Operational condition: Temperature, K = 363.15 (Liquid)
Mole fraction of 1,4-Dioxane (2) - Liquid | Mole fraction of 1,4-Dioxane (2) - Gas |
---|---|
0.0000 | 0.0000 |
0.0215 | 0.0562 |
0.0652 | 0.1586 |
0.1284 | 0.2808 |
0.1777 | 0.3610 |
0.2033 | 0.4015 |
0.2469 | 0.4463 |
0.3158 | 0.5211 |
0.3642 | 0.5714 |
0.4091 | 0.6067 |
0.4565 | 0.6482 |
0.5172 | 0.6829 |
0.5988 | 0.7504 |
0.6292 | 0.7688 |
0.8217 | 0.8844 |
0.9578 | 0.9713 |
1.0000 | 1.0000 |
Operational condition: Temperature, K = 363.15 (Liquid)
Mole fraction of 1,4-Dioxane (2) - Liquid | Mole fraction of 1,4-Dioxane (2) - Gas |
---|---|
0.0000 | 0.0000 |
0.0215 | 0.0562 |
0.0652 | 0.1586 |
0.1284 | 0.2808 |
0.1777 | 0.3610 |
0.2033 | 0.4015 |
0.2469 | 0.4463 |
0.3158 | 0.5211 |
0.3642 | 0.5714 |
0.4091 | 0.6067 |
0.4565 | 0.6482 |
0.5172 | 0.6829 |
0.5988 | 0.7504 |
0.6292 | 0.7688 |
0.8217 | 0.8844 |
0.9578 | 0.9713 |
1.0000 | 1.0000 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of 1,4-Dioxane (2) - Liquid | Viscosity, Pa*s - Liquid |
303.15 | 0.0000 | 0.0023 |
303.15 | 0.1066 | 0.0020 |
303.15 | 0.2116 | 0.0016 |
303.15 | 0.3151 | 0.0014 |
303.15 | 0.4171 | 0.0012 |
303.15 | 0.5177 | 0.0012 |
303.15 | 0.6169 | 0.0011 |
303.15 | 0.6659 | 0.0011 |
303.15 | 0.7146 | 0.0010 |
303.15 | 0.7630 | 0.0010 |
303.15 | 0.8111 | 0.0010 |
303.15 | 0.8588 | 0.0010 |
303.15 | 0.9062 | 0.0011 |
303.15 | 1.0000 | 0.0011 |
308.15 | 0.0000 | 0.0019 |
308.15 | 0.1066 | 0.0017 |
308.15 | 0.2116 | 0.0014 |
308.15 | 0.3151 | 0.0012 |
308.15 | 0.4171 | 0.0011 |
308.15 | 0.5177 | 0.0010 |
308.15 | 0.6169 | 0.0010 |
308.15 | 0.6659 | 0.0010 |
308.15 | 0.7146 | 0.0010 |
308.15 | 0.7630 | 0.0010 |
308.15 | 0.8111 | 0.0009 |
308.15 | 0.8588 | 0.0010 |
308.15 | 0.9062 | 0.0010 |
308.15 | 1.0000 | 0.0010 |
313.15 | 0.0000 | 0.0017 |
313.15 | 0.1066 | 0.0015 |
313.15 | 0.2116 | 0.0013 |
313.15 | 0.3151 | 0.0011 |
313.15 | 0.4171 | 0.0010 |
313.15 | 0.5177 | 0.0010 |
313.15 | 0.6169 | 0.0009 |
313.15 | 0.6659 | 0.0009 |
313.15 | 0.7146 | 0.0009 |
313.15 | 0.7630 | 0.0009 |
313.15 | 0.8111 | 0.0009 |
313.15 | 0.8588 | 0.0009 |
313.15 | 0.9062 | 0.0009 |
313.15 | 1.0000 | 0.0010 |
Operational condition: Pressure, kPa = 101 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of 1,4-Dioxane (2) - Liquid | Viscosity, Pa*s - Liquid |
