Mixture of Benzene, 1,3-dimethyl- + 1,4-Dioxane

Datasets

1. η - Viscosity, Pa*s (2)
2. Excess molar enthalpy (molar enthalpy (2)
3. n₀ - Refractive index (Na D-line) (2)
4. ρ_l - Mass density, kg/m3 (2)
5. c_sound,fluid - Speed of Sound, m/s (2)

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1,4-Dioxane (2) - Liquid	Viscosity, Pa*s - Liquid
293.15	0.0000	0.0006
293.15	0.0938	0.0007
293.15	0.1532	0.0007
293.15	0.2046	0.0007
293.15	0.2698	0.0008
293.15	0.3374	0.0008
293.15	0.4002	0.0009
293.15	0.4714	0.0009
293.15	0.5487	0.0010
293.15	0.6300	0.0010
293.15	0.7182	0.0011
293.15	0.8035	0.0012
293.15	0.8708	0.0012
293.15	0.9324	0.0013
293.15	1.0000	0.0013
298.15	0.0000	0.0006
298.15	0.0938	0.0006
298.15	0.1532	0.0007
298.15	0.2046	0.0007
298.15	0.2698	0.0007
298.15	0.3374	0.0008
298.15	0.4002	0.0008
298.15	0.4714	0.0008
298.15	0.5487	0.0009
298.15	0.6300	0.0009
298.15	0.7182	0.0010
298.15	0.8035	0.0011
298.15	0.8708	0.0011
298.15	0.9324	0.0011
298.15	1.0000	0.0012
303.15	0.0000	0.0006
303.15	0.0938	0.0006
303.15	0.1532	0.0006
303.15	0.2046	0.0006
303.15	0.2698	0.0007
303.15	0.3374	0.0007
303.15	0.4002	0.0007
303.15	0.4714	0.0008
303.15	0.5487	0.0008
303.15	0.6300	0.0009
303.15	0.7182	0.0009
303.15	0.8035	0.0010
303.15	0.8708	0.0010
303.15	0.9324	0.0011
303.15	1.0000	0.0011
308.15	0.0000	0.0005
308.15	0.0938	0.0006
308.15	0.1532	0.0006
308.15	0.2046	0.0006
308.15	0.2698	0.0006
308.15	0.3374	0.0007
308.15	0.4002	0.0007
308.15	0.4714	0.0007
308.15	0.5487	0.0008
308.15	0.6300	0.0008
308.15	0.7182	0.0009
308.15	0.8035	0.0009
308.15	0.8708	0.0009
308.15	0.9324	0.0010
308.15	1.0000	0.0010
313.15	0.0000	0.0005
313.15	0.0938	0.0005
313.15	0.1532	0.0006
313.15	0.2046	0.0006
313.15	0.2698	0.0006
313.15	0.3374	0.0006
313.15	0.4002	0.0007
313.15	0.4714	0.0007
313.15	0.5487	0.0007
313.15	0.6300	0.0008
313.15	0.7182	0.0008
313.15	0.8035	0.0008
313.15	0.8708	0.0009
313.15	0.9324	0.0009
313.15	1.0000	0.0009
318.15	0.0000	0.0005
318.15	0.0938	0.0005
318.15	0.1532	0.0005
318.15	0.2046	0.0005
318.15	0.2698	0.0006
318.15	0.3374	0.0006
318.15	0.4002	0.0006
318.15	0.4714	0.0006
318.15	0.5487	0.0007
318.15	0.6300	0.0007
318.15	0.7182	0.0008
318.15	0.8035	0.0008
318.15	0.8708	0.0008
318.15	0.9324	0.0009
318.15	1.0000	0.0009

