Mixture of Cyclopentane + 1,4-Dioxane

Datasets

1. Mole fraction (2)
2. n₀ - Refractive index (Na D-line) (2)
3. ρ_l - Mass density, kg/m3 (2)
4. c_sound,fluid - Speed of Sound, m/s (2)
5. γ - Surface tension liquid-gas, N/m (2)
6. T_boil - Boiling temperature at pressure P, K (2)

Mole fraction of 1,4-Dioxane (2) [ref]

Fixed		Measured
Mole fraction of 1,4-Dioxane (2) - Liquid	Pressure, kPa - Liquid	Mole fraction of 1,4-Dioxane (2) - Gas
0.0518	101.30	0.0244
0.0521	66.60	0.0230
0.0585	40.00	0.0210
0.1024	101.30	0.0442
0.1051	66.60	0.0420
0.1066	40.00	0.0453
0.2029	40.00	0.0605
0.2033	101.30	0.0740
0.2077	66.60	0.0680
0.3097	101.30	0.0989
0.3163	66.60	0.0899
0.3294	40.00	0.0836
0.4187	66.60	0.1063
0.4213	101.30	0.1219
0.4317	40.00	0.0971
0.5183	101.30	0.1449
0.5225	66.60	0.1293
0.5300	40.00	0.1140
0.6106	40.00	0.1315
0.6360	101.30	0.1794
0.6378	66.60	0.1590
0.7200	101.30	0.2283
0.7285	66.60	0.1952
0.7359	40.00	0.1707
0.8144	101.30	0.2862
0.8231	66.60	0.2696
0.8303	40.00	0.2413
0.8851	40.00	0.3135
0.8944	66.60	0.3706
0.9000	101.30	0.4279
0.9094	40.00	0.3728
0.9098	66.60	0.4111
0.9206	101.30	0.4878
0.9430	66.60	0.5351
0.9439	40.00	0.5021
0.9617	101.30	0.6697
0.9698	66.60	0.7018
0.9760	40.00	0.7179
0.9770	101.30	0.7780
0.9892	40.00	0.8516
0.9914	66.60	0.8958
0.9914	101.30	0.9186

Mole fraction of 1,4-Dioxane (2) [ref]

Fixed		Measured
Mole fraction of 1,4-Dioxane (2) - Liquid	Pressure, kPa - Liquid	Mole fraction of 1,4-Dioxane (2) - Gas
0.0518	101.30	0.0244
0.0521	66.60	0.0230
0.0585	40.00	0.0210
0.1024	101.30	0.0442
0.1051	66.60	0.0420
0.1066	40.00	0.0453
0.2029	40.00	0.0605
0.2033	101.30	0.0740
0.2077	66.60	0.0680
0.3097	101.30	0.0989
0.3163	66.60	0.0899
0.3294	40.00	0.0836
0.4187	66.60	0.1063
0.4213	101.30	0.1219
0.4317	40.00	0.0971
0.5183	101.30	0.1449
0.5225	66.60	0.1293
0.5300	40.00	0.1140
0.6106	40.00	0.1315
0.6360	101.30	0.1794
0.6378	66.60	0.1590
0.7200	101.30	0.2283
0.7285	66.60	0.1952
0.7359	40.00	0.1707
0.8144	101.30	0.2862
0.8231	66.60	0.2696
0.8303	40.00	0.2413
0.8851	40.00	0.3135
0.8944	66.60	0.3706
0.9000	101.30	0.4279
0.9094	40.00	0.3728
0.9098	66.60	0.4111
0.9206	101.30	0.4878
0.9430	66.60	0.5351
0.9439	40.00	0.5021
0.9617	101.30	0.6697
0.9698	66.60	0.7018
0.9760	40.00	0.7179
0.9770	101.30	0.7780
0.9892	40.00	0.8516
0.9914	66.60	0.8958
0.9914	101.30	0.9186