298.15 | 0.0000 | 0.0026 |
298.15 | 0.1014 | 0.0022 |
298.15 | 0.2015 | 0.0018 |
298.15 | 0.2982 | 0.0015 |
298.15 | 0.3995 | 0.0013 |
298.15 | 0.4945 | 0.0012 |
298.15 | 0.5993 | 0.0012 |
298.15 | 0.7023 | 0.0012 |
298.15 | 0.8020 | 0.0012 |
298.15 | 0.9017 | 0.0012 |
298.15 | 1.0000 | 0.0012 |
303.15 | 0.0000 | 0.0022 |
303.15 | 0.1014 | 0.0019 |
303.15 | 0.2015 | 0.0016 |
303.15 | 0.2982 | 0.0013 |
303.15 | 0.3995 | 0.0012 |
303.15 | 0.4945 | 0.0011 |
303.15 | 0.5993 | 0.0011 |
303.15 | 0.7023 | 0.0011 |
303.15 | 0.8020 | 0.0011 |
303.15 | 0.9017 | 0.0011 |
303.15 | 1.0000 | 0.0011 |
308.15 | 0.0000 | 0.0020 |
308.15 | 0.1014 | 0.0017 |
308.15 | 0.2015 | 0.0014 |
308.15 | 0.2982 | 0.0012 |
308.15 | 0.3995 | 0.0011 |
308.15 | 0.4945 | 0.0010 |
308.15 | 0.5993 | 0.0010 |
308.15 | 0.7023 | 0.0010 |
308.15 | 0.8020 | 0.0010 |
308.15 | 0.9017 | 0.0010 |
308.15 | 1.0000 | 0.0010 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of 1,4-Dioxane (2) - Liquid | Viscosity, Pa*s - Liquid |
303.15 | 0.0000 | 0.0023 |
303.15 | 0.1066 | 0.0020 |
303.15 | 0.2116 | 0.0016 |
303.15 | 0.3151 | 0.0014 |
303.15 | 0.4171 | 0.0012 |
303.15 | 0.5177 | 0.0012 |
303.15 | 0.6169 | 0.0011 |
303.15 | 0.6659 | 0.0011 |
303.15 | 0.7146 | 0.0010 |
303.15 | 0.7630 | 0.0010 |
303.15 | 0.8111 | 0.0010 |
303.15 | 0.8588 | 0.0010 |
303.15 | 0.9062 | 0.0011 |
303.15 | 1.0000 | 0.0011 |
308.15 | 0.0000 | 0.0019 |
308.15 | 0.1066 | 0.0017 |
308.15 | 0.2116 | 0.0014 |
308.15 | 0.3151 | 0.0012 |
308.15 | 0.4171 | 0.0011 |
308.15 | 0.5177 | 0.0010 |
308.15 | 0.6169 | 0.0010 |
308.15 | 0.6659 | 0.0010 |
308.15 | 0.7146 | 0.0010 |
308.15 | 0.7630 | 0.0010 |
308.15 | 0.8111 | 0.0009 |
308.15 | 0.8588 | 0.0010 |
308.15 | 0.9062 | 0.0010 |
308.15 | 1.0000 | 0.0010 |
313.15 | 0.0000 | 0.0017 |
313.15 | 0.1066 | 0.0015 |
313.15 | 0.2116 | 0.0013 |
313.15 | 0.3151 | 0.0011 |
313.15 | 0.4171 | 0.0010 |
313.15 | 0.5177 | 0.0010 |
313.15 | 0.6169 | 0.0009 |
313.15 | 0.6659 | 0.0009 |
313.15 | 0.7146 | 0.0009 |
313.15 | 0.7630 | 0.0009 |
313.15 | 0.8111 | 0.0009 |
313.15 | 0.8588 | 0.0009 |
313.15 | 0.9062 | 0.0009 |
313.15 | 1.0000 | 0.0010 |