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1,4-Dioxane (2) - Liquid	Viscosity, Pa*s - Liquid
293.15	0.0000	0.0006
293.15	0.0938	0.0007
293.15	0.1532	0.0007
293.15	0.2046	0.0007
293.15	0.2698	0.0008
293.15	0.3374	0.0008
293.15	0.4002	0.0009
293.15	0.4714	0.0009
293.15	0.5487	0.0010
293.15	0.6300	0.0010
293.15	0.7182	0.0011
293.15	0.8035	0.0012
293.15	0.8708	0.0012
293.15	0.9324	0.0013
293.15	1.0000	0.0013
298.15	0.0000	0.0006
298.15	0.0938	0.0006
298.15	0.1532	0.0007
298.15	0.2046	0.0007
298.15	0.2698	0.0007
298.15	0.3374	0.0008
298.15	0.4002	0.0008
298.15	0.4714	0.0008
298.15	0.5487	0.0009
298.15	0.6300	0.0009
298.15	0.7182	0.0010
298.15	0.8035	0.0011
298.15	0.8708	0.0011
298.15	0.9324	0.0011
298.15	1.0000	0.0012
303.15	0.0000	0.0006
303.15	0.0938	0.0006
303.15	0.1532	0.0006
303.15	0.2046	0.0006
303.15	0.2698	0.0007
303.15	0.3374	0.0007
303.15	0.4002	0.0007
303.15	0.4714	0.0008
303.15	0.5487	0.0008
303.15	0.6300	0.0009
303.15	0.7182	0.0009
303.15	0.8035	0.0010
303.15	0.8708	0.0010
303.15	0.9324	0.0011
303.15	1.0000	0.0011
308.15	0.0000	0.0005
308.15	0.0938	0.0006
308.15	0.1532	0.0006
308.15	0.2046	0.0006
308.15	0.2698	0.0006
308.15	0.3374	0.0007
308.15	0.4002	0.0007
308.15	0.4714	0.0007
308.15	0.5487	0.0008
308.15	0.6300	0.0008
308.15	0.7182	0.0009
308.15	0.8035	0.0009
308.15	0.8708	0.0009
308.15	0.9324	0.0010
308.15	1.0000	0.0010
313.15	0.0000	0.0005
313.15	0.0938	0.0005
313.15	0.1532	0.0006
313.15	0.2046	0.0006
313.15	0.2698	0.0006
313.15	0.3374	0.0006
313.15	0.4002	0.0007
313.15	0.4714	0.0007
313.15	0.5487	0.0007
313.15	0.6300	0.0008
313.15	0.7182	0.0008
313.15	0.8035	0.0008
313.15	0.8708	0.0009
313.15	0.9324	0.0009
313.15	1.0000	0.0009
318.15	0.0000	0.0005
318.15	0.0938	0.0005
318.15	0.1532	0.0005
318.15	0.2046	0.0005
318.15	0.2698	0.0006
318.15	0.3374	0.0006
318.15	0.4002	0.0006
318.15	0.4714	0.0006
318.15	0.5487	0.0007
318.15	0.6300	0.0007
318.15	0.7182	0.0008
318.15	0.8035	0.0008
318.15	0.8708	0.0008
318.15	0.9324	0.0009
318.15	1.0000	0.0009

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

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Temperature, K = 308.15 (Liquid)

Mole fraction of 1,4-Dioxane (2) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0638	0.0623
0.1239	0.1208
0.1845	0.1797
0.2230	0.2074
0.2742	0.2481
0.3357	0.2823
0.4212	0.3175
0.4781	0.3331
0.5516	0.3334
0.6212	0.3131
0.6836	0.2876
0.7583	0.2409
0.7797	0.2236
0.8183	0.1955
0.8884	0.1246
0.9481	0.0603

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

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Temperature, K = 308.15 (Liquid)

Mole fraction of 1,4-Dioxane (2) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0638	0.0623
0.1239	0.1208
0.1845	0.1797
0.2230	0.2074
0.2742	0.2481
0.3357	0.2823
0.4212	0.3175
0.4781	0.3331
0.5516	0.3334
0.6212	0.3131
0.6836	0.2876
0.7583	0.2409
0.7797	0.2236
0.8183	0.1955
0.8884	0.1246
0.9481	0.0603