Refractive index (Na D-line) [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Volume fraction of 1,4-Dioxane (2) - Liquid	Refractive index (Na D-line) - Liquid
283.15	0.0438	1.4119
283.15	0.0870	1.412
283.15	0.1787	1.4127
283.15	0.2781	1.4138
283.15	0.3694	1.4151
283.15	0.4754	1.4169
283.15	0.5928	1.4185
283.15	0.7068	1.4208
283.15	0.7975	1.4227
283.15	0.9083	1.4252
283.15	0.9568	1.4262
298.15	0.0401	1.4033
298.15	0.0979	1.4036
298.15	0.1873	1.4043
298.15	0.2827	1.4056
298.15	0.3727	1.407
298.15	0.4709	1.4087
298.15	0.5703	1.4106
298.15	0.6847	1.413
298.15	0.7850	1.4152
298.15	0.8986	1.4177
298.15	0.9436	1.4187
313.15	0.0434	1.3945
313.15	0.0858	1.3948
313.15	0.1810	1.3956
313.15	0.2747	1.3969
313.15	0.3702	1.3985
313.15	0.4720	1.4005
313.15	0.5688	1.4026
313.15	0.6767	1.405
313.15	0.7759	1.4073
313.15	0.8977	1.4102
313.15	0.9330	1.411

Refractive index (Na D-line) [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Volume fraction of 1,4-Dioxane (2) - Liquid	Refractive index (Na D-line) - Liquid
283.15	0.0438	1.4119
283.15	0.0870	1.412
283.15	0.1787	1.4127
283.15	0.2781	1.4138
283.15	0.3694	1.4151
283.15	0.4754	1.4169
283.15	0.5928	1.4185
283.15	0.7068	1.4208
283.15	0.7975	1.4227
283.15	0.9083	1.4252
283.15	0.9568	1.4262
298.15	0.0401	1.4033
298.15	0.0979	1.4036
298.15	0.1873	1.4043
298.15	0.2827	1.4056
298.15	0.3727	1.407
298.15	0.4709	1.4087
298.15	0.5703	1.4106
298.15	0.6847	1.413
298.15	0.7850	1.4152
298.15	0.8986	1.4177
298.15	0.9436	1.4187
313.15	0.0434	1.3945
313.15	0.0858	1.3948
313.15	0.1810	1.3956
313.15	0.2747	1.3969
313.15	0.3702	1.3985
313.15	0.4720	1.4005
313.15	0.5688	1.4026
313.15	0.6767	1.405
313.15	0.7759	1.4073
313.15	0.8977	1.4102
313.15	0.9330	1.411

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1,4-Dioxane (2) - Liquid	Mass density, kg/m3 - Liquid
283.15	0.0516	766.94
283.15	0.0950	777.38
283.15	0.1944	802.55
283.15	0.2987	830.28
283.15	0.3973	857.59
283.15	0.4990	886.71
283.15	0.6003	916.64
283.15	0.7063	949.05
283.15	0.8072	980.93
283.15	0.9076	1013.82
283.15	0.9528	1029.04
298.15	0.0488	751.07
298.15	0.0945	762.02
298.15	0.1818	783.72
298.15	0.2983	814.38
298.15	0.3959	841.12
298.15	0.4962	869.6
298.15	0.6067	902.0
298.15	0.7034	931.45
298.15	0.8110	965.2
298.15	0.9025	995.13
298.15	0.9506	1011.12
313.15	0.0449	734.98
313.15	0.0940	746.73
313.15	0.1950	771.73
313.15	0.2962	798.13
313.15	0.3969	825.52
313.15	0.4983	854.12
313.15	0.5994	883.66
313.15	0.6987	913.64
313.15	0.8026	946.08
313.15	0.9066	979.72
313.15	0.9482	993.49

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1,4-Dioxane (2) - Liquid	Mass density, kg/m3 - Liquid
283.15	0.0516	766.94
283.15	0.0950	777.38
283.15	0.1944	802.55
283.15	0.2987	830.28
283.15	0.3973	857.59
283.15	0.4990	886.71
283.15	0.6003	916.64
283.15	0.7063	949.05
283.15	0.8072	980.93
283.15	0.9076	1013.82
283.15	0.9528	1029.04
298.15	0.0488	751.07
298.15	0.0945	762.02
298.15	0.1818	783.72
298.15	0.2983	814.38
298.15	0.3959	841.12
298.15	0.4962	869.6
298.15	0.6067	902.0
298.15	0.7034	931.45
298.15	0.8110	965.2
298.15	0.9025	995.13
298.15	0.9506	1011.12
313.15	0.0449	734.98
313.15	0.0940	746.73
313.15	0.1950	771.73
313.15	0.2962	798.13
313.15	0.3969	825.52
313.15	0.4983	854.12
313.15	0.5994	883.66
313.15	0.6987	913.64
313.15	0.8026	946.08
313.15	0.9066	979.72
313.15	0.9482	993.49