Operational condition: Pressure, kPa = 101 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of 1,4-Dioxane (2) - Liquid | Viscosity, Pa*s - Liquid |
298.15 | 0.0000 | 0.0026 |
298.15 | 0.1014 | 0.0022 |
298.15 | 0.2015 | 0.0018 |
298.15 | 0.2982 | 0.0015 |
298.15 | 0.3995 | 0.0013 |
298.15 | 0.4945 | 0.0012 |
298.15 | 0.5993 | 0.0012 |
298.15 | 0.7023 | 0.0012 |
298.15 | 0.8020 | 0.0012 |
298.15 | 0.9017 | 0.0012 |
298.15 | 1.0000 | 0.0012 |
303.15 | 0.0000 | 0.0022 |
303.15 | 0.1014 | 0.0019 |
303.15 | 0.2015 | 0.0016 |
303.15 | 0.2982 | 0.0013 |
303.15 | 0.3995 | 0.0012 |
303.15 | 0.4945 | 0.0011 |
303.15 | 0.5993 | 0.0011 |
303.15 | 0.7023 | 0.0011 |
303.15 | 0.8020 | 0.0011 |
303.15 | 0.9017 | 0.0011 |
303.15 | 1.0000 | 0.0011 |
308.15 | 0.0000 | 0.0020 |
308.15 | 0.1014 | 0.0017 |
308.15 | 0.2015 | 0.0014 |
308.15 | 0.2982 | 0.0012 |
308.15 | 0.3995 | 0.0011 |
308.15 | 0.4945 | 0.0010 |
308.15 | 0.5993 | 0.0010 |
308.15 | 0.7023 | 0.0010 |
308.15 | 0.8020 | 0.0010 |
308.15 | 0.9017 | 0.0010 |
308.15 | 1.0000 | 0.0010 |
Operational condition: Temperature, K = 363.15 (Liquid)
Mole fraction of 1,4-Dioxane (2) - Liquid | Vapor or sublimation pressure, kPa - Liquid |
---|---|
0.0000 | 34.12 |
0.0215 | 35.72 |
0.0652 | 37.99 |
0.1284 | 41.99 |
0.1777 | 44.25 |
0.2033 | 45.85 |
0.2469 | 47.72 |
0.3158 | 50.65 |
0.3642 | 52.79 |
0.4091 | 54.79 |
0.4565 | 56.52 |
0.5172 | 58.25 |
0.5988 | 61.18 |
0.6292 | 62.12 |
0.8217 | 67.32 |
0.9578 | 69.85 |
1.0000 | 70.91 |
Operational condition: Temperature, K = 363.15 (Liquid)
Mole fraction of 1,4-Dioxane (2) - Liquid | Vapor or sublimation pressure, kPa - Liquid |
---|---|
0.0000 | 34.12 |
0.0215 | 35.72 |
0.0652 | 37.99 |
0.1284 | 41.99 |
0.1777 | 44.25 |
0.2033 | 45.85 |
0.2469 | 47.72 |
0.3158 | 50.65 |
0.3642 | 52.79 |
0.4091 | 54.79 |
0.4565 | 56.52 |
0.5172 | 58.25 |
0.5988 | 61.18 |
0.6292 | 62.12 |
0.8217 | 67.32 |
0.9578 | 69.85 |
1.0000 | 70.91 |
Operational condition: Pressure, kPa = 101 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of 1,4-Dioxane (2) - Liquid | Refractive index (Na D-line) - Liquid |
298.15 | 0.0000 | 1.3983 |
298.15 | 0.1014 | 1.3999 |
298.15 | 0.2015 | 1.4016 |
298.15 | 0.2982 | 1.4032 |
298.15 | 0.3995 | 1.4052 |
298.15 | 0.4945 | 1.4071 |
298.15 | 0.5993 | 1.4095 |
298.15 | 0.7023 | 1.4119 |
298.15 | 0.8020 | 1.4145 |
