	0.6113
0.6299	0.6454
0.6337	0.6422
0.7999	0.6566
0.8078	0.6706
0.8161	0.6740
0.9377	0.7921
0.9412	0.7817
0.9494	0.8034
0.9544	0.8053
0.9575	0.8201
1.0000	1.0000

Mole fraction of Ethanol (1) [ref]

Operational condition: Temperature, K = 323.15 (Gas)

Mole fraction of Ethanol (1) - Liquid	Mole fraction of Ethanol (1) - Gas
0.0045	0.1432
0.0097	0.2414
0.0210	0.3604
0.0601	0.4435
0.0808	0.4624
0.1197	0.4878
0.1701	0.5081
0.2303	0.5313
0.2903	0.5463
0.3501	0.5592
0.4114	0.5699
0.4699	0.5775
0.5305	0.5891
0.5907	0.6028
0.6504	0.6155
0.7109	0.6329
0.7700	0.6467
0.8302	0.6699
0.8806	0.7007
0.9201	0.7532
0.9406	0.7816
0.9602	0.8309
0.9802	0.8964

Mole fraction of Ethanol (1) [ref]

Operational condition: Pressure, kPa = 101.32 (Liquid)

Mole fraction of Ethanol (1) - Liquid	Mole fraction of Ethanol (1) - Gas
0.0000	0.0000
0.0240	0.2510
0.0570	0.4300
0.0970	0.5340
0.1370	0.5660
0.2090	0.5860
0.2730	0.6000
0.3330	0.6080
0.4000	0.6180
0.4440	0.6210
0.5020	0.6260
0.5450	0.6310
0.5970	0.6400
0.6520	0.6480
0.7050	0.6570
0.7540	0.6650
0.8070	0.6790
0.8600	0.7130
0.9060	0.7630
0.9540	0.8490
1.0000	1.0000

Mole fraction of Ethanol (1) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Ethanol (1) - Liquid	Mole fraction of Ethanol (1) - Gas
0.0000	0.0000
0.0280	0.2870
0.0580	0.4300
0.0880	0.5200
0.1440	0.5800
0.2730	0.6000
0.3070	0.6030
0.3330	0.6080
0.4000	0.6180
0.4460	0.6200
0.5020	0.6260
0.5450	0.6310
0.5970	0.6400
0.6520	0.6480
0.7050	0.6570
0.7650	0.6770
0.8000	0.6890
0.8600	0.7130
0.9020	0.7560
0.9580	0.8300
1.0000	1.0000

Azeotropic composition: mole fraction of Ethanol (1) [ref]

Pressure, kPa - Liquid	Azeotropic composition: mole fraction of Ethanol (1) - Liquid
101.30	0.6460

Mole fraction of Ethanol (1) [ref]

Operational condition: Temperature, K = 333.15 (Gas)

Mole fraction of Ethanol (1) - Liquid	Mole fraction of Ethanol (1) - Gas
0.0196	0.3315
0.0589	0.4679
0.0791	0.4999
0.1189	0.5346
0.1676	0.5531
0.2292	0.5666
0.2904	0.5764
0.3486	0.5842
0.4102	0.5912
0.4702	0.5993
0.5303	0.6066
0.5897	0.6084
0.6499	0.6103
0.7099	0.6292
0.7705	0.6428
0.8300	0.6723
0.8803	0.7105
0.9198	0.7526
0.9399	0.7989
0.9602	0.8486
0.9799	0.9260

Mole fraction of Ethanol (1) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Ethanol (1) - Liquid	Mole fraction of Ethanol (1) - Gas
1.0000	1.0000
0.9960	0.9950
0.9840	0.9220
0.9820	0.9670
0.9660	0.9030
0.9660	0.8410
0.9570	0.8260
0.9350	0.7820
0.8640	0.7300
0.6740	0.6820
0.6180	0.6410
0.5910	0.6610
0.5640	0.6350
0.5320	0.6270
0.4940	0.6530
0.4620	0.6240
0.4190	0.6200
0.3530	0.6120
0.2550	0.5940
0.2510	0.5940
0.1840	0.5750
0.0381	0.3930
0.0000	0.0000

Mole fraction of Ethanol (1) [ref]

Fixed		Measured
Temperature, K - Gas	Mole fraction of Ethanol (1) - Liquid	Mole fraction of Ethanol (1) - Gas
308.15	0.0560	0.4360
308.15	0.1540	0.5000
308.15	0.1990	0.5100
308.15	0.2400	0.5190
308.15	0.3290	0.5270
308.15	0.4310	0.5320
308.15	0.5460	0.5400
308.15	0.6110	0.5480
308.15	0.6640	0.5570
308.15	0.7440	0.5850
308.15	0.7560	0.5880
308.15	0.7760	0.5970
308.15	0.7790	0.5920
308.15	0.8170	0.6110
308.15	0.8410	0.6300
308.15	0.8610	0.6480
308.15	0.8930	0.6690
308.15	0.9150	0.7010
308.15	0.9410	0.7480
308.15	0.9500	0.7730
308.15	0.9640	0.8110
308.15	0.9720	0.8360
308.15	0.9760	0.8580
308.15	0.9890	0.9220
313.15	0.0560	0.4440
313.15	0.1050	0.4840
313.15	0.1540	0.5040
313.15	0.1990	0.5150
313.15	0.2400	0.5250
313.15	0.2790	0.5300
313.15	0.3290	0.5410
313.15	0.4310	0.5440
313.15	0.4810	0.5480
313.15	0.5460	0.5560
313.15	0.6030	0.5590
313.15	0.6410	0.5670
313.15	0.7220	0.5860
313.15	0.7560	0.5900
313.15	0.7790	0.6100
313.15	0.8170	0.6230
313.15	0.8410	0.6400
313.15	0.8610	0.6440
313.15	0.8930	0.6820
313.15	0.9050	0.6970
313.15	0.9250	0.7270
313.15	0.9410	0.7610
313.15	0.9500	0.7790
313.15	0.9670	0.8280
313.15	0.9760	0.8650
313.15	0.9890	0.9300
318.15	0.0560	0.4320
318.15	0.1050	0.4910
318.15	0.1540	0.5140
318.15	0.1990	0.5260
318.15	0.2400	0.5350
318.15	0.2790	0.5410
318.15	0.3290	0.5480
318.15	0.4310	0.5570
318.15	0.4810	0.5620
318.15	0.5460	0.5660
318.15	0.6110	0.5770
318.15	0.6640	0.5820
318.15	0.6990	0.5820
318.15	0.7500	0.5960
318.15	0.7790	0.6100
318.15	0.8170	0.6390
318.15	0.8610	0.6660
318.15	0.8930	0.6910
318.15	0.9050	0.7140
318.15	0.9250	0.7390
318.15	0.9460	0.7790
318.15	0.9620	0.8210
318.15	0.9660	0.8340
318.15	0.9890	0.9320

Mole fraction of Ethanol (1) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Ethanol (1) - Liquid	Mole fraction of Ethanol (1) - Gas
0.0000	0.0000
0.1406	0.5971
0.1456	0.5813
0.1698	0.5920
0.1914	0.5986
0.2058	0.6056
0.2203	0.6007
0.2398	0.5988
0.2451	0.6087
0.2659	0.6103
0.2922	0.6112
0.2930	0.6100
0.2962	0.6113
0.6299	0.6454
0.6337	0.6422
0.7999	0.6566
0.8078	0.6706
0.8161	0.6740
0.9377	0.7921
0.9412	0.7817
0.9494	0.8034
0.9544	0.8053
0.9575	0.8201
1.0000	1.0000

Mole fraction of Ethanol (1) [ref]

Operational condition: Temperature, K = 323.15 (Gas)

Mole fraction of Ethanol (1) - Liquid	Mole fraction of Ethanol (1) - Gas
0.0045	0.1432
0.0097	0.2414
0.0210	0.3604
0.0601	0.4435
0.0808	0.4624
0.1197	0.4878
0.1701	0.5081
0.2303	0.5313
0.2903	0.5463
0.3501	0.5592
0.4114	0.5699
0.4699	0.5775
0.5305	0.5891
0.5907	0.6028
0.6504	0.6155
0.7109	0.6329
0.7700	0.6467
0.8302	0.6699
0.8806	0.7007
0.9201	0.7532
0.9406	0.7816
0.9602	0.8309
0.9802	0.8964

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 100.8 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol (1) - Liquid	Viscosity, Pa*s - Liquid
298.15	0.0000	0.0005
298.15	0.0500	0.0005
298.15	0.1000	0.0005
298.15	0.1500	0.0005
298.15	0.2000	0.0005
298.15	0.2500	0.0005
298.15	0.3000	0.0005
298.15	0.3500	0.0005
298.15	0.4000	0.0005
298.15	0.4500	0.0006
298.15	0.5000	0.0006
298.15	0.5500	0.0006
298.15	0.6000	0.0006
298.15	0.6500	0.0007
298.15	0.7000	0.0007
298.15	0.7500	0.0008
298.15	0.8000	0.0008
298.15	0.8500	0.0009
298.15	0.9000	0.0009
298.15	0.9500	0.0010
298.15	1.0000	0.0011
308.15	0.0000	0.0004
308.15	0.0500	0.0004
308.15	0.1000	0.0004
308.15	0.1500	0.0004
308.15	0.2000	0.0004
308.15	0.2500	0.0004
308.15	0.3000	0.0004
308.15	0.3500	0.0005
308.15	0.4000	0.0005
308.15	0.4500	0.0005
308.15	0.5000	0.0005
308.15	0.5500	0.0005
308.15	0.6000	0.0006
308.15	0.6500	0.0006
308.15	0.7000	0.0006
308.15	0.7500	0.0006
308.15	0.8000	0.0007
308.15	0.8500	0.0007
308.15	0.9000	0.0008
308.15	0.9500	0.0008
308.15	1.0000	0.0009
318.15	0.0000	0.0004
318.15	0.0500	0.0004
318.15	0.1000	0.0004
318.15	0.1500	0.0004
318.15	0.2000	0.0004
318.15	0.2500	0.0004
318.15	0.3000	0.0004
318.15	0.3500	0.0004
318.15	0.4000	0.0004
318.15	0.4500	0.0004
318.15	0.5000	0.0004
318.15	0.5500	0.0005
318.15	0.6000	0.0005
318.15	0.6500	0.0005
318.15	0.7000	0.0005
318.15	0.7500	0.0006
318.15	0.8000	0.0006
318.15	0.8500	0.0006
318.15	0.9000	0.0007
318.15	0.9500	0.0007
318.15	1.0000	0.0008