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1,4-Dioxane (2) - Liquid	Speed of sound, m/s - Liquid
283.15	0.0516	1280.7
283.15	0.0950	1279.4
283.15	0.1944	1280.5
283.15	0.2987	1286.0
283.15	0.3973	1294.2
283.15	0.4990	1305.8
283.15	0.6003	1320.5
283.15	0.7063	1339.6
283.15	0.8072	1361.0
283.15	0.9076	1385.1
283.15	0.9528	1397.0
298.15	0.0488	1204.5
298.15	0.0945	1203.8
298.15	0.1818	1205.5
298.15	0.2983	1211.9
298.15	0.3959	1221.4
298.15	0.4962	1234.1
298.15	0.6067	1251.5
298.15	0.7034	1269.8
298.15	0.8110	1293.3
298.15	0.9025	1316.4
298.15	0.9506	1329.6
313.15	0.0449	1128.5
313.15	0.0940	1128.3
313.15	0.1950	1131.3
313.15	0.2962	1138.6
313.15	0.3969	1149.5
313.15	0.4983	1163.6
313.15	0.5994	1180.8
313.15	0.6987	1200.2
313.15	0.8026	1223.8
313.15	0.9066	1250.8
313.15	0.9482	1263.0

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1,4-Dioxane (2) - Liquid	Speed of sound, m/s - Liquid
283.15	0.0516	1280.7
283.15	0.0950	1279.4
283.15	0.1944	1280.5
283.15	0.2987	1286.0
283.15	0.3973	1294.2
283.15	0.4990	1305.8
283.15	0.6003	1320.5
283.15	0.7063	1339.6
283.15	0.8072	1361.0
283.15	0.9076	1385.1
283.15	0.9528	1397.0
298.15	0.0488	1204.5
298.15	0.0945	1203.8
298.15	0.1818	1205.5
298.15	0.2983	1211.9
298.15	0.3959	1221.4
298.15	0.4962	1234.1
298.15	0.6067	1251.5
298.15	0.7034	1269.8
298.15	0.8110	1293.3
298.15	0.9025	1316.4
298.15	0.9506	1329.6
313.15	0.0449	1128.5
313.15	0.0940	1128.3
313.15	0.1950	1131.3
313.15	0.2962	1138.6
313.15	0.3969	1149.5
313.15	0.4983	1163.6
313.15	0.5994	1180.8
313.15	0.6987	1200.2
313.15	0.8026	1223.8
313.15	0.9066	1250.8
313.15	0.9482	1263.0

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

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1,4-Dioxane (2) - Liquid	Surface tension liquid-gas, N/m - Liquid
283.15	0.0615	0.0244
283.15	0.1210	0.0246
283.15	0.1824	0.0248
283.15	0.2656	0.0250
283.15	0.4058	0.0256
283.15	0.5313	0.0264
283.15	0.6376	0.0273
283.15	0.7264	0.0284
283.15	0.8060	0.0297
283.15	0.9020	0.0319
283.15	0.9642	0.0338
298.15	0.0615	0.0224
298.15	0.1210	0.0226
298.15	0.1824	0.0227
298.15	0.2656	0.0230
298.15	0.4058	0.0237
298.15	0.5313	0.0246
298.15	0.6376	0.0256
298.15	0.7264	0.0267
298.15	0.8060	0.0279
298.15	0.9020	0.0300
298.15	0.9642	0.0319
313.15	0.0615	0.0201
313.15	0.1210	0.0204
313.15	0.1824	0.0208
313.15	0.2656	0.0211
313.15	0.4058	0.0218
313.15	0.5313	0.0226
313.15	0.6376	0.0236
313.15	0.7264	0.0247
313.15	0.8060	0.0261
313.15	0.9020	0.0282
313.15	0.9642	0.0300