298.15 | 0.9017 | 1.4172 |
298.15 | 1.0000 | 1.4203 |
303.15 | 0.0000 | 1.3955 |
303.15 | 0.1014 | 1.3976 |
303.15 | 0.2015 | 1.3992 |
303.15 | 0.2982 | 1.4008 |
303.15 | 0.3995 | 1.4028 |
303.15 | 0.4945 | 1.4046 |
303.15 | 0.5993 | 1.4069 |
303.15 | 0.7023 | 1.4094 |
303.15 | 0.8020 | 1.4118 |
303.15 | 0.9017 | 1.4145 |
303.15 | 1.0000 | 1.4164 |
308.15 | 0.0000 | 1.3937 |
308.15 | 0.1014 | 1.3952 |
308.15 | 0.2015 | 1.3968 |
308.15 | 0.2982 | 1.3984 |
308.15 | 0.3995 | 1.4003 |
308.15 | 0.4945 | 1.4022 |
308.15 | 0.5993 | 1.4044 |
308.15 | 0.7023 | 1.4068 |
308.15 | 0.8020 | 1.4093 |
308.15 | 0.9017 | 1.4118 |
308.15 | 1.0000 | 1.4145 |
Operational condition: Pressure, kPa = 101 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of 1,4-Dioxane (2) - Liquid | Refractive index (Na D-line) - Liquid |
298.15 | 0.0000 | 1.3983 |
298.15 | 0.1014 | 1.3999 |
298.15 | 0.2015 | 1.4016 |
298.15 | 0.2982 | 1.4032 |
298.15 | 0.3995 | 1.4052 |
298.15 | 0.4945 | 1.4071 |
298.15 | 0.5993 | 1.4095 |
298.15 | 0.7023 | 1.4119 |
298.15 | 0.8020 | 1.4145 |
298.15 | 0.9017 | 1.4172 |
298.15 | 1.0000 | 1.4203 |
303.15 | 0.0000 | 1.3955 |
303.15 | 0.1014 | 1.3976 |
303.15 | 0.2015 | 1.3992 |
303.15 | 0.2982 | 1.4008 |
303.15 | 0.3995 | 1.4028 |
303.15 | 0.4945 | 1.4046 |
303.15 | 0.5993 | 1.4069 |
303.15 | 0.7023 | 1.4094 |
303.15 | 0.8020 | 1.4118 |
303.15 | 0.9017 | 1.4145 |
303.15 | 1.0000 | 1.4164 |
308.15 | 0.0000 | 1.3937 |
308.15 | 0.1014 | 1.3952 |
308.15 | 0.2015 | 1.3968 |
308.15 | 0.2982 | 1.3984 |
308.15 | 0.3995 | 1.4003 |
308.15 | 0.4945 | 1.4022 |
308.15 | 0.5993 | 1.4044 |
308.15 | 0.7023 | 1.4068 |
308.15 | 0.8020 | 1.4093 |
308.15 | 0.9017 | 1.4118 |
308.15 | 1.0000 | 1.4145 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of 1,4-Dioxane (2) - Liquid | Mass density, kg/m3 - Liquid |
303.15 | 0.0000 | 805.7 |
303.15 | 0.1066 | 826.5 |
303.15 | 0.2116 | 847.6 |
303.15 | 0.3151 | 868.6 |
303.15 | 0.4171 | 889.9 |
303.15 | 0.5177 | 911.3 |
303.15 | 0.6169 | 932.8 |
303.15 | 0.6659 | 943.6 |
303.15 | 0.7146 | 954.6 |
303.15 | 0.7630 | 965.6 |
303.15 | 0.8111 | 976.7 |
303.15 | 0.8588 | 987.9 |
303.15 | 0.9062 | 999.2 |
303.15 | 1.0000 | 1022.3 |
308.15 | 0.0000 | 797.2 |
308.15 | 0.1066 | 818.4 |
308.15 | 0.2116 | 839.9 |