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 100.8 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol (1) - Liquid	Viscosity, Pa*s - Liquid
288.15	0.0000	0.0005
288.15	0.0502	0.0005
288.15	0.1000	0.0005
288.15	0.1500	0.0005
288.15	0.2000	0.0006
288.15	0.2500	0.0006
288.15	0.3000	0.0006
288.15	0.3500	0.0006
288.15	0.4000	0.0006
288.15	0.4500	0.0007
288.15	0.5000	0.0007
288.15	0.5500	0.0007
288.15	0.6000	0.0008
288.15	0.6500	0.0008
288.15	0.7000	0.0008
288.15	0.7500	0.0009
288.15	0.8000	0.0010
288.15	0.8500	0.0010
288.15	0.9000	0.0011
288.15	0.9500	0.0012
288.15	1.0000	0.0013
298.15	0.0000	0.0005
298.15	0.0502	0.0005
298.15	0.1000	0.0005
298.15	0.1500	0.0005
298.15	0.2000	0.0005
298.15	0.2500	0.0005
298.15	0.3000	0.0005
298.15	0.3500	0.0005
298.15	0.4000	0.0005
298.15	0.4500	0.0006
298.15	0.5000	0.0006
298.15	0.5500	0.0006
298.15	0.6000	0.0006
298.15	0.6500	0.0007
298.15	0.7000	0.0007
298.15	0.7500	0.0008
298.15	0.8000	0.0008
298.15	0.8500	0.0009
298.15	0.9000	0.0009
298.15	0.9500	0.0010
298.15	1.0000	0.0011
308.15	0.0000	0.0004
308.15	0.0502	0.0004
308.15	0.1000	0.0004
308.15	0.1500	0.0004
308.15	0.2000	0.0004
308.15	0.2500	0.0004
308.15	0.3000	0.0005
308.15	0.3500	0.0005
308.15	0.4000	0.0005
308.15	0.4500	0.0005
308.15	0.5000	0.0005
308.15	0.5500	0.0005
308.15	0.6000	0.0006
308.15	0.6500	0.0006
308.15	0.7000	0.0006
308.15	0.7500	0.0006
308.15	0.8000	0.0007
308.15	0.8500	0.0007
308.15	0.9000	0.0008
308.15	0.9500	0.0008
308.15	1.0000	0.0009

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 100.8 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol (1) - Liquid	Viscosity, Pa*s - Liquid
298.15	0.0000	0.0005
298.15	0.0500	0.0005
298.15	0.1000	0.0005
298.15	0.1500	0.0005
298.15	0.2000	0.0005
298.15	0.2500	0.0005
298.15	0.3000	0.0005
298.15	0.3500	0.0005
298.15	0.4000	0.0005
298.15	0.4500	0.0006
298.15	0.5000	0.0006
298.15	0.5500	0.0006
298.15	0.6000	0.0006
298.15	0.6500	0.0007
298.15	0.7000	0.0007
298.15	0.7500	0.0008
298.15	0.8000	0.0008
298.15	0.8500	0.0009
298.15	0.9000	0.0009
298.15	0.9500	0.0010
298.15	1.0000	0.0011
308.15	0.0000	0.0004
308.15	0.0500	0.0004
308.15	0.1000	0.0004
308.15	0.1500	0.0004
308.15	0.2000	0.0004
308.15	0.2500	0.0004
308.15	0.3000	0.0004
308.15	0.3500	0.0005
308.15	0.4000	0.0005
308.15	0.4500	0.0005
308.15	0.5000	0.0005
308.15	0.5500	0.0005
308.15	0.6000	0.0006
308.15	0.6500	0.0006
308.15	0.7000	0.0006
308.15	0.7500	0.0006
308.15	0.8000	0.0007
308.15	0.8500	0.0007
308.15	0.9000	0.0008
308.15	0.9500	0.0008
308.15	1.0000	0.0009
318.15	0.0000	0.0004
318.15	0.0500	0.0004
318.15	0.1000	0.0004
318.15	0.1500	0.0004
318.15	0.2000	0.0004
318.15	0.2500	0.0004
318.15	0.3000	0.0004
318.15	0.3500	0.0004
318.15	0.4000	0.0004
318.15	0.4500	0.0004
318.15	0.5000	0.0004
318.15	0.5500	0.0005
318.15	0.6000	0.0005
318.15	0.6500	0.0005
318.15	0.7000	0.0005
318.15	0.7500	0.0006
318.15	0.8000	0.0006
318.15	0.8500	0.0006
318.15	0.9000	0.0007
318.15	0.9500	0.0007
318.15	1.0000	0.0008

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 100.8 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol (1) - Liquid	Viscosity, Pa*s - Liquid
288.15	0.0000	0.0005
288.15	0.0502	0.0005
288.15	0.1000	0.0005
288.15	0.1500	0.0005
288.15	0.2000	0.0006
288.15	0.2500	0.0006
288.15	0.3000	0.0006
288.15	0.3500	0.0006
288.15	0.4000	0.0006
288.15	0.4500	0.0007
288.15	0.5000	0.0007
288.15	0.5500	0.0007
288.15	0.6000	0.0008
288.15	0.6500	0.0008
288.15	0.7000	0.0008
288.15	0.7500	0.0009
288.15	0.8000	0.0010
288.15	0.8500	0.0010
288.15	0.9000	0.0011
288.15	0.9500	0.0012
288.15	1.0000	0.0013
298.15	0.0000	0.0005
298.15	0.0502	0.0005
298.15	0.1000	0.0005
298.15	0.1500	0.0005
298.15	0.2000	0.0005
298.15	0.2500	0.0005
298.15	0.3000	0.0005
298.15	0.3500	0.0005
298.15	0.4000	0.0005
298.15	0.4500	0.0006
298.15	0.5000	0.0006
298.15	0.5500	0.0006
298.15	0.6000	0.0006
298.15	0.6500	0.0007
298.15	0.7000	0.0007
298.15	0.7500	0.0008
298.15	0.8000	0.0008
298.15	0.8500	0.0009
298.15	0.9000	0.0009
298.15	0.9500	0.0010
298.15	1.0000	0.0011
308.15	0.0000	0.0004
308.15	0.0502	0.0004
308.15	0.1000	0.0004
308.15	0.1500	0.0004
308.15	0.2000	0.0004
308.15	0.2500	0.0004
308.15	0.3000	0.0005
308.15	0.3500	0.0005
308.15	0.4000	0.0005
308.15	0.4500	0.0005
308.15	0.5000	0.0005
308.15	0.5500	0.0005
308.15	0.6000	0.0006
308.15	0.6500	0.0006
308.15	0.7000	0.0006
308.15	0.7500	0.0006
308.15	0.8000	0.0007
308.15	0.8500	0.0007
308.15	0.9000	0.0008
308.15	0.9500	0.0008
308.15	1.0000	0.0009

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 100.8 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol (1) - Liquid	Viscosity, Pa*s - Liquid
298.15	0.0000	0.0005
298.15	0.0500	0.0005
298.15	0.1000	0.0005
298.15	0.1500	0.0005
298.15	0.2000	0.0005
298.15	0.2500	0.0005
298.15	0.3000	0.0005
298.15	0.3500	0.0005
298.15	0.4000	0.0005
298.15	0.4500	0.0006
298.15	0.5000	0.0006
298.15	0.5500	0.0006
298.15	0.6000	0.0006
298.15	0.6500	0.0007
298.15	0.7000	0.0007
298.15	0.7500	0.0008
298.15	0.8000	0.0008
298.15	0.8500	0.0009
298.15	0.9000	0.0009
298.15	0.9500	0.0010
298.15	1.0000	0.0011
308.15	0.0000	0.0004
308.15	0.0500	0.0004
308.15	0.1000	0.0004
308.15	0.1500	0.0004
308.15	0.2000	0.0004
308.15	0.2500	0.0004
308.15	0.3000	0.0004
308.15	0.3500	0.0005
308.15	0.4000	0.0005
308.15	0.4500	0.0005
308.15	0.5000	0.0005
308.15	0.5500	0.0005
308.15	0.6000	0.0006
308.15	0.6500	0.0006
308.15	0.7000	0.0006
308.15	0.7500	0.0006
308.15	0.8000	0.0007
308.15	0.8500	0.0007
308.15	0.9000	0.0008
308.15	0.9500	0.0008
308.15	1.0000	0.0009
318.15	0.0000	0.0004
318.15	0.0500	0.0004
318.15	0.1000	0.0004
318.15	0.1500	0.0004
318.15	0.2000	0.0004
318.15	0.2500	0.0004
318.15	0.3000	0.0004
318.15	0.3500	0.0004
318.15	0.4000	0.0004
318.15	0.4500	0.0004
318.15	0.5000	0.0004
318.15	0.5500	0.0005
318.15	0.6000	0.0005
318.15	0.6500	0.0005
318.15	0.7000	0.0005
318.15	0.7500	0.0006
318.15	0.8000	0.0006
318.15	0.8500	0.0006
318.15	0.9000	0.0007
318.15	0.9500	0.0007
318.15	1.0000	0.0008

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 100.8 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol (1) - Liquid	Viscosity, Pa*s - Liquid
288.15	0.0000	0.0005
288.15	0.0502	0.0005
288.15	0.1000	0.0005
288.15	0.1500	0.0005
288.15	0.2000	0.0006
288.15	0.2500	0.0006
288.15	0.3000	0.0006
288.15	0.3500	0.0006
288.15	0.4000	0.0006
288.15	0.4500	0.0007
288.15	0.5000	0.0007
288.15	0.5500	0.0007
288.15	0.6000	0.0008
288.15	0.6500	0.0008
288.15	0.7000	0.0008
288.15	0.7500	0.0009
288.15	0.8000	0.0010
288.15	0.8500	0.0010
288.15	0.9000	0.0011
288.15	0.9500	0.0012
288.15	1.0000	0.0013
298.15	0.0000	0.0005
298.15	0.0502	0.0005
298.15	0.1000	0.0005
298.15	0.1500	0.0005
298.15	0.2000	0.0005
298.15	0.2500	0.0005
298.15	0.3000	0.0005
298.15	0.3500	0.0005
298.15	0.4000	0.0005
298.15	0.4500	0.0006
298.15	0.5000	0.0006
298.15	0.5500	0.0006
298.15	0.6000	0.0006
298.15	0.6500	0.0007
298.15	0.7000	0.0007
298.15	0.7500	0.0008
298.15	0.8000	0.0008
298.15	0.8500	0.0009
298.15	0.9000	0.0009
298.15	0.9500	0.0010
298.15	1.0000	0.0011
308.15	0.0000	0.0004
308.15	0.0502	0.0004
308.15	0.1000	0.0004
308.15	0.1500	0.0004
308.15	0.2000	0.0004
308.15	0.2500	0.0004
308.15	0.3000	0.0005
308.15	0.3500	0.0005
308.15	0.4000	0.0005
308.15	0.4500	0.0005
308.15	0.5000	0.0005
308.15	0.5500	0.0005
308.15	0.6000	0.0006
308.15	0.6500	0.0006
308.15	0.7000	0.0006
308.15	0.7500	0.0006
308.15	0.8000	0.0007
308.15	0.8500	0.0007
308.15	0.9000	0.0008
308.15	0.9500	0.0008
308.15	1.0000	0.0009