Refractive index (Na D-line) [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1,4-Dioxane (2) - Liquid	Refractive index (Na D-line) - Liquid
288.15	0.0000	1.4999
288.15	0.0938	1.4933
288.15	0.1532	1.489
288.15	0.2046	1.4852
288.15	0.2698	1.4805
288.15	0.3374	1.4755
288.15	0.4002	1.4709
288.15	0.4714	1.4656
288.15	0.5487	1.4598
288.15	0.6300	1.4536
288.15	0.7182	1.4468
288.15	0.8035	1.4401
288.15	0.8708	1.4348
288.15	0.9324	1.4299
288.15	1.0000	1.4245
293.15	0.0000	1.4974
293.15	0.0938	1.4907
293.15	0.1532	1.4864
293.15	0.2046	1.4826
293.15	0.2698	1.4779
293.15	0.3374	1.473
293.15	0.4002	1.4684
293.15	0.4714	1.4631
293.15	0.5487	1.4574
293.15	0.6300	1.4512
293.15	0.7182	1.4444
293.15	0.8035	1.4378
293.15	0.8708	1.4325
293.15	0.9324	1.4277
293.15	1.0000	1.4224
298.15	0.0000	1.4948
298.15	0.0938	1.488
298.15	0.1532	1.4837
298.15	0.2046	1.4799
298.15	0.2698	1.4753
298.15	0.3374	1.4704
298.15	0.4002	1.4658
298.15	0.4714	1.4606
298.15	0.5487	1.4549
298.15	0.6300	1.4487
298.15	0.7182	1.442
298.15	0.8035	1.4354
298.15	0.8708	1.4302
298.15	0.9324	1.4255
298.15	1.0000	1.4203
303.15	0.0000	1.4922
303.15	0.0938	1.4853
303.15	0.1532	1.4811
303.15	0.2046	1.4772
303.15	0.2698	1.4726
303.15	0.3374	1.4677
303.15	0.4002	1.4632
303.15	0.4714	1.458
303.15	0.5487	1.4524
303.15	0.6300	1.4462
303.15	0.7182	1.4395
303.15	0.8035	1.4329
303.15	0.8708	1.4279
303.15	0.9324	1.4232
303.15	1.0000	1.4182
308.15	0.0000	1.4896
308.15	0.0938	1.4826
308.15	0.1532	1.4783
308.15	0.2046	1.4745
308.15	0.2698	1.4699
308.15	0.3374	1.4651
308.15	0.4002	1.4606
308.15	0.4714	1.4555
308.15	0.5487	1.4498
308.15	0.6300	1.4437
308.15	0.7182	1.4371
308.15	0.8035	1.4305
308.15	0.8708	1.4255
308.15	0.9324	1.4209
308.15	1.0000	1.4161
313.15	0.0000	1.487
313.15	0.0938	1.4799
313.15	0.1532	1.4756
313.15	0.2046	1.4718
313.15	0.2698	1.4672
313.15	0.3374	1.4624
313.15	0.4002	1.458
313.15	0.4714	1.4529
313.15	0.5487	1.4473
313.15	0.6300	1.4412
313.15	0.7182	1.4346
313.15	0.8035	1.428
313.15	0.8708	1.4231
313.15	0.9324	1.4186
313.15	1.0000	1.4139
318.15	0.0000	1.4844
318.15	0.0938	1.4772
318.15	0.1532	1.4728
318.15	0.2046	1.4691
318.15	0.2698	1.4645
318.15	0.3374	1.4597
318.15	0.4002	1.4553
318.15	0.4714	1.4503
318.15	0.5487	1.4447
318.15	0.6300	1.4387
318.15	0.7182	1.4321
318.15	0.8035	1.4256
318.15	0.8708	1.4206
318.15	0.9324	1.4163
318.15	1.0000	1.4117

