Mixture of 1-Butanol + 1,4-Dioxane

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1-Butanol

Name
1-Butanol
InChI
InChI=1S/C4H10O/c1-2-3-4-5/h5H,2-4H2,1H3
InChI Key
LRHPLDYGYMQRHN-UHFFFAOYSA-N
Formula
C4H10O
SMILES
CCCCO
Mol. Weight (g/mol)
74.12
CAS
71-36-3

1,4-Dioxane

Name
1,4-Dioxane
InChI
InChI=1S/C4H8O2/c1-2-6-4-3-5-1/h1-4H2
InChI Key
RYHBNJHYFVUHQT-UHFFFAOYSA-N
Formula
C4H8O2
SMILES
C1COCCO1
Mol. Weight (g/mol)
88.11
CAS
123-91-1
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Datasets

  1. Mole fraction (2)
  2. η - Viscosity, Pa*s (4)
  3. Pvap - Vapor or sublimation pressure, kPa (2)
  4. n0 - Refractive index (Na D-line) (2)
  5. ρl - Mass density, kg/m3 (4)
  6. csound,fluid - Speed of Sound, m/s (2)

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

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

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

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

Viscosity, Pa*s [ref]

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

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
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

Viscosity, Pa*s [ref]

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

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
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

Vapor or sublimation pressure, kPa [ref]

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

Vapor or sublimation pressure, kPa [ref]

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

Refractive index (Na D-line) [ref]

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

Refractive index (Na D-line) [ref]

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

Mass density, kg/m3 [ref]

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

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
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

Mass density, kg/m3 [ref]

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

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
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

Speed of sound, m/s [ref]

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

Speed of sound, m/s [ref]

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

Sources