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 100.8 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol (1) - Liquid	Viscosity, Pa*s - Liquid
298.15	0.0000	0.0005
298.15	0.0500	0.0005
298.15	0.1000	0.0005
298.15	0.1500	0.0005
298.15	0.2000	0.0005
298.15	0.2500	0.0005
298.15	0.3000	0.0005
298.15	0.3500	0.0005
298.15	0.4000	0.0005
298.15	0.4500	0.0006
298.15	0.5000	0.0006
298.15	0.5500	0.0006
298.15	0.6000	0.0006
298.15	0.6500	0.0007
298.15	0.7000	0.0007
298.15	0.7500	0.0008
298.15	0.8000	0.0008
298.15	0.8500	0.0009
298.15	0.9000	0.0009
298.15	0.9500	0.0010
298.15	1.0000	0.0011
308.15	0.0000	0.0004
308.15	0.0500	0.0004
308.15	0.1000	0.0004
308.15	0.1500	0.0004
308.15	0.2000	0.0004
308.15	0.2500	0.0004
308.15	0.3000	0.0004
308.15	0.3500	0.0005
308.15	0.4000	0.0005
308.15	0.4500	0.0005
308.15	0.5000	0.0005
308.15	0.5500	0.0005
308.15	0.6000	0.0006
308.15	0.6500	0.0006
308.15	0.7000	0.0006
308.15	0.7500	0.0006
308.15	0.8000	0.0007
308.15	0.8500	0.0007
308.15	0.9000	0.0008
308.15	0.9500	0.0008
308.15	1.0000	0.0009
318.15	0.0000	0.0004
318.15	0.0500	0.0004
318.15	0.1000	0.0004
318.15	0.1500	0.0004
318.15	0.2000	0.0004
318.15	0.2500	0.0004
318.15	0.3000	0.0004
318.15	0.3500	0.0004
318.15	0.4000	0.0004
318.15	0.4500	0.0004
318.15	0.5000	0.0004
318.15	0.5500	0.0005
318.15	0.6000	0.0005
318.15	0.6500	0.0005
318.15	0.7000	0.0005
318.15	0.7500	0.0006
318.15	0.8000	0.0006
318.15	0.8500	0.0006
318.15	0.9000	0.0007
318.15	0.9500	0.0007
318.15	1.0000	0.0008

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 100.8 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol (1) - Liquid	Viscosity, Pa*s - Liquid
288.15	0.0000	0.0005
288.15	0.0502	0.0005
288.15	0.1000	0.0005
288.15	0.1500	0.0005
288.15	0.2000	0.0006
288.15	0.2500	0.0006
288.15	0.3000	0.0006
288.15	0.3500	0.0006
288.15	0.4000	0.0006
288.15	0.4500	0.0007
288.15	0.5000	0.0007
288.15	0.5500	0.0007
288.15	0.6000	0.0008
288.15	0.6500	0.0008
288.15	0.7000	0.0008
288.15	0.7500	0.0009
288.15	0.8000	0.0010
288.15	0.8500	0.0010
288.15	0.9000	0.0011
288.15	0.9500	0.0012
288.15	1.0000	0.0013
298.15	0.0000	0.0005
298.15	0.0502	0.0005
298.15	0.1000	0.0005
298.15	0.1500	0.0005
298.15	0.2000	0.0005
298.15	0.2500	0.0005
298.15	0.3000	0.0005
298.15	0.3500	0.0005
298.15	0.4000	0.0005
298.15	0.4500	0.0006
298.15	0.5000	0.0006
298.15	0.5500	0.0006
298.15	0.6000	0.0006
298.15	0.6500	0.0007
298.15	0.7000	0.0007
298.15	0.7500	0.0008
298.15	0.8000	0.0008
298.15	0.8500	0.0009
298.15	0.9000	0.0009
298.15	0.9500	0.0010
298.15	1.0000	0.0011
308.15	0.0000	0.0004
308.15	0.0502	0.0004
308.15	0.1000	0.0004
308.15	0.1500	0.0004
308.15	0.2000	0.0004
308.15	0.2500	0.0004
308.15	0.3000	0.0005
308.15	0.3500	0.0005
308.15	0.4000	0.0005
308.15	0.4500	0.0005
308.15	0.5000	0.0005
308.15	0.5500	0.0005
308.15	0.6000	0.0006
308.15	0.6500	0.0006
308.15	0.7000	0.0006
308.15	0.7500	0.0006
308.15	0.8000	0.0007
308.15	0.8500	0.0007
308.15	0.9000	0.0008
308.15	0.9500	0.0008
308.15	1.0000	0.0009

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

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Temperature, K = 303.15 (Liquid)

Mole fraction of Ethanol (1) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.1291	0.5429
0.2383	0.6340
0.3320	0.6620
0.4132	0.6590
0.4842	0.6390
0.5469	0.6114
0.6026	0.5773
0.6525	0.5410
0.6974	0.5005
0.7380	0.4612
0.7749	0.4183
0.8086	0.3757
0.8395	0.3335
0.8679	0.2886
0.8942	0.2436
0.9185	0.1978
0.9410	0.1494
0.9620	0.1005
0.9817	0.0501

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

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Temperature, K = 303.15 (Liquid)

Mole fraction of Ethanol (1) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.1291	0.5429
0.2383	0.6340
0.3320	0.6620
0.4132	0.6590
0.4842	0.6390
0.5469	0.6114
0.6026	0.5773
0.6525	0.5410
0.6974	0.5005
0.7380	0.4612
0.7749	0.4183
0.8086	0.3757
0.8395	0.3335
0.8679	0.2886
0.8942	0.2436
0.9185	0.1978
0.9410	0.1494
0.9620	0.1005
0.9817	0.0501

Refractive index (Na D-line) [ref]

Operational condition: Pressure, kPa = 100.8 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol (1) - Liquid	Refractive index (Na D-line) - Liquid
288.15	0.0000	1.394
288.15	0.0502	1.3932
288.15	0.1000	1.3924
288.15	0.1500	1.3916
288.15	0.2000	1.3908
288.15	0.2500	1.39
288.15	0.3000	1.3891
288.15	0.3500	1.3881
288.15	0.4000	1.3871
288.15	0.4500	1.386
288.15	0.5000	1.3848
288.15	0.5500	1.3835
288.15	0.6000	1.3821
288.15	0.6500	1.3805
288.15	0.7000	1.3788
288.15	0.7500	1.3769
288.15	0.8000	1.3748
288.15	0.8500	1.3725
288.15	0.9000	1.3698
288.15	0.9500	1.3668
288.15	1.0000	1.3634
298.15	0.0000	1.389
298.15	0.0502	1.3881
298.15	0.1000	1.3873
298.15	0.1500	1.3865
298.15	0.2000	1.3857
298.15	0.2500	1.3848
298.15	0.3000	1.384
298.15	0.3500	1.383
298.15	0.4000	1.382
298.15	0.4500	1.381
298.15	0.5000	1.3798
298.15	0.5500	1.3786
298.15	0.6000	1.3772
298.15	0.6500	1.3757
298.15	0.7000	1.3741
298.15	0.7500	1.3722
298.15	0.8000	1.3702
298.15	0.8500	1.3679
298.15	0.9000	1.3654
298.15	0.9500	1.3625
298.15	1.0000	1.3592
308.15	0.0000	1.384
308.15	0.0502	1.383
308.15	0.1000	1.3822
308.15	0.1500	1.3814
308.15	0.2000	1.3806
308.15	0.2500	1.3797
308.15	0.3000	1.3788
308.15	0.3500	1.3779
308.15	0.4000	1.377
308.15	0.4500	1.3759
308.15	0.5000	1.3748
308.15	0.5500	1.3736
308.15	0.6000	1.3723
308.15	0.6500	1.3708
308.15	0.7000	1.3692
308.15	0.7500	1.3675
308.15	0.8000	1.3655
308.15	0.8500	1.3633
308.15	0.9000	1.3608
308.15	0.9500	1.3581
308.15	1.0000	1.355

Refractive index (Na D-line) [ref]

Operational condition: Pressure, kPa = 100.8 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol (1) - Liquid	Refractive index (Na D-line) - Liquid
298.15	0.0000	1.389
298.15	0.0500	1.3882
298.15	0.1000	1.3875
298.15	0.1500	1.3867
298.15	0.2000	1.3859
298.15	0.2500	1.385
298.15	0.3000	1.3841
298.15	0.3500	1.3831
298.15	0.4000	1.3821
298.15	0.4500	1.381
298.15	0.5000	1.3798
298.15	0.5500	1.3785
298.15	0.6000	1.3772
298.15	0.6500	1.3757
298.15	0.7000	1.374
298.15	0.7500	1.3722
298.15	0.8000	1.3702
298.15	0.8500	1.368
298.15	0.9000	1.3655
298.15	0.9500	1.3626
298.15	1.0000	1.3593
308.15	0.0000	1.384
308.15	0.0500	1.3833
308.15	0.1000	1.3825
308.15	0.1500	1.3817
308.15	0.2000	1.3809
308.15	0.2500	1.38
308.15	0.3000	1.3791
308.15	0.3500	1.3782
308.15	0.4000	1.3772
308.15	0.4500	1.3761
308.15	0.5000	1.375
308.15	0.5500	1.3737
308.15	0.6000	1.3724
308.15	0.6500	1.3709
308.15	0.7000	1.3693
308.15	0.7500	1.3676
308.15	0.8000	1.3656
308.15	0.8500	1.3635
308.15	0.9000	1.361
308.15	0.9500	1.3583
308.15	1.0000	1.3551
318.15	0.0000	1.379
318.15	0.0500	1.3781
318.15	0.1000	1.3774
318.15	0.1500	1.3766
318.15	0.2000	1.3758
318.15	0.2500	1.375
318.15	0.3000	1.3742
318.15	0.3500	1.3733
318.15	0.4000	1.3723
318.15	0.4500	1.3713
318.15	0.5000	1.3701
318.15	0.5500	1.3689
318.15	0.6000	1.3676
318.15	0.6500	1.3662
318.15	0.7000	1.3647
318.15	0.7500	1.363
318.15	0.8000	1.3611
318.15	0.8500	1.359
318.15	0.9000	1.3566
318.15	0.9500	1.354
318.15	1.0000	1.351