Refractive index (Na D-line) [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1,4-Dioxane (2) - Liquid	Refractive index (Na D-line) - Liquid
288.15	0.0000	1.4999
288.15	0.0938	1.4933
288.15	0.1532	1.489
288.15	0.2046	1.4852
288.15	0.2698	1.4805
288.15	0.3374	1.4755
288.15	0.4002	1.4709
288.15	0.4714	1.4656
288.15	0.5487	1.4598
288.15	0.6300	1.4536
288.15	0.7182	1.4468
288.15	0.8035	1.4401
288.15	0.8708	1.4348
288.15	0.9324	1.4299
288.15	1.0000	1.4245
293.15	0.0000	1.4974
293.15	0.0938	1.4907
293.15	0.1532	1.4864
293.15	0.2046	1.4826
293.15	0.2698	1.4779
293.15	0.3374	1.473
293.15	0.4002	1.4684
293.15	0.4714	1.4631
293.15	0.5487	1.4574
293.15	0.6300	1.4512
293.15	0.7182	1.4444
293.15	0.8035	1.4378
293.15	0.8708	1.4325
293.15	0.9324	1.4277
293.15	1.0000	1.4224
298.15	0.0000	1.4948
298.15	0.0938	1.488
298.15	0.1532	1.4837
298.15	0.2046	1.4799
298.15	0.2698	1.4753
298.15	0.3374	1.4704
298.15	0.4002	1.4658
298.15	0.4714	1.4606
298.15	0.5487	1.4549
298.15	0.6300	1.4487
298.15	0.7182	1.442
298.15	0.8035	1.4354
298.15	0.8708	1.4302
298.15	0.9324	1.4255
298.15	1.0000	1.4203
303.15	0.0000	1.4922
303.15	0.0938	1.4853
303.15	0.1532	1.4811
303.15	0.2046	1.4772
303.15	0.2698	1.4726
303.15	0.3374	1.4677
303.15	0.4002	1.4632
303.15	0.4714	1.458
303.15	0.5487	1.4524
303.15	0.6300	1.4462
303.15	0.7182	1.4395
303.15	0.8035	1.4329
303.15	0.8708	1.4279
303.15	0.9324	1.4232
303.15	1.0000	1.4182
308.15	0.0000	1.4896
308.15	0.0938	1.4826
308.15	0.1532	1.4783
308.15	0.2046	1.4745
308.15	0.2698	1.4699
308.15	0.3374	1.4651
308.15	0.4002	1.4606
308.15	0.4714	1.4555
308.15	0.5487	1.4498
308.15	0.6300	1.4437
308.15	0.7182	1.4371
308.15	0.8035	1.4305
308.15	0.8708	1.4255
308.15	0.9324	1.4209
308.15	1.0000	1.4161
313.15	0.0000	1.487
313.15	0.0938	1.4799
313.15	0.1532	1.4756
313.15	0.2046	1.4718
313.15	0.2698	1.4672
313.15	0.3374	1.4624
313.15	0.4002	1.458
313.15	0.4714	1.4529
313.15	0.5487	1.4473
313.15	0.6300	1.4412
313.15	0.7182	1.4346
313.15	0.8035	1.428
313.15	0.8708	1.4231
313.15	0.9324	1.4186
313.15	1.0000	1.4139
318.15	0.0000	1.4844
318.15	0.0938	1.4772
318.15	0.1532	1.4728
318.15	0.2046	1.4691
318.15	0.2698	1.4645
318.15	0.3374	1.4597
318.15	0.4002	1.4553
318.15	0.4714	1.4503
318.15	0.5487	1.4447
318.15	0.6300	1.4387
318.15	0.7182	1.4321
318.15	0.8035	1.4256
318.15	0.8708	1.4206
318.15	0.9324	1.4163
318.15	1.0000	1.4117