308.15 | 0.3151 | 861.3 |
308.15 | 0.4171 | 882.7 |
308.15 | 0.5177 | 904.3 |
308.15 | 0.6169 | 926.2 |
308.15 | 0.6659 | 937.3 |
308.15 | 0.7146 | 948.4 |
308.15 | 0.7630 | 959.6 |
308.15 | 0.8111 | 971.0 |
308.15 | 0.8588 | 982.3 |
308.15 | 0.9062 | 993.6 |
308.15 | 1.0000 | 1016.7 |
313.15 | 0.0000 | 795.5 |
313.15 | 0.1066 | 816.8 |
313.15 | 0.2116 | 837.9 |
313.15 | 0.3151 | 859.0 |
313.15 | 0.4171 | 880.2 |
313.15 | 0.5177 | 901.5 |
313.15 | 0.6169 | 923.1 |
313.15 | 0.6659 | 934.0 |
313.15 | 0.7146 | 945.2 |
313.15 | 0.7630 | 956.3 |
313.15 | 0.8111 | 967.4 |
313.15 | 0.8588 | 978.6 |
313.15 | 0.9062 | 989.7 |
313.15 | 1.0000 | 1012.0 |
Operational condition: Pressure, kPa = 101 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of 1,4-Dioxane (2) - Liquid | Mass density, kg/m3 - Liquid |
298.15 | 0.0000 | 805.8 |
298.15 | 0.1014 | 826.1 |
298.15 | 0.2015 | 846.7 |
298.15 | 0.2982 | 866.9 |
298.15 | 0.3995 | 888.7 |
298.15 | 0.4945 | 909.6 |
298.15 | 0.5993 | 933.5 |
298.15 | 0.7023 | 957.5 |
298.15 | 0.8020 | 981.1 |
298.15 | 0.9017 | 1004.9 |
298.15 | 1.0000 | 1028.6 |
303.15 | 0.0000 | 802.0 |
303.15 | 0.1014 | 822.1 |
303.15 | 0.2015 | 842.4 |
303.15 | 0.2982 | 862.4 |
303.15 | 0.3995 | 884.0 |
303.15 | 0.4945 | 904.8 |
303.15 | 0.5993 | 928.4 |
303.15 | 0.7023 | 952.3 |
303.15 | 0.8020 | 975.8 |
303.15 | 0.9017 | 999.5 |
303.15 | 1.0000 | 1022.9 |
308.15 | 0.0000 | 798.0 |
308.15 | 0.1014 | 818.1 |
308.15 | 0.2015 | 838.1 |
308.15 | 0.2982 | 858.0 |
308.15 | 0.3995 | 879.5 |
308.15 | 0.4945 | 900.1 |
308.15 | 0.5993 | 923.4 |
308.15 | 0.7023 | 947.1 |
308.15 | 0.8020 | 970.4 |
308.15 | 0.9017 | 994.0 |
308.15 | 1.0000 | 1017.2 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of 1,4-Dioxane (2) - Liquid | Mass density, kg/m3 - Liquid |
303.15 | 0.0000 | 805.7 |
303.15 | 0.1066 | 826.5 |
303.15 | 0.2116 | 847.6 |
303.15 | 0.3151 | 868.6 |
303.15 | 0.4171 | 889.9 |
303.15 | 0.5177 | 911.3 |
303.15 | 0.6169 | 932.8 |
303.15 | 0.6659 | 943.6 |
303.15 | 0.7146 | 954.6 |
303.15 | 0.7630 | 965.6 |
303.15 | 0.8111 | 976.7 |
303.15 | 0.8588 | 987.9 |
303.15 | 0.9062 | 999.2 |
303.15 | 1.0000 | 1022.3 |
308.15 | 0.0000 | 797.2 |
308.15 | 0.1066 | 818.4 |
308.15 | 0.2116 | 839.9 |
308.15 | 0.3151 | 861.3 |