Refractive index (Na D-line) [ref]

Operational condition: Pressure, kPa = 100.8 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol (1) - Liquid	Refractive index (Na D-line) - Liquid
288.15	0.0000	1.394
288.15	0.0502	1.3932
288.15	0.1000	1.3924
288.15	0.1500	1.3916
288.15	0.2000	1.3908
288.15	0.2500	1.39
288.15	0.3000	1.3891
288.15	0.3500	1.3881
288.15	0.4000	1.3871
288.15	0.4500	1.386
288.15	0.5000	1.3848
288.15	0.5500	1.3835
288.15	0.6000	1.3821
288.15	0.6500	1.3805
288.15	0.7000	1.3788
288.15	0.7500	1.3769
288.15	0.8000	1.3748
288.15	0.8500	1.3725
288.15	0.9000	1.3698
288.15	0.9500	1.3668
288.15	1.0000	1.3634
298.15	0.0000	1.389
298.15	0.0502	1.3881
298.15	0.1000	1.3873
298.15	0.1500	1.3865
298.15	0.2000	1.3857
298.15	0.2500	1.3848
298.15	0.3000	1.384
298.15	0.3500	1.383
298.15	0.4000	1.382
298.15	0.4500	1.381
298.15	0.5000	1.3798
298.15	0.5500	1.3786
298.15	0.6000	1.3772
298.15	0.6500	1.3757
298.15	0.7000	1.3741
298.15	0.7500	1.3722
298.15	0.8000	1.3702
298.15	0.8500	1.3679
298.15	0.9000	1.3654
298.15	0.9500	1.3625
298.15	1.0000	1.3592
308.15	0.0000	1.384
308.15	0.0502	1.383
308.15	0.1000	1.3822
308.15	0.1500	1.3814
308.15	0.2000	1.3806
308.15	0.2500	1.3797
308.15	0.3000	1.3788
308.15	0.3500	1.3779
308.15	0.4000	1.377
308.15	0.4500	1.3759
308.15	0.5000	1.3748
308.15	0.5500	1.3736
308.15	0.6000	1.3723
308.15	0.6500	1.3708
308.15	0.7000	1.3692
308.15	0.7500	1.3675
308.15	0.8000	1.3655
308.15	0.8500	1.3633
308.15	0.9000	1.3608
308.15	0.9500	1.3581
308.15	1.0000	1.355

Refractive index (Na D-line) [ref]

Operational conditions:

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

Mole fraction of Ethanol (1) - Liquid	Refractive index (Na D-line) - Liquid
0.0000	1.3927
0.0520	1.3909
0.1002	1.39
0.1990	1.3885
0.2992	1.3868
0.3991	1.3846
0.5005	1.3823
0.6006	1.3795
0.7002	1.3761
0.8006	1.3721
0.8998	1.3673
0.9503	1.3644
1.0000	1.3616

Refractive index (Na D-line) [ref]

Operational conditions:

• Temperature, K = 303.15 (Liquid)
• Pressure, kPa = 101 (Liquid)

Mole fraction of Ethanol (1) - Liquid	Refractive index (Na D-line) - Liquid
0.0000	1.3865
0.0498	1.3863
0.0992	1.3863
0.1997	1.3848
0.2998	1.384
0.4005	1.3811
0.4990	1.3775
0.5999	1.3732
0.7000	1.3685
0.8001	1.3639
0.8999	1.3615
0.9508	1.3579
1.0000	1.3573

Refractive index (Na D-line) [ref]

Operational condition: Pressure, kPa = 100.8 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol (1) - Liquid	Refractive index (Na D-line) - Liquid
288.15	0.0000	1.394
288.15	0.0502	1.3932
288.15	0.1000	1.3924
288.15	0.1500	1.3916
288.15	0.2000	1.3908
288.15	0.2500	1.39
288.15	0.3000	1.3891
288.15	0.3500	1.3881
288.15	0.4000	1.3871
288.15	0.4500	1.386
288.15	0.5000	1.3848
288.15	0.5500	1.3835
288.15	0.6000	1.3821
288.15	0.6500	1.3805
288.15	0.7000	1.3788
288.15	0.7500	1.3769
288.15	0.8000	1.3748
288.15	0.8500	1.3725
288.15	0.9000	1.3698
288.15	0.9500	1.3668
288.15	1.0000	1.3634
298.15	0.0000	1.389
298.15	0.0502	1.3881
298.15	0.1000	1.3873
298.15	0.1500	1.3865
298.15	0.2000	1.3857
298.15	0.2500	1.3848
298.15	0.3000	1.384
298.15	0.3500	1.383
298.15	0.4000	1.382
298.15	0.4500	1.381
298.15	0.5000	1.3798
298.15	0.5500	1.3786
298.15	0.6000	1.3772
298.15	0.6500	1.3757
298.15	0.7000	1.3741
298.15	0.7500	1.3722
298.15	0.8000	1.3702
298.15	0.8500	1.3679
298.15	0.9000	1.3654
298.15	0.9500	1.3625
298.15	1.0000	1.3592
308.15	0.0000	1.384
308.15	0.0502	1.383
308.15	0.1000	1.3822
308.15	0.1500	1.3814
308.15	0.2000	1.3806
308.15	0.2500	1.3797
308.15	0.3000	1.3788
308.15	0.3500	1.3779
308.15	0.4000	1.377
308.15	0.4500	1.3759
308.15	0.5000	1.3748
308.15	0.5500	1.3736
308.15	0.6000	1.3723
308.15	0.6500	1.3708
308.15	0.7000	1.3692
308.15	0.7500	1.3675
308.15	0.8000	1.3655
308.15	0.8500	1.3633
308.15	0.9000	1.3608
308.15	0.9500	1.3581
308.15	1.0000	1.355

Refractive index (Na D-line) [ref]

Operational condition: Pressure, kPa = 100.8 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol (1) - Liquid	Refractive index (Na D-line) - Liquid
298.15	0.0000	1.389
298.15	0.0500	1.3882
298.15	0.1000	1.3875
298.15	0.1500	1.3867
298.15	0.2000	1.3859
298.15	0.2500	1.385
298.15	0.3000	1.3841
298.15	0.3500	1.3831
298.15	0.4000	1.3821
298.15	0.4500	1.381
298.15	0.5000	1.3798
298.15	0.5500	1.3785
298.15	0.6000	1.3772
298.15	0.6500	1.3757
298.15	0.7000	1.374
298.15	0.7500	1.3722
298.15	0.8000	1.3702
298.15	0.8500	1.368
298.15	0.9000	1.3655
298.15	0.9500	1.3626
298.15	1.0000	1.3593
308.15	0.0000	1.384
308.15	0.0500	1.3833
308.15	0.1000	1.3825
308.15	0.1500	1.3817
308.15	0.2000	1.3809
308.15	0.2500	1.38
308.15	0.3000	1.3791
308.15	0.3500	1.3782
308.15	0.4000	1.3772
308.15	0.4500	1.3761
308.15	0.5000	1.375
308.15	0.5500	1.3737
308.15	0.6000	1.3724
308.15	0.6500	1.3709
308.15	0.7000	1.3693
308.15	0.7500	1.3676
308.15	0.8000	1.3656
308.15	0.8500	1.3635
308.15	0.9000	1.361
308.15	0.9500	1.3583
308.15	1.0000	1.3551
318.15	0.0000	1.379
318.15	0.0500	1.3781
318.15	0.1000	1.3774
318.15	0.1500	1.3766
318.15	0.2000	1.3758
318.15	0.2500	1.375
318.15	0.3000	1.3742
318.15	0.3500	1.3733
318.15	0.4000	1.3723
318.15	0.4500	1.3713
318.15	0.5000	1.3701
318.15	0.5500	1.3689
318.15	0.6000	1.3676
318.15	0.6500	1.3662
318.15	0.7000	1.3647
318.15	0.7500	1.363
318.15	0.8000	1.3611
318.15	0.8500	1.359
318.15	0.9000	1.3566
318.15	0.9500	1.354
318.15	1.0000	1.351

Refractive index (Na D-line) [ref]

Operational condition: Pressure, kPa = 100.8 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol (1) - Liquid	Refractive index (Na D-line) - Liquid
288.15	0.0000	1.394
288.15	0.0502	1.3932
288.15	0.1000	1.3924
288.15	0.1500	1.3916
288.15	0.2000	1.3908
288.15	0.2500	1.39
288.15	0.3000	1.3891
288.15	0.3500	1.3881
288.15	0.4000	1.3871
288.15	0.4500	1.386
288.15	0.5000	1.3848
288.15	0.5500	1.3835
288.15	0.6000	1.3821
288.15	0.6500	1.3805
288.15	0.7000	1.3788
288.15	0.7500	1.3769
288.15	0.8000	1.3748
288.15	0.8500	1.3725
288.15	0.9000	1.3698
288.15	0.9500	1.3668
288.15	1.0000	1.3634
298.15	0.0000	1.389
298.15	0.0502	1.3881
298.15	0.1000	1.3873
298.15	0.1500	1.3865
298.15	0.2000	1.3857
298.15	0.2500	1.3848
298.15	0.3000	1.384
298.15	0.3500	1.383
298.15	0.4000	1.382
298.15	0.4500	1.381
298.15	0.5000	1.3798
298.15	0.5500	1.3786
298.15	0.6000	1.3772
298.15	0.6500	1.3757
298.15	0.7000	1.3741
298.15	0.7500	1.3722
298.15	0.8000	1.3702
298.15	0.8500	1.3679
298.15	0.9000	1.3654
298.15	0.9500	1.3625
298.15	1.0000	1.3592
308.15	0.0000	1.384
308.15	0.0502	1.383
308.15	0.1000	1.3822
308.15	0.1500	1.3814
308.15	0.2000	1.3806
308.15	0.2500	1.3797
308.15	0.3000	1.3788
308.15	0.3500	1.3779
308.15	0.4000	1.377
308.15	0.4500	1.3759
308.15	0.5000	1.3748
308.15	0.5500	1.3736
308.15	0.6000	1.3723
308.15	0.6500	1.3708
308.15	0.7000	1.3692
308.15	0.7500	1.3675
308.15	0.8000	1.3655
308.15	0.8500	1.3633
308.15	0.9000	1.3608
308.15	0.9500	1.3581
308.15	1.0000	1.355