Mass density, kg/m3 [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1,4-Dioxane (2) - Liquid	Mass density, kg/m3 - Liquid
288.15	0.0000	868.59
288.15	0.0938	879.61
288.15	0.1532	886.95
288.15	0.2046	893.54
288.15	0.2698	902.26
288.15	0.3374	911.76
288.15	0.4002	921.05
288.15	0.4714	932.18
288.15	0.5487	945.0
288.15	0.6300	959.44
288.15	0.7182	976.23
288.15	0.8035	993.74
288.15	0.8708	1008.47
288.15	0.9324	1022.71
288.15	1.0000	1039.23
293.15	0.0000	864.31
293.15	0.0938	875.2
293.15	0.1532	882.46
293.15	0.2046	888.98
293.15	0.2698	897.62
293.15	0.3374	907.05
293.15	0.4002	916.26
293.15	0.4714	927.3
293.15	0.5487	940.02
293.15	0.6300	954.33
293.15	0.7182	970.98
293.15	0.8035	988.36
293.15	0.8708	1002.99
293.15	0.9324	1017.15
293.15	1.0000	1033.59
298.15	0.0000	860.02
298.15	0.0938	870.79
298.15	0.1532	877.97
298.15	0.2046	884.42
298.15	0.2698	892.98
298.15	0.3374	902.34
298.15	0.4002	911.47
298.15	0.4714	922.42
298.15	0.5487	935.04
298.15	0.6300	949.22
298.15	0.7182	965.73
298.15	0.8035	982.98
298.15	0.8708	997.51
298.15	0.9324	1011.59
298.15	1.0000	1027.95
303.15	0.0000	855.74
303.15	0.0938	866.38
303.15	0.1532	873.48
303.15	0.2046	879.87
303.15	0.2698	888.35
303.15	0.3374	897.63
303.15	0.4002	906.68
303.15	0.4714	917.55
303.15	0.5487	930.06
303.15	0.6300	944.11
303.15	0.7182	960.49
303.15	0.8035	977.6
303.15	0.8708	992.03
303.15	0.9324	1006.03
303.15	1.0000	1022.32
308.15	0.0000	851.45
308.15	0.0938	861.97
308.15	0.1532	868.99
308.15	0.2046	875.32
308.15	0.2698	883.72
308.15	0.3374	892.92
308.15	0.4002	901.9
308.15	0.4714	912.68
308.15	0.5487	925.08
308.15	0.6300	939.01
308.15	0.7182	955.25
308.15	0.8035	972.23
308.15	0.8708	986.56
308.15	0.9324	1000.48
308.15	1.0000	1016.68
313.15	0.0000	847.17
313.15	0.0938	857.56
313.15	0.1532	864.5
313.15	0.2046	870.77
313.15	0.2698	879.09
313.15	0.3374	888.21
313.15	0.4002	897.12
313.15	0.4714	907.81
313.15	0.5487	920.1
313.15	0.6300	933.91
313.15	0.7182	950.01
313.15	0.8035	966.86
313.15	0.8708	981.09
313.15	0.9324	994.93
313.15	1.0000	1011.05
318.15	0.0000	842.88
318.15	0.0938	853.16
318.15	0.1532	860.01
318.15	0.2046	866.22
318.15	0.2698	874.47
318.15	0.3374	883.5
318.15	0.4002	892.34
318.15	0.4714	902.94
318.15	0.5487	915.12
318.15	0.6300	928.81
318.15	0.7182	944.77
318.15	0.8035	961.5
318.15	0.8708	975.62
318.15	0.9324	989.38
318.15	1.0000	1005.42

Mass density, kg/m3 [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1,4-Dioxane (2) - Liquid	Mass density, kg/m3 - Liquid
288.15	0.0000	868.59
288.15	0.0938	879.61
288.15	0.1532	886.95
288.15	0.2046	893.54
288.15	0.2698	902.26
288.15	0.3374	911.76
288.15	0.4002	921.05
288.15	0.4714	932.18
288.15	0.5487	945.0
288.15	0.6300	959.44
288.15	0.7182	976.23
288.15	0.8035	993.74
288.15	0.8708	1008.47
288.15	0.9324	1022.71
288.15	1.0000	1039.23
293.15	0.0000	864.31
293.15	0.0938	875.2
293.15	0.1532	882.46
293.15	0.2046	888.98
293.15	0.2698	897.62
293.15	0.3374	907.05
293.15	0.4002	916.26
293.15	0.4714	927.3
293.15	0.5487	940.02
293.15	0.6300	954.33
293.15	0.7182	970.98
293.15	0.8035	988.36
293.15	0.8708	1002.99
293.15	0.9324	1017.15
293.15	1.0000	1033.59
298.15	0.0000	860.02
298.15	0.0938	870.79
298.15	0.1532	877.97
298.15	0.2046	884.42
298.15	0.2698	892.98
298.15	0.3374	902.34
298.15	0.4002	911.47
298.15	0.4714	922.42
298.15	0.5487	935.04
298.15	0.6300	949.22
298.15	0.7182	965.73
298.15	0.8035	982.98
298.15	0.8708	997.51
298.15	0.9324	1011.59
298.15	1.0000	1027.95
303.15	0.0000	855.74
303.15	0.0938	866.38
303.15	0.1532	873.48
303.15	0.2046	879.87
303.15	0.2698	888.35
303.15	0.3374	897.63
303.15	0.4002	906.68
303.15	0.4714	917.55
303.15	0.5487	930.06
303.15	0.6300	944.11
303.15	0.7182	960.49
303.15	0.8035	977.6
303.15	0.8708	992.03
303.15	0.9324	1006.03
303.15	1.0000	1022.32
308.15	0.0000	851.45
308.15	0.0938	861.97
308.15	0.1532	868.99
308.15	0.2046	875.32
308.15	0.2698	883.72
308.15	0.3374	892.92
308.15	0.4002	901.9
308.15	0.4714	912.68
308.15	0.5487	925.08
308.15	0.6300	939.01
308.15	0.7182	955.25
308.15	0.8035	972.23
308.15	0.8708	986.56
308.15	0.9324	1000.48
308.15	1.0000	1016.68
313.15	0.0000	847.17
313.15	0.0938	857.56
313.15	0.1532	864.5
313.15	0.2046	870.77
313.15	0.2698	879.09
313.15	0.3374	888.21
313.15	0.4002	897.12
313.15	0.4714	907.81
313.15	0.5487	920.1
313.15	0.6300	933.91
313.15	0.7182	950.01
313.15	0.8035	966.86
313.15	0.8708	981.09
313.15	0.9324	994.93
313.15	1.0000	1011.05
318.15	0.0000	842.88
318.15	0.0938	853.16
318.15	0.1532	860.01
318.15	0.2046	866.22
318.15	0.2698	874.47
318.15	0.3374	883.5
318.15	0.4002	892.34
318.15	0.4714	902.94
318.15	0.5487	915.12
318.15	0.6300	928.81
318.15	0.7182	944.77
318.15	0.8035	961.5
318.15	0.8708	975.62
318.15	0.9324	989.38
318.15	1.0000	1005.42