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

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1,4-Dioxane (2) - Liquid	Surface tension liquid-gas, N/m - Liquid
283.15	0.0615	0.0244
283.15	0.1210	0.0246
283.15	0.1824	0.0248
283.15	0.2656	0.0250
283.15	0.4058	0.0256
283.15	0.5313	0.0264
283.15	0.6376	0.0273
283.15	0.7264	0.0284
283.15	0.8060	0.0297
283.15	0.9020	0.0319
283.15	0.9642	0.0338
298.15	0.0615	0.0224
298.15	0.1210	0.0226
298.15	0.1824	0.0227
298.15	0.2656	0.0230
298.15	0.4058	0.0237
298.15	0.5313	0.0246
298.15	0.6376	0.0256
298.15	0.7264	0.0267
298.15	0.8060	0.0279
298.15	0.9020	0.0300
298.15	0.9642	0.0319
313.15	0.0615	0.0201
313.15	0.1210	0.0204
313.15	0.1824	0.0208
313.15	0.2656	0.0211
313.15	0.4058	0.0218
313.15	0.5313	0.0226
313.15	0.6376	0.0236
313.15	0.7264	0.0247
313.15	0.8060	0.0261
313.15	0.9020	0.0282
313.15	0.9642	0.0300

Boiling temperature at pressure P, K [ref]

Fixed		Measured
Mole fraction of 1,4-Dioxane (2) - Liquid	Pressure, kPa - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	101.30	322.40
0.0518	101.30	323.32
0.0521	66.60	311.08
0.0585	40.00	298.00
0.1024	101.30	324.13
0.1051	66.60	311.83
0.1066	40.00	298.41
0.2029	40.00	299.71
0.2033	101.30	325.50
0.2077	66.60	313.29
0.3097	101.30	327.13
0.3163	66.60	314.81
0.3294	40.00	301.27
0.4187	66.60	316.24
0.4213	101.30	329.06
0.4317	40.00	302.36
0.5183	101.30	330.82
0.5225	66.60	318.13
0.5300	40.00	304.02
0.6106	40.00	305.78
0.6360	101.30	334.00
0.6378	66.60	320.64
0.7200	101.30	337.67
0.7285	66.60	324.01
0.7359	40.00	309.63
0.8144	101.30	342.63
0.8231	66.60	329.70
0.8303	40.00	315.27
0.8851	40.00	320.28
0.8944	66.60	336.55
0.9000	101.30	351.55
0.9094	40.00	323.31
0.9098	66.60	338.81
0.9206	101.30	354.51
0.9430	66.60	344.91
0.9439	40.00	330.05
0.9617	101.30	362.84
0.9698	66.60	351.41
0.9760	40.00	338.06
0.9770	101.30	366.85
0.9892	40.00	342.24
0.9914	66.60	358.09
0.9914	101.30	371.58

Boiling temperature at pressure P, K [ref]

Fixed		Measured
Mole fraction of 1,4-Dioxane (2) - Liquid	Pressure, kPa - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	101.30	322.40
0.0518	101.30	323.32
0.0521	66.60	311.08
0.0585	40.00	298.00
0.1024	101.30	324.13
0.1051	66.60	311.83
0.1066	40.00	298.41
0.2029	40.00	299.71
0.2033	101.30	325.50
0.2077	66.60	313.29
0.3097	101.30	327.13
0.3163	66.60	314.81
0.3294	40.00	301.27
0.4187	66.60	316.24
0.4213	101.30	329.06
0.4317	40.00	302.36
0.5183	101.30	330.82
0.5225	66.60	318.13
0.5300	40.00	304.02
0.6106	40.00	305.78
0.6360	101.30	334.00
0.6378	66.60	320.64
0.7200	101.30	337.67
0.7285	66.60	324.01
0.7359	40.00	309.63
0.8144	101.30	342.63
0.8231	66.60	329.70
0.8303	40.00	315.27
0.8851	40.00	320.28
0.8944	66.60	336.55
0.9000	101.30	351.55
0.9094	40.00	323.31
0.9098	66.60	338.81
0.9206	101.30	354.51
0.9430	66.60	344.91
0.9439	40.00	330.05
0.9617	101.30	362.84
0.9698	66.60	351.41
0.9760	40.00	338.06
0.9770	101.30	366.85
0.9892	40.00	342.24
0.9914	66.60	358.09
0.9914	101.30	371.58

Sources

• Speeds of Sound and Isentropic Compressibilities for Binary Mixtures of a Cyclic Diether with a Cyclic Compound at Three Temperatures
• Experimental and predicted vapour liquid equilibrium of 1,4-dioxane with cycloalkanes and benzene
• Thermophysical study of 1,4-dioxane with cycloalkane mixtures