Refractive index (Na D-line) [ref]

Operational conditions:

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

Mole fraction of Ethanol (1) - Liquid	Refractive index (Na D-line) - Liquid
0.0000	1.3927
0.0520	1.3909
0.1002	1.39
0.1990	1.3885
0.2992	1.3868
0.3991	1.3846
0.5005	1.3823
0.6006	1.3795
0.7002	1.3761
0.8006	1.3721
0.8998	1.3673
0.9503	1.3644
1.0000	1.3616

Refractive index (Na D-line) [ref]

Operational conditions:

• Temperature, K = 303.15 (Liquid)
• Pressure, kPa = 101 (Liquid)

Mole fraction of Ethanol (1) - Liquid	Refractive index (Na D-line) - Liquid
0.0000	1.3865
0.0498	1.3863
0.0992	1.3863
0.1997	1.3848
0.2998	1.384
0.4005	1.3811
0.4990	1.3775
0.5999	1.3732
0.7000	1.3685
0.8001	1.3639
0.8999	1.3615
0.9508	1.3579
1.0000	1.3573

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol (1) - Liquid	Mass density, kg/m3 - Liquid
298.15	0.0000	687.68
298.15	0.0599	689.06
298.15	0.0935	690.1
298.15	0.1677	692.68
298.15	0.2123	694.49
298.15	0.2640	696.79
298.15	0.3426	700.71
298.15	0.4109	704.63
298.15	0.4552	707.46
298.15	0.5063	711.05
298.15	0.5823	717.18
298.15	0.6240	720.98
298.15	0.6877	727.57
298.15	0.7388	733.65
298.15	0.8024	742.52
298.15	0.8669	753.52
298.15	0.9360	767.9
298.15	1.0000	785.07
308.15	0.0000	679.45
308.15	0.0599	680.66
308.15	0.0935	681.65
308.15	0.1677	684.16
308.15	0.2123	685.94
308.15	0.2640	688.2
308.15	0.3426	692.08
308.15	0.4109	695.98
308.15	0.4552	698.8
308.15	0.5063	702.37
308.15	0.5823	708.49
308.15	0.6240	712.29
308.15	0.6877	718.88
308.15	0.7388	724.97
308.15	0.8024	733.85
308.15	0.8669	744.87
308.15	0.9360	759.28
308.15	1.0000	776.46
318.15	0.0000	671.31
318.15	0.0599	672.3
318.15	0.0935	673.24
318.15	0.1677	675.66
318.15	0.2123	677.39
318.15	0.2640	679.61
318.15	0.3426	683.43
318.15	0.4109	687.3
318.15	0.4552	690.1
318.15	0.5063	693.66
318.15	0.5823	699.76
318.15	0.6240	703.56
318.15	0.6877	710.16
318.15	0.7388	716.25
318.15	0.8024	725.15
318.15	0.8669	736.19
318.15	0.9360	750.63
318.15	1.0000	767.83
328.15	0.0000	663.2
328.15	0.0599	663.93
328.15	0.0935	664.79
328.15	0.1677	667.1
328.15	0.2123	668.78
328.15	0.2640	670.94
328.15	0.3426	674.71
328.15	0.4109	678.52
328.15	0.4552	681.27
328.15	0.5063	684.83
328.15	0.5823	690.91
328.15	0.6240	694.71
328.15	0.6877	701.3
328.15	0.7388	707.4
328.15	0.8024	716.32
328.15	0.8669	727.39
328.15	0.9360	741.86
328.15	1.0000	759.11

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 100.8 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol (1) - Liquid	Mass density, kg/m3 - Liquid
298.15	0.0000	687.8
298.15	0.0500	688.8
298.15	0.1000	690.3
298.15	0.1500	692.1
298.15	0.2000	694.0
298.15	0.2500	696.2
298.15	0.3000	698.5
298.15	0.3500	701.1
298.15	0.4000	704.0
298.15	0.4500	707.1
298.15	0.5000	710.6
298.15	0.5500	714.5
298.15	0.6000	718.8
298.15	0.6500	723.6
298.15	0.7000	729.1
298.15	0.7500	735.4
298.15	0.8000	742.3
298.15	0.8500	750.5
298.15	0.9000	760.1
298.15	0.9500	771.5
298.15	1.0000	785.1
308.15	0.0000	679.5
308.15	0.0500	680.4
308.15	0.1000	681.8
308.15	0.1500	683.5
308.15	0.2000	685.4
308.15	0.2500	687.5
308.15	0.3000	689.8
308.15	0.3500	692.4
308.15	0.4000	695.2
308.15	0.4500	698.3
308.15	0.5000	701.8
308.15	0.5500	705.7
308.15	0.6000	710.0
308.15	0.6500	714.9
308.15	0.7000	720.3
308.15	0.7500	726.6
308.15	0.8000	733.6
308.15	0.8500	741.7
308.15	0.9000	751.4
308.15	0.9500	762.8
308.15	1.0000	776.5
318.15	0.0000	671.0
318.15	0.0500	671.7
318.15	0.1000	673.0
318.15	0.1500	674.7
318.15	0.2000	676.5
318.15	0.2500	678.6
318.15	0.3000	680.9
318.15	0.3500	683.4
318.15	0.4000	686.2
318.15	0.4500	689.3
318.15	0.5000	692.8
318.15	0.5500	696.6
318.15	0.6000	700.9
318.15	0.6500	705.8
318.15	0.7000	711.3
318.15	0.7500	717.6
318.15	0.8000	724.7
318.15	0.8500	732.9
318.15	0.9000	742.5
318.15	0.9500	753.9
318.15	1.0000	767.7

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 100.8 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol (1) - Liquid	Mass density, kg/m3 - Liquid
288.15	0.0000	695.95
288.15	0.0502	697.2
288.15	0.1000	698.76
288.15	0.1500	700.55
288.15	0.2000	702.53
288.15	0.2500	704.71
288.15	0.3000	707.1
288.15	0.3500	709.71
288.15	0.4000	712.6
288.15	0.4500	715.8
288.15	0.5000	719.31
288.15	0.5500	723.22
288.15	0.6000	727.55
288.15	0.6500	732.37
288.15	0.7000	737.81
288.15	0.7500	743.99
288.15	0.8000	751.11
288.15	0.8500	759.27
288.15	0.9000	768.81
288.15	0.9500	780.26
288.15	1.0000	793.74
298.15	0.0000	687.74
298.15	0.0502	688.84
298.15	0.1000	690.33
298.15	0.1500	692.11
298.15	0.2000	694.07
298.15	0.2500	696.21
298.15	0.3000	698.57
298.15	0.3500	701.17
298.15	0.4000	704.03
298.15	0.4500	707.2
298.15	0.5000	710.68
298.15	0.5500	714.59
298.15	0.6000	718.9
298.15	0.6500	723.73
298.15	0.7000	729.14
298.15	0.7500	735.34
298.15	0.8000	742.37
298.15	0.8500	750.54
298.15	0.9000	760.17
298.15	0.9500	771.59
298.15	1.0000	785.17
308.15	0.0000	679.41
308.15	0.0502	680.36
308.15	0.1000	681.76
308.15	0.1500	683.52
308.15	0.2000	685.43
308.15	0.2500	687.56
308.15	0.3000	689.88
308.15	0.3500	692.45
308.15	0.4000	695.3
308.15	0.4500	698.44
308.15	0.5000	701.91
308.15	0.5500	705.8
308.15	0.6000	710.11
308.15	0.6500	714.93
308.15	0.7000	720.34
308.15	0.7500	726.54
308.15	0.8000	733.58
308.15	0.8500	741.75
308.15	0.9000	751.44
308.15	0.9500	762.84
308.15	1.0000	776.49

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 100.8 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol (1) - Liquid	Mass density, kg/m3 - Liquid
298.15	0.0000	687.89
298.15	0.0500	688.94
298.15	0.1000	690.43
298.15	0.1500	692.16
298.15	0.2000	694.08
298.15	0.2500	696.22
298.15	0.3000	698.58
298.15	0.3500	701.19
298.15	0.4000	704.04
298.15	0.4500	707.19
298.15	0.5000	710.69
298.15	0.5500	714.59
298.15	0.6000	718.95
298.15	0.6500	723.82
298.15	0.7000	729.34
298.15	0.7500	735.56
298.15	0.8000	742.67
298.15	0.8500	750.87
298.15	0.9000	760.47
298.15	0.9500	771.78
298.15	1.0000	785.1
308.15	0.0000	679.55
308.15	0.0500	680.44
308.15	0.1000	681.85
308.15	0.1500	683.55
308.15	0.2000	685.46
308.15	0.2500	687.59
308.15	0.3000	689.91
308.15	0.3500	692.48
308.15	0.4000	695.33
308.15	0.4500	698.47
308.15	0.5000	701.95
308.15	0.5500	705.81
308.15	0.6000	710.14
308.15	0.6500	714.99
308.15	0.7000	720.46
308.15	0.7500	726.64
308.15	0.8000	733.71
308.15	0.8500	741.88
308.15	0.9000	751.45
308.15	0.9500	762.83
308.15	1.0000	776.43
318.15	0.0000	671.1
318.15	0.0500	671.89
318.15	0.1000	673.2
318.15	0.1500	674.81
318.15	0.2000	676.67
318.15	0.2500	678.74
318.15	0.3000	681.05
318.15	0.3500	683.6
318.15	0.4000	686.41
318.15	0.4500	689.53
318.15	0.5000	693.0
318.15	0.5500	696.87
318.15	0.6000	701.18
318.15	0.6500	706.0
318.15	0.7000	711.43
318.15	0.7500	717.6
318.15	0.8000	724.66
318.15	0.8500	732.81
318.15	0.9000	742.33
318.15	0.9500	753.76
318.15	1.0000	767.61