Speed of sound, m/s [ref]

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Frequency, MHz = 3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1,4-Dioxane (2) - Liquid	Speed of sound, m/s - Liquid
293.15	0.0000	1346.7
293.15	0.0938	1341.2
293.15	0.1532	1338.2
293.15	0.2046	1335.9
293.15	0.2698	1333.4
293.15	0.3374	1331.4
293.15	0.4002	1330.1
293.15	0.4714	1329.3
293.15	0.5487	1329.6
293.15	0.6300	1331.2
293.15	0.7182	1335.0
293.15	0.8035	1341.0
293.15	0.8708	1347.8
293.15	0.9324	1355.8
293.15	1.0000	1367.2
298.15	0.0000	1323.6
298.15	0.0938	1318.3
298.15	0.1532	1315.4
298.15	0.2046	1313.2
298.15	0.2698	1310.8
298.15	0.3374	1308.8
298.15	0.4002	1307.6
298.15	0.4714	1307.0
298.15	0.5487	1307.3
298.15	0.6300	1309.1
298.15	0.7182	1312.9
298.15	0.8035	1318.8
298.15	0.8708	1325.5
298.15	0.9324	1333.5
298.15	1.0000	1344.7
303.15	0.0000	1302.4
303.15	0.0938	1297.2
303.15	0.1532	1294.4
303.15	0.2046	1292.2
303.15	0.2698	1289.8
303.15	0.3374	1287.9
303.15	0.4002	1286.6
303.15	0.4714	1286.0
303.15	0.5487	1286.3
303.15	0.6300	1288.1
303.15	0.7182	1291.9
303.15	0.8035	1297.7
303.15	0.8708	1304.4
303.15	0.9324	1312.2
303.15	1.0000	1323.1
308.15	0.0000	1282.3
308.15	0.0938	1277.1
308.15	0.1532	1274.3
308.15	0.2046	1272.1
308.15	0.2698	1269.7
308.15	0.3374	1267.8
308.15	0.4002	1266.5
308.15	0.4714	1265.8
308.15	0.5487	1266.0
308.15	0.6300	1267.7
308.15	0.7182	1271.2
308.15	0.8035	1276.9
308.15	0.8708	1283.2
308.15	0.9324	1290.7
308.15	1.0000	1301.2
313.15	0.0000	1262.3
313.15	0.0938	1257.2
313.15	0.1532	1254.3
313.15	0.2046	1252.2
313.15	0.2698	1249.8
313.15	0.3374	1247.9
313.15	0.4002	1246.6
313.15	0.4714	1245.8
313.15	0.5487	1246.0
313.15	0.6300	1247.5
313.15	0.7182	1250.9
313.15	0.8035	1256.4
313.15	0.8708	1262.4
313.15	0.9324	1269.6
313.15	1.0000	1279.7
318.15	0.0000	1243.0
318.15	0.0938	1237.9
318.15	0.1532	1235.1
318.15	0.2046	1232.9
318.15	0.2698	1230.5
318.15	0.3374	1228.5
318.15	0.4002	1227.2
318.15	0.4714	1226.4
318.15	0.5487	1226.5
318.15	0.6300	1227.9
318.15	0.7182	1231.1
318.15	0.8035	1236.2
318.15	0.8708	1242.0
318.15	0.9324	1248.9
318.15	1.0000	1258.6