308.15 | 0.4171 | 882.7 |
308.15 | 0.5177 | 904.3 |
308.15 | 0.6169 | 926.2 |
308.15 | 0.6659 | 937.3 |
308.15 | 0.7146 | 948.4 |
308.15 | 0.7630 | 959.6 |
308.15 | 0.8111 | 971.0 |
308.15 | 0.8588 | 982.3 |
308.15 | 0.9062 | 993.6 |
308.15 | 1.0000 | 1016.7 |
313.15 | 0.0000 | 795.5 |
313.15 | 0.1066 | 816.8 |
313.15 | 0.2116 | 837.9 |
313.15 | 0.3151 | 859.0 |
313.15 | 0.4171 | 880.2 |
313.15 | 0.5177 | 901.5 |
313.15 | 0.6169 | 923.1 |
313.15 | 0.6659 | 934.0 |
313.15 | 0.7146 | 945.2 |
313.15 | 0.7630 | 956.3 |
313.15 | 0.8111 | 967.4 |
313.15 | 0.8588 | 978.6 |
313.15 | 0.9062 | 989.7 |
313.15 | 1.0000 | 1012.0 |
Operational condition: Pressure, kPa = 101 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of 1,4-Dioxane (2) - Liquid | Mass density, kg/m3 - Liquid |
298.15 | 0.0000 | 805.8 |
298.15 | 0.1014 | 826.1 |
298.15 | 0.2015 | 846.7 |
298.15 | 0.2982 | 866.9 |
298.15 | 0.3995 | 888.7 |
298.15 | 0.4945 | 909.6 |
298.15 | 0.5993 | 933.5 |
298.15 | 0.7023 | 957.5 |
298.15 | 0.8020 | 981.1 |
298.15 | 0.9017 | 1004.9 |
298.15 | 1.0000 | 1028.6 |
303.15 | 0.0000 | 802.0 |
303.15 | 0.1014 | 822.1 |
303.15 | 0.2015 | 842.4 |
303.15 | 0.2982 | 862.4 |
303.15 | 0.3995 | 884.0 |
303.15 | 0.4945 | 904.8 |
303.15 | 0.5993 | 928.4 |
303.15 | 0.7023 | 952.3 |
303.15 | 0.8020 | 975.8 |
303.15 | 0.9017 | 999.5 |
303.15 | 1.0000 | 1022.9 |
308.15 | 0.0000 | 798.0 |
308.15 | 0.1014 | 818.1 |
308.15 | 0.2015 | 838.1 |
308.15 | 0.2982 | 858.0 |
308.15 | 0.3995 | 879.5 |
308.15 | 0.4945 | 900.1 |
308.15 | 0.5993 | 923.4 |
308.15 | 0.7023 | 947.1 |
308.15 | 0.8020 | 970.4 |
308.15 | 0.9017 | 994.0 |
308.15 | 1.0000 | 1017.2 |
Operational conditions:
Mole fraction of 1,4-Dioxane (2) - Liquid | Speed of sound, m/s - Liquid |
---|---|
0.0000 | 1237.0 |
0.1014 | 1249.0 |
0.2015 | 1260.0 |
0.2982 | 1270.0 |
0.3995 | 1281.0 |
0.4945 | 1291.0 |
0.5993 | 1301.0 |
0.7023 | 1310.0 |
0.8020 | 1320.0 |
0.9017 | 1332.0 |
1.0000 | 1345.0 |
Operational conditions:
Mole fraction of 1,4-Dioxane (2) - Liquid | Speed of sound, m/s - Liquid |
---|---|
0.0000 | 1237.0 |
0.1014 | 1249.0 |
0.2015 | 1260.0 |
0.2982 | 1270.0 |
0.3995 | 1281.0 |
0.4945 | 1291.0 |
0.5993 | 1301.0 |
0.7023 | 1310.0 |
0.8020 | 1320.0 |
0.9017 | 1332.0 |
1.0000 | 1345.0 |