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 100.8 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol (1) - Liquid	Mass density, kg/m3 - Liquid
288.15	0.0000	695.95
288.15	0.0502	697.2
288.15	0.1000	698.76
288.15	0.1500	700.55
288.15	0.2000	702.53
288.15	0.2500	704.71
288.15	0.3000	707.1
288.15	0.3500	709.71
288.15	0.4000	712.6
288.15	0.4500	715.8
288.15	0.5000	719.31
288.15	0.5500	723.22
288.15	0.6000	727.55
288.15	0.6500	732.37
288.15	0.7000	737.81
288.15	0.7500	743.99
288.15	0.8000	751.11
288.15	0.8500	759.27
288.15	0.9000	768.81
288.15	0.9500	780.26
288.15	1.0000	793.74
298.15	0.0000	687.74
298.15	0.0502	688.84
298.15	0.1000	690.33
298.15	0.1500	692.11
298.15	0.2000	694.07
298.15	0.2500	696.21
298.15	0.3000	698.57
298.15	0.3500	701.17
298.15	0.4000	704.03
298.15	0.4500	707.2
298.15	0.5000	710.68
298.15	0.5500	714.59
298.15	0.6000	718.9
298.15	0.6500	723.73
298.15	0.7000	729.14
298.15	0.7500	735.34
298.15	0.8000	742.37
298.15	0.8500	750.54
298.15	0.9000	760.17
298.15	0.9500	771.59
298.15	1.0000	785.17
308.15	0.0000	679.41
308.15	0.0502	680.36
308.15	0.1000	681.76
308.15	0.1500	683.52
308.15	0.2000	685.43
308.15	0.2500	687.56
308.15	0.3000	689.88
308.15	0.3500	692.45
308.15	0.4000	695.3
308.15	0.4500	698.44
308.15	0.5000	701.91
308.15	0.5500	705.8
308.15	0.6000	710.11
308.15	0.6500	714.93
308.15	0.7000	720.34
308.15	0.7500	726.54
308.15	0.8000	733.58
308.15	0.8500	741.75
308.15	0.9000	751.44
308.15	0.9500	762.84
308.15	1.0000	776.49

Mass density, kg/m3 [ref]

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Temperature, K = 293.15 (Liquid)

Mole fraction of Ethanol (1) - Liquid	Mass density, kg/m3 - Liquid
0.0520	693.45
0.1002	694.99
0.1990	698.69
0.2992	703.17
0.3991	708.52
0.5005	715.22
0.6006	723.37
0.7002	733.6
0.8006	746.91
0.8998	764.31
0.9503	775.79

Mass density, kg/m3 [ref]

Operational conditions:

• Temperature, K = 303.15 (Liquid)
• Pressure, kPa = 101 (Liquid)

Mole fraction of Ethanol (1) - Liquid	Mass density, kg/m3 - Liquid
0.0000	684.1
0.0610	685.45
0.1201	687.2
0.2363	691.81
0.3467	697.27
0.4530	703.74
0.5525	711.14
0.6502	720.18
0.7431	730.88
0.8322	744.05
0.9176	760.58
0.9599	770.78
1.0000	781.99

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol (1) - Liquid	Mass density, kg/m3 - Liquid
298.15	0.0000	687.68
298.15	0.0599	689.06
298.15	0.0935	690.1
298.15	0.1677	692.68
298.15	0.2123	694.49
298.15	0.2640	696.79
298.15	0.3426	700.71
298.15	0.4109	704.63
298.15	0.4552	707.46
298.15	0.5063	711.05
298.15	0.5823	717.18
298.15	0.6240	720.98
298.15	0.6877	727.57
298.15	0.7388	733.65
298.15	0.8024	742.52
298.15	0.8669	753.52
298.15	0.9360	767.9
298.15	1.0000	785.07
308.15	0.0000	679.45
308.15	0.0599	680.66
308.15	0.0935	681.65
308.15	0.1677	684.16
308.15	0.2123	685.94
308.15	0.2640	688.2
308.15	0.3426	692.08
308.15	0.4109	695.98
308.15	0.4552	698.8
308.15	0.5063	702.37
308.15	0.5823	708.49
308.15	0.6240	712.29
308.15	0.6877	718.88
308.15	0.7388	724.97
308.15	0.8024	733.85
308.15	0.8669	744.87
308.15	0.9360	759.28
308.15	1.0000	776.46
318.15	0.0000	671.31
318.15	0.0599	672.3
318.15	0.0935	673.24
318.15	0.1677	675.66
318.15	0.2123	677.39
318.15	0.2640	679.61
318.15	0.3426	683.43
318.15	0.4109	687.3
318.15	0.4552	690.1
318.15	0.5063	693.66
318.15	0.5823	699.76
318.15	0.6240	703.56
318.15	0.6877	710.16
318.15	0.7388	716.25
318.15	0.8024	725.15
318.15	0.8669	736.19
318.15	0.9360	750.63
318.15	1.0000	767.83
328.15	0.0000	663.2
328.15	0.0599	663.93
328.15	0.0935	664.79
328.15	0.1677	667.1
328.15	0.2123	668.78
328.15	0.2640	670.94
328.15	0.3426	674.71
328.15	0.4109	678.52
328.15	0.4552	681.27
328.15	0.5063	684.83
328.15	0.5823	690.91
328.15	0.6240	694.71
328.15	0.6877	701.3
328.15	0.7388	707.4
328.15	0.8024	716.32
328.15	0.8669	727.39
328.15	0.9360	741.86
328.15	1.0000	759.11

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 100.8 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol (1) - Liquid	Mass density, kg/m3 - Liquid
298.15	0.0000	687.8
298.15	0.0500	688.8
298.15	0.1000	690.3
298.15	0.1500	692.1
298.15	0.2000	694.0
298.15	0.2500	696.2
298.15	0.3000	698.5
298.15	0.3500	701.1
298.15	0.4000	704.0
298.15	0.4500	707.1
298.15	0.5000	710.6
298.15	0.5500	714.5
298.15	0.6000	718.8
298.15	0.6500	723.6
298.15	0.7000	729.1
298.15	0.7500	735.4
298.15	0.8000	742.3
298.15	0.8500	750.5
298.15	0.9000	760.1
298.15	0.9500	771.5
298.15	1.0000	785.1
308.15	0.0000	679.5
308.15	0.0500	680.4
308.15	0.1000	681.8
308.15	0.1500	683.5
308.15	0.2000	685.4
308.15	0.2500	687.5
308.15	0.3000	689.8
308.15	0.3500	692.4
308.15	0.4000	695.2
308.15	0.4500	698.3
308.15	0.5000	701.8
308.15	0.5500	705.7
308.15	0.6000	710.0
308.15	0.6500	714.9
308.15	0.7000	720.3
308.15	0.7500	726.6
308.15	0.8000	733.6
308.15	0.8500	741.7
308.15	0.9000	751.4
308.15	0.9500	762.8
308.15	1.0000	776.5
318.15	0.0000	671.0
318.15	0.0500	671.7
318.15	0.1000	673.0
318.15	0.1500	674.7
318.15	0.2000	676.5
318.15	0.2500	678.6
318.15	0.3000	680.9
318.15	0.3500	683.4
318.15	0.4000	686.2
318.15	0.4500	689.3
318.15	0.5000	692.8
318.15	0.5500	696.6
318.15	0.6000	700.9
318.15	0.6500	705.8
318.15	0.7000	711.3
318.15	0.7500	717.6
318.15	0.8000	724.7
318.15	0.8500	732.9
318.15	0.9000	742.5
318.15	0.9500	753.9
318.15	1.0000	767.7

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 100.8 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol (1) - Liquid	Mass density, kg/m3 - Liquid
288.15	0.0000	695.95
288.15	0.0502	697.2
288.15	0.1000	698.76
288.15	0.1500	700.55
288.15	0.2000	702.53
288.15	0.2500	704.71
288.15	0.3000	707.1
288.15	0.3500	709.71
288.15	0.4000	712.6
288.15	0.4500	715.8
288.15	0.5000	719.31
288.15	0.5500	723.22
288.15	0.6000	727.55
288.15	0.6500	732.37
288.15	0.7000	737.81
288.15	0.7500	743.99
288.15	0.8000	751.11
288.15	0.8500	759.27
288.15	0.9000	768.81
288.15	0.9500	780.26
288.15	1.0000	793.74
298.15	0.0000	687.74
298.15	0.0502	688.84
298.15	0.1000	690.33
298.15	0.1500	692.11
298.15	0.2000	694.07
298.15	0.2500	696.21
298.15	0.3000	698.57
298.15	0.3500	701.17
298.15	0.4000	704.03
298.15	0.4500	707.2
298.15	0.5000	710.68
298.15	0.5500	714.59
298.15	0.6000	718.9
298.15	0.6500	723.73
298.15	0.7000	729.14
298.15	0.7500	735.34
298.15	0.8000	742.37
298.15	0.8500	750.54
298.15	0.9000	760.17
298.15	0.9500	771.59
298.15	1.0000	785.17
308.15	0.0000	679.41
308.15	0.0502	680.36
308.15	0.1000	681.76
308.15	0.1500	683.52
308.15	0.2000	685.43
308.15	0.2500	687.56
308.15	0.3000	689.88
308.15	0.3500	692.45
308.15	0.4000	695.3
308.15	0.4500	698.44
308.15	0.5000	701.91
308.15	0.5500	705.8
308.15	0.6000	710.11
308.15	0.6500	714.93
308.15	0.7000	720.34
308.15	0.7500	726.54
308.15	0.8000	733.58
308.15	0.8500	741.75
308.15	0.9000	751.44
308.15	0.9500	762.84
308.15	1.0000	776.49