Speed of sound, m/s [ref]

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Frequency, MHz = 3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1,4-Dioxane (2) - Liquid	Speed of sound, m/s - Liquid
293.15	0.0000	1346.7
293.15	0.0938	1341.2
293.15	0.1532	1338.2
293.15	0.2046	1335.9
293.15	0.2698	1333.4
293.15	0.3374	1331.4
293.15	0.4002	1330.1
293.15	0.4714	1329.3
293.15	0.5487	1329.6
293.15	0.6300	1331.2
293.15	0.7182	1335.0
293.15	0.8035	1341.0
293.15	0.8708	1347.8
293.15	0.9324	1355.8
293.15	1.0000	1367.2
298.15	0.0000	1323.6
298.15	0.0938	1318.3
298.15	0.1532	1315.4
298.15	0.2046	1313.2
298.15	0.2698	1310.8
298.15	0.3374	1308.8
298.15	0.4002	1307.6
298.15	0.4714	1307.0
298.15	0.5487	1307.3
298.15	0.6300	1309.1
298.15	0.7182	1312.9
298.15	0.8035	1318.8
298.15	0.8708	1325.5
298.15	0.9324	1333.5
298.15	1.0000	1344.7
303.15	0.0000	1302.4
303.15	0.0938	1297.2
303.15	0.1532	1294.4
303.15	0.2046	1292.2
303.15	0.2698	1289.8
303.15	0.3374	1287.9
303.15	0.4002	1286.6
303.15	0.4714	1286.0
303.15	0.5487	1286.3
303.15	0.6300	1288.1
303.15	0.7182	1291.9
303.15	0.8035	1297.7
303.15	0.8708	1304.4
303.15	0.9324	1312.2
303.15	1.0000	1323.1
308.15	0.0000	1282.3
308.15	0.0938	1277.1
308.15	0.1532	1274.3
308.15	0.2046	1272.1
308.15	0.2698	1269.7
308.15	0.3374	1267.8
308.15	0.4002	1266.5
308.15	0.4714	1265.8
308.15	0.5487	1266.0
308.15	0.6300	1267.7
308.15	0.7182	1271.2
308.15	0.8035	1276.9
308.15	0.8708	1283.2
308.15	0.9324	1290.7
308.15	1.0000	1301.2
313.15	0.0000	1262.3
313.15	0.0938	1257.2
313.15	0.1532	1254.3
313.15	0.2046	1252.2
313.15	0.2698	1249.8
313.15	0.3374	1247.9
313.15	0.4002	1246.6
313.15	0.4714	1245.8
313.15	0.5487	1246.0
313.15	0.6300	1247.5
313.15	0.7182	1250.9
313.15	0.8035	1256.4
313.15	0.8708	1262.4
313.15	0.9324	1269.6
313.15	1.0000	1279.7
318.15	0.0000	1243.0
318.15	0.0938	1237.9
318.15	0.1532	1235.1
318.15	0.2046	1232.9
318.15	0.2698	1230.5
318.15	0.3374	1228.5
318.15	0.4002	1227.2
318.15	0.4714	1226.4
318.15	0.5487	1226.5
318.15	0.6300	1227.9
318.15	0.7182	1231.1
318.15	0.8035	1236.2
318.15	0.8708	1242.0
318.15	0.9324	1248.9
318.15	1.0000	1258.6

Sources

• Physicochemical study of intermolecular interactions in 1,4-dioxane + aromatic hydrocarbons binary mixtures at different temperatures by using ultrasonic and viscometric methods
• Excess Molar Enthalpies for Binary and Ternary Mixtures containing Cyclic Ether, 2-Methylaniline and Aromatic Hydrocarbons
• Densities, Refractive Indices, and Excess Properties of Binary Mixtures of 1,4-Dioxane with Benzene, Toluene, o-Xylene, m-Xylene, p-Xylene, and Mesitylene at Temperatures from (288.15 to 318.15) K