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 100.8 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol (1) - Liquid	Mass density, kg/m3 - Liquid
298.15	0.0000	687.89
298.15	0.0500	688.94
298.15	0.1000	690.43
298.15	0.1500	692.16
298.15	0.2000	694.08
298.15	0.2500	696.22
298.15	0.3000	698.58
298.15	0.3500	701.19
298.15	0.4000	704.04
298.15	0.4500	707.19
298.15	0.5000	710.69
298.15	0.5500	714.59
298.15	0.6000	718.95
298.15	0.6500	723.82
298.15	0.7000	729.34
298.15	0.7500	735.56
298.15	0.8000	742.67
298.15	0.8500	750.87
298.15	0.9000	760.47
298.15	0.9500	771.78
298.15	1.0000	785.1
308.15	0.0000	679.55
308.15	0.0500	680.44
308.15	0.1000	681.85
308.15	0.1500	683.55
308.15	0.2000	685.46
308.15	0.2500	687.59
308.15	0.3000	689.91
308.15	0.3500	692.48
308.15	0.4000	695.33
308.15	0.4500	698.47
308.15	0.5000	701.95
308.15	0.5500	705.81
308.15	0.6000	710.14
308.15	0.6500	714.99
308.15	0.7000	720.46
308.15	0.7500	726.64
308.15	0.8000	733.71
308.15	0.8500	741.88
308.15	0.9000	751.45
308.15	0.9500	762.83
308.15	1.0000	776.43
318.15	0.0000	671.1
318.15	0.0500	671.89
318.15	0.1000	673.2
318.15	0.1500	674.81
318.15	0.2000	676.67
318.15	0.2500	678.74
318.15	0.3000	681.05
318.15	0.3500	683.6
318.15	0.4000	686.41
318.15	0.4500	689.53
318.15	0.5000	693.0
318.15	0.5500	696.87
318.15	0.6000	701.18
318.15	0.6500	706.0
318.15	0.7000	711.43
318.15	0.7500	717.6
318.15	0.8000	724.66
318.15	0.8500	732.81
318.15	0.9000	742.33
318.15	0.9500	753.76
318.15	1.0000	767.61

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 100.8 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol (1) - Liquid	Mass density, kg/m3 - Liquid
288.15	0.0000	695.95
288.15	0.0502	697.2
288.15	0.1000	698.76
288.15	0.1500	700.55
288.15	0.2000	702.53
288.15	0.2500	704.71
288.15	0.3000	707.1
288.15	0.3500	709.71
288.15	0.4000	712.6
288.15	0.4500	715.8
288.15	0.5000	719.31
288.15	0.5500	723.22
288.15	0.6000	727.55
288.15	0.6500	732.37
288.15	0.7000	737.81
288.15	0.7500	743.99
288.15	0.8000	751.11
288.15	0.8500	759.27
288.15	0.9000	768.81
288.15	0.9500	780.26
288.15	1.0000	793.74
298.15	0.0000	687.74
298.15	0.0502	688.84
298.15	0.1000	690.33
298.15	0.1500	692.11
298.15	0.2000	694.07
298.15	0.2500	696.21
298.15	0.3000	698.57
298.15	0.3500	701.17
298.15	0.4000	704.03
298.15	0.4500	707.2
298.15	0.5000	710.68
298.15	0.5500	714.59
298.15	0.6000	718.9
298.15	0.6500	723.73
298.15	0.7000	729.14
298.15	0.7500	735.34
298.15	0.8000	742.37
298.15	0.8500	750.54
298.15	0.9000	760.17
298.15	0.9500	771.59
298.15	1.0000	785.17
308.15	0.0000	679.41
308.15	0.0502	680.36
308.15	0.1000	681.76
308.15	0.1500	683.52
308.15	0.2000	685.43
308.15	0.2500	687.56
308.15	0.3000	689.88
308.15	0.3500	692.45
308.15	0.4000	695.3
308.15	0.4500	698.44
308.15	0.5000	701.91
308.15	0.5500	705.8
308.15	0.6000	710.11
308.15	0.6500	714.93
308.15	0.7000	720.34
308.15	0.7500	726.54
308.15	0.8000	733.58
308.15	0.8500	741.75
308.15	0.9000	751.44
308.15	0.9500	762.84
308.15	1.0000	776.49

Mass density, kg/m3 [ref]

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Temperature, K = 293.15 (Liquid)

Mole fraction of Ethanol (1) - Liquid	Mass density, kg/m3 - Liquid
0.0520	693.45
0.1002	694.99
0.1990	698.69
0.2992	703.17
0.3991	708.52
0.5005	715.22
0.6006	723.37
0.7002	733.6
0.8006	746.91
0.8998	764.31
0.9503	775.79

Mass density, kg/m3 [ref]

Operational conditions:

• Temperature, K = 303.15 (Liquid)
• Pressure, kPa = 101 (Liquid)

Mole fraction of Ethanol (1) - Liquid	Mass density, kg/m3 - Liquid
0.0000	684.1
0.0610	685.45
0.1201	687.2
0.2363	691.81
0.3467	697.27
0.4530	703.74
0.5525	711.14
0.6502	720.18
0.7431	730.88
0.8322	744.05
0.9176	760.58
0.9599	770.78
1.0000	781.99

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol (1) - Liquid	Speed of sound, m/s - Liquid
298.15	0.0000	1082.7
298.15	0.0599	1078.3
298.15	0.0935	1077.4
298.15	0.1677	1076.3
298.15	0.2123	1075.8
298.15	0.2640	1075.8
298.15	0.3426	1076.5
298.15	0.4109	1077.5
298.15	0.4552	1078.6
298.15	0.5063	1080.1
298.15	0.5823	1083.1
298.15	0.6240	1085.2
298.15	0.6877	1089.3
298.15	0.7388	1093.5
298.15	0.8024	1100.2
298.15	0.8669	1109.9
298.15	0.9360	1123.9
298.15	1.0000	1143.2
308.15	0.0000	1041.1
308.15	0.0599	1036.5
308.15	0.0935	1035.5
308.15	0.1677	1034.3
308.15	0.2123	1033.9
308.15	0.2640	1034.0
308.15	0.3426	1034.8
308.15	0.4109	1036.2
308.15	0.4552	1037.5
308.15	0.5063	1039.3
308.15	0.5823	1042.9
308.15	0.6240	1045.4
308.15	0.6877	1050.1
308.15	0.7388	1054.9
308.15	0.8024	1062.6
308.15	0.8669	1073.3
308.15	0.9360	1088.7
308.15	1.0000	1109.5
318.15	0.0000	1000.0
318.15	0.0599	995.1
318.15	0.0935	994.0
318.15	0.1677	992.7
318.15	0.2123	992.4
318.15	0.2640	992.5
318.15	0.3426	993.6
318.15	0.4109	995.2
318.15	0.4552	996.7
318.15	0.5063	998.8
318.15	0.5823	1002.9
318.15	0.6240	1005.8
318.15	0.6877	1011.2
318.15	0.7388	1016.5
318.15	0.8024	1025.2
318.15	0.8669	1037.0
318.15	0.9360	1053.8
318.15	1.0000	1076.0
328.15	0.0000	959.4
328.15	0.0599	954.2
328.15	0.0935	952.9
328.15	0.1677	951.5
328.15	0.2123	951.2
328.15	0.2640	951.4
328.15	0.3426	952.5
328.15	0.4109	954.0
328.15	0.4552	956.0
328.15	0.5063	958.4
328.15	0.5823	963.0
328.15	0.6240	966.2
328.15	0.6877	972.4
328.15	0.7388	978.3
328.15	0.8024	987.9
328.15	0.8669	1000.7
328.15	0.9360	1018.9
328.15	1.0000	1042.7

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol (1) - Liquid	Speed of sound, m/s - Liquid
298.15	0.0000	1082.7
298.15	0.0599	1078.3
298.15	0.0935	1077.4
298.15	0.1677	1076.3
298.15	0.2123	1075.8
298.15	0.2640	1075.8
298.15	0.3426	1076.5
298.15	0.4109	1077.5
298.15	0.4552	1078.6
298.15	0.5063	1080.1
298.15	0.5823	1083.1
298.15	0.6240	1085.2
298.15	0.6877	1089.3
298.15	0.7388	1093.5
298.15	0.8024	1100.2
298.15	0.8669	1109.9
298.15	0.9360	1123.9
298.15	1.0000	1143.2
308.15	0.0000	1041.1
308.15	0.0599	1036.5
308.15	0.0935	1035.5
308.15	0.1677	1034.3
308.15	0.2123	1033.9
308.15	0.2640	1034.0
308.15	0.3426	1034.8
308.15	0.4109	1036.2
308.15	0.4552	1037.5
308.15	0.5063	1039.3
308.15	0.5823	1042.9
308.15	0.6240	1045.4
308.15	0.6877	1050.1
308.15	0.7388	1054.9
308.15	0.8024	1062.6
308.15	0.8669	1073.3
308.15	0.9360	1088.7
308.15	1.0000	1109.5
318.15	0.0000	1000.0
318.15	0.0599	995.1
318.15	0.0935	994.0
318.15	0.1677	992.7
318.15	0.2123	992.4
318.15	0.2640	992.5
318.15	0.3426	993.6
318.15	0.4109	995.2
318.15	0.4552	996.7
318.15	0.5063	998.8
318.15	0.5823	1002.9
318.15	0.6240	1005.8
318.15	0.6877	1011.2
318.15	0.7388	1016.5
318.15	0.8024	1025.2
318.15	0.8669	1037.0
318.15	0.9360	1053.8
318.15	1.0000	1076.0
328.15	0.0000	959.4
328.15	0.0599	954.2
328.15	0.0935	952.9
328.15	0.1677	951.5
328.15	0.2123	951.2
328.15	0.2640	951.4
328.15	0.3426	952.5
328.15	0.4109	954.0
328.15	0.4552	956.0
328.15	0.5063	958.4
328.15	0.5823	963.0
328.15	0.6240	966.2
328.15	0.6877	972.4
328.15	0.7388	978.3
328.15	0.8024	987.9
328.15	0.8669	1000.7
328.15	0.9360	1018.9
328.15	1.0000	1042.7

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

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Pentane, 2,2,4-trimethyl- (2) - Liquid	Surface tension liquid-gas, N/m - Liquid
288.15	1.0000	0.0191
288.15	0.7840	0.0195
288.15	0.6173	0.0198
288.15	0.4848	0.0200
288.15	0.3769	0.0204
288.15	0.2874	0.0207
288.15	0.2119	0.0211
288.15	0.1474	0.0215
288.15	0.0916	0.0219
288.15	0.0429	0.0223
288.15	0.0000	0.0227
298.15	1.0000	0.0183
298.15	0.7840	0.0186
298.15	0.6173	0.0188
298.15	0.4848	0.0191
298.15	0.3769	0.0195
298.15	0.2874	0.0198
298.15	0.2119	0.0202
298.15	0.1474	0.0205
298.15	0.0916	0.0210
298.15	0.0429	0.0214
298.15	0.0000	0.0219
308.15	1.0000	0.0174
308.15	0.7840	0.0177
308.15	0.6173	0.0179
308.15	0.4848	0.0182
308.15	0.3769	0.0186
308.15	0.2874	0.0189
308.15	0.2119	0.0193
308.15	0.1474	0.0197
308.15	0.0916	0.0201
308.15	0.0429	0.0205
308.15	0.0000	0.0210
318.15	1.0000	0.0166
318.15	0.7840	0.0169
318.15	0.6173	0.0170
318.15	0.4848	0.0173
318.15	0.3769	0.0177
318.15	0.2874	0.0181
318.15	0.2119	0.0185
318.15	0.1474	0.0188
318.15	0.0916	0.0193
318.15	0.0429	0.0198
318.15	0.0000	0.0203

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

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Pentane, 2,2,4-trimethyl- (2) - Liquid	Surface tension liquid-gas, N/m - Liquid
288.15	1.0000	0.0191
288.15	0.7840	0.0195
288.15	0.6173	0.0198
288.15	0.4848	0.0200
288.15	0.3769	0.0204
288.15	0.2874	0.0207
288.15	0.2119	0.0211
288.15	0.1474	0.0215
288.15	0.0916	0.0219
288.15	0.0429	0.0223
288.15	0.0000	0.0227
298.15	1.0000	0.0183
298.15	0.7840	0.0186
298.15	0.6173	0.0188
298.15	0.4848	0.0191
298.15	0.3769	0.0195
298.15	0.2874	0.0198
298.15	0.2119	0.0202
298.15	0.1474	0.0205
298.15	0.0916	0.0210
298.15	0.0429	0.0214
298.15	0.0000	0.0219
308.15	1.0000	0.0174
308.15	0.7840	0.0177
308.15	0.6173	0.0179
308.15	0.4848	0.0182
308.15	0.3769	0.0186
308.15	0.2874	0.0189
308.15	0.2119	0.0193
308.15	0.1474	0.0197
308.15	0.0916	0.0201
308.15	0.0429	0.0205
308.15	0.0000	0.0210
318.15	1.0000	0.0166
318.15	0.7840	0.0169
318.15	0.6173	0.0170
318.15	0.4848	0.0173
318.15	0.3769	0.0177
318.15	0.2874	0.0181
318.15	0.2119	0.0185
318.15	0.1474	0.0188
318.15	0.0916	0.0193
318.15	0.0429	0.0198
318.15	0.0000	0.0203

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.32 (Liquid)

Mole fraction of Ethanol (1) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	372.33
0.0240	362.55
0.0570	353.82
0.0970	348.56
0.1370	346.51
0.2090	345.84
0.2730	345.70
0.3330	345.33
0.4000	344.90
0.4440	344.74
0.5020	344.53
0.5450	344.52
0.5970	344.47
0.6520	344.44
0.7050	344.48
0.7540	344.58
0.8070	344.71
0.8600	345.22
0.9060	346.22
0.9540	348.35
1.0000	351.44

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Ethanol (1) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	372.33
0.0280	361.27
0.0580	353.92
0.0880	349.19
0.1440	346.02
0.2730	345.50
0.3070	345.34
0.3330	345.22
0.4000	344.90
0.4460	344.85
0.5020	344.63
0.5450	344.53
0.5970	344.48
0.6520	344.44
0.7050	344.48
0.7650	344.61
0.8000	344.82
0.8600	345.32
0.9020	346.16
0.9580	348.57
1.0000	351.44

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 95.8 (Liquid)

Mole fraction of Ethanol (1) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	370.55
0.1186	352.55
0.2876	346.55
0.4468	344.55
0.6079	344.05
0.7502	343.95
0.9087	344.65
1.0000	350.05

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Ethanol (1) - Liquid	Boiling temperature at pressure P, K - Liquid
1.0000	351.44
0.9960	351.17
0.9840	350.63
0.9820	350.03
0.9660	349.29
0.9660	349.17
0.9570	348.16
0.9350	346.77
0.8640	345.54
0.6740	344.84
0.6180	344.58
0.5910	344.53
0.5640	344.48
0.5320	344.42
0.4940	344.40
0.4620	344.33
0.4190	344.37
0.3530	344.35
0.2550	344.49
0.2510	344.73
0.1840	346.37
0.0381	355.43
0.0000	372.26

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Ethanol (1) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	372.35
0.1406	346.48
0.1456	346.48
0.1698	346.35
0.1914	345.65
0.2058	345.65
0.2203	345.65
0.2398	345.05
0.2451	345.00
0.2659	345.00
0.2922	344.95
0.2930	344.94
0.2962	344.79
0.6299	344.57
0.6337	344.57
0.7999	344.62
0.8078	344.62
0.8161	344.60
0.9377	346.75
0.9412	346.80
0.9494	347.42
0.9544	347.55
0.9575	347.65
1.0000	351.47

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.32 (Liquid)

Mole fraction of Ethanol (1) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	372.33
0.0240	362.55
0.0570	353.82
0.0970	348.56
0.1370	346.51
0.2090	345.84
0.2730	345.70
0.3330	345.33
0.4000	344.90
0.4440	344.74
0.5020	344.53
0.5450	344.52
0.5970	344.47
0.6520	344.44
0.7050	344.48
0.7540	344.58
0.8070	344.71
0.8600	345.22
0.9060	346.22
0.9540	348.35
1.0000	351.44

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Ethanol (1) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	372.33
0.0280	361.27
0.0580	353.92
0.0880	349.19
0.1440	346.02
0.2730	345.50
0.3070	345.34
0.3330	345.22
0.4000	344.90
0.4460	344.85
0.5020	344.63
0.5450	344.53
0.5970	344.48
0.6520	344.44
0.7050	344.48
0.7650	344.61
0.8000	344.82
0.8600	345.32
0.9020	346.16
0.9580	348.57
1.0000	351.44

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 95.8 (Liquid)

Mole fraction of Ethanol (1) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	370.55
0.1186	352.55
0.2876	346.55
0.4468	344.55
0.6079	344.05
0.7502	343.95
0.9087	344.65
1.0000	350.05

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Ethanol (1) - Liquid	Boiling temperature at pressure P, K - Liquid
1.0000	351.44
0.9960	351.17
0.9840	350.63
0.9820	350.03
0.9660	349.29
0.9660	349.17
0.9570	348.16
0.9350	346.77
0.8640	345.54
0.6740	344.84
0.6180	344.58
0.5910	344.53
0.5640	344.48
0.5320	344.42
0.4940	344.40
0.4620	344.33
0.4190	344.37
0.3530	344.35
0.2550	344.49
0.2510	344.73
0.1840	346.37
0.0381	355.43
0.0000	372.26

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Ethanol (1) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	372.35
0.1406	346.48
0.1456	346.48
0.1698	346.35
0.1914	345.65
0.2058	345.65
0.2203	345.65
0.2398	345.05
0.2451	345.00
0.2659	345.00
0.2922	344.95
0.2930	344.94
0.2962	344.79
0.6299	344.57
0.6337	344.57
0.7999	344.62
0.8078	344.62
0.8161	344.60
0.9377	346.75
0.9412	346.80
0.9494	347.42
0.9544	347.55
0.9575	347.65
1.0000	351.47

Azeotropic temperature, K [ref]

Pressure, kPa - Liquid	Azeotropic temperature, K - Liquid
101.30	344.43

Azeotropic temperature, K [ref]

Pressure, kPa - Liquid	Azeotropic temperature, K - Liquid
101.30	344.43

Sources

• Isobaric vapor liquid equilibria for mixtures of acetone, ethanol, and 2,2,4-trimethylpentane at 101.3 kPa
• Vapor liquid equilibria for binary and ternary mixtures of ethanol, 2-butanone, and 2,2,4-trimethylpentane at 101.3 kPa
• Isothermal vapor liquid equilibrium at 333.15K and excess molar volumes and refractive indices at 298.15K for the mixtures of di-methyl carbonate, ethanol and 2,2,4-trimethylpentane
• (Vapor + liquid) equilibria of binary mixtures formed by iso-octane with a variety of compounds at 95.8 kPa
• Volumetric behaviour of binary and ternary liquid systems composed of ethanol, isooctane, and toluene at temperatures from (298.15 to 328.15) K. Experimental data and correlation
• Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane +1-Alkanols from 298.15 to 323.15 K
• Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
• Densities and Viscosities for Binary and Ternary Mixtures of Ethanol, 2-Butanone, and 2,2,4-Trimethylpentane at T = (298.15, 308.15, and 318.15) K
• Densities, Refractive indices and Viscosities for Binary and Ternary Mixtures of Acetone, Ethanol and 2,2,4-Trimethylpentane at T = (288.15, 298.15, and 308.15) K
• Densities, Viscosities, and Refractive Indices for Binary and Ternary Mixtures of Ethanol, 2-Methylpropan-2-ol, and 2,2,4-Trimethylpentane
• Densities, Viscosities, and Refractive Indices for Binary and Ternary Mixtures of Diisopropyl Ether, Ethanol, and 2,2,4-Trimethylpentane
• Vapor-Liquid Equilibrium of Binary Mixtures. 2. Ethanol + 2,2,4-Trimethylpentane, 1-Butanol + 2,2,4-Trimethylpentane, and Ethanol + o-Xylene
• Vapor Liquid Liquid Equilibria Measurements for the Dehydration of Ethanol, Isopropanol, and n-Propanol via Azeotropic Distillation Using DIPE and Isooctane as Entrainers
• Isothermal Binary and Ternary VLE for the Mixtures of Propyl Vinyl Ether + Ethanol + Isooctane at 323.15 K and VE at 293.15 K
• Binary LLE for Propyl Vinyl Ether (PVE) + Water, Ternary LLE for PVE + Methanol or Ethanol + Water at 298.15 K, and VE and centsR at 293.15 K for the Mixture of PVE + Ethanol + 2,2,4-Trimethylpentane
• Liquid Liquid Equilibrium for Ternary Systems of Propyl Vinyl Ether + C3 or C4 Alcohols + Water at 298.15 K and Excess Molar Enthalpies for Ternary and Constituent Binary Systems of Propyl Vinyl Ether + Ethanol + Isooctane at 303.15 K
• Isothermal Vapor-Liquid Equilibrium at 333.15 K and Excess Molar Volumes, Refractive Indices, and Excess Molar Enthalpies at 303.15 K for the Binary and Ternary Mixtures of Di-isopropyl Ether, Ethanol, and 2,2,4-Trimethylpentane