Mixture of 1,4-Dioxane + Water

Excel

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

Water

Name
Water
InChI
InChI=1S/H2O/h1H2
InChI Key
XLYOFNOQVPJJNP-UHFFFAOYSA-N
Formula
H2O
SMILES
O
Mol. Weight (g/mol)
18.02
CAS
7732-18-5
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Datasets

  1. Activity coefficient (12)
  2. Henry's Law constant (molality scale), kPa*kg/mol (2)
  3. η - Viscosity, Pa*s (2)
  4. Apparent molar heat capacity, J/K/mol (2)
  5. Pvap - Vapor or sublimation pressure, kPa (2)
  6. n0 - Refractive index (Na D-line) (2)
  7. ρl - Mass density, kg/m3 (10)
  8. csound,fluid - Speed of Sound, m/s (4)
  9. γ - Surface tension liquid-gas, N/m (2)
  10. Partial molar volume, m3/mol (2)

Activity coefficient of 1,4-Dioxane (1) [ref]

Operational condition: Mole fraction = 0 (Liquid)

Temperature, K - Liquid Activity coefficient of 1,4-Dioxane (1) - Liquid
273.35 3.53
278.15 4.0
288.15 4.75
308.15 6.15
318.15 6.82

Activity coefficient of 1,4-Dioxane (1) [ref]

Operational condition: Mole fraction = 0 (Liquid)

Temperature, K - Liquid Activity coefficient of 1,4-Dioxane (1) - Liquid
288.15 5.17
298.15 5.88
308.15 6.7

Activity coefficient of 1,4-Dioxane (1) [ref]

Operational condition: Mole fraction = 0 (Liquid)

Temperature, K - Liquid Activity coefficient of 1,4-Dioxane (1) - Liquid
328.15 7.76
338.15 8.27

Activity coefficient of 1,4-Dioxane (1) [ref]

Fixed Measured
Temperature, K - Liquid Mole fraction of 1,4-Dioxane (1) - Liquid Activity coefficient of 1,4-Dioxane (1) - Liquid
338.15 0.0000 8.22

Activity coefficient of 1,4-Dioxane (1) [ref]

Fixed Measured
Temperature, K - Liquid Mole fraction of 1,4-Dioxane (1) - Liquid Activity coefficient of 1,4-Dioxane (1) - Liquid
348.15 0.0000 8.43

Activity coefficient of 1,4-Dioxane (1) [ref]

Fixed Measured
Temperature, K - Liquid Mole fraction of 1,4-Dioxane (1) - Liquid Activity coefficient of 1,4-Dioxane (1) - Liquid
372.50 0.0000 10.3

Activity coefficient of 1,4-Dioxane (1) [ref]

Operational condition: Mole fraction = 0 (Liquid)

Temperature, K - Liquid Activity coefficient of 1,4-Dioxane (1) - Liquid
273.35 3.53
278.15 4.0
288.15 4.75
308.15 6.15
318.15 6.82

Activity coefficient of 1,4-Dioxane (1) [ref]

Operational condition: Mole fraction = 0 (Liquid)

Temperature, K - Liquid Activity coefficient of 1,4-Dioxane (1) - Liquid
288.15 5.17
298.15 5.88
308.15 6.7

Activity coefficient of 1,4-Dioxane (1) [ref]

Operational condition: Mole fraction = 0 (Liquid)

Temperature, K - Liquid Activity coefficient of 1,4-Dioxane (1) - Liquid
328.15 7.76
338.15 8.27

Activity coefficient of 1,4-Dioxane (1) [ref]

Fixed Measured
Temperature, K - Liquid Mole fraction of 1,4-Dioxane (1) - Liquid Activity coefficient of 1,4-Dioxane (1) - Liquid
338.15 0.0000 8.22

Activity coefficient of 1,4-Dioxane (1) [ref]

Fixed Measured
Temperature, K - Liquid Mole fraction of 1,4-Dioxane (1) - Liquid Activity coefficient of 1,4-Dioxane (1) - Liquid
348.15 0.0000 8.43

Activity coefficient of 1,4-Dioxane (1) [ref]

Fixed Measured
Temperature, K - Liquid Mole fraction of 1,4-Dioxane (1) - Liquid Activity coefficient of 1,4-Dioxane (1) - Liquid
372.50 0.0000 10.3

Henry's Law constant (molality scale), kPa*kg/mol of 1,4-Dioxane (1) [ref]

Operational condition: Mole fraction = 0 (Liquid)

Temperature, K - Liquid Henry's Law constant (molality scale), kPa*kg/mol of 1,4-Dioxane (1) - Liquid
274.15 0.0629
294.65 0.4817
294.65 0.3495
296.15 0.4193
310.15 0.8404
320.15 1.9962
331.15 3.9168

Henry's Law constant (molality scale), kPa*kg/mol of 1,4-Dioxane (1) [ref]

Operational condition: Mole fraction = 0 (Liquid)

Temperature, K - Liquid Henry's Law constant (molality scale), kPa*kg/mol of 1,4-Dioxane (1) - Liquid
274.15 0.0629
294.65 0.4817
294.65 0.3495
296.15 0.4193
310.15 0.8404
320.15 1.9962
331.15 3.9168

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed Measured
Temperature, K - Liquid Mass fraction of Water (2) - Liquid Viscosity, Pa*s - Liquid
303.15 0.0000 0.0010
303.15 0.3523 0.0012
303.15 0.5503 0.0014
303.15 0.6772 0.0016
303.15 0.7654 0.0016
303.15 0.8304 0.0015
303.15 0.8801 0.0014
303.15 0.9195 0.0012
303.15 0.9514 0.0011
303.15 0.9778 0.0009
303.15 1.0000 0.0008
313.15 0.0000 0.0009
313.15 0.3523 0.0010
313.15 0.5503 0.0012
313.15 0.6772 0.0013
313.15 0.7654 0.0013
313.15 0.8304 0.0012
313.15 0.8801 0.0011
313.15 0.9195 0.0010
313.15 0.9514 0.0009
313.15 0.9778 0.0007
313.15 1.0000 0.0006
323.15 0.0000 0.0008
323.15 0.3523 0.0009
323.15 0.5503 0.0010
323.15 0.6772 0.0010
323.15 0.7654 0.0010
323.15 0.8304 0.0010
323.15 0.8801 0.0009
323.15 0.9195 0.0008
323.15 0.9514 0.0007
323.15 0.9778 0.0006
323.15 1.0000 0.0005

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed Measured
Temperature, K - Liquid Mass fraction of Water (2) - Liquid Viscosity, Pa*s - Liquid
303.15 0.0000 0.0010
303.15 0.3523 0.0012
303.15 0.5503 0.0014
303.15 0.6772 0.0016
303.15 0.7654 0.0016
303.15 0.8304 0.0015
303.15 0.8801 0.0014
303.15 0.9195 0.0012
303.15 0.9514 0.0011
303.15 0.9778 0.0009
303.15 1.0000 0.0008
313.15 0.0000 0.0009
313.15 0.3523 0.0010
313.15 0.5503 0.0012
313.15 0.6772 0.0013
313.15 0.7654 0.0013
313.15 0.8304 0.0012
313.15 0.8801 0.0011
313.15 0.9195 0.0010
313.15 0.9514 0.0009
313.15 0.9778 0.0007
313.15 1.0000 0.0006
323.15 0.0000 0.0008
323.15 0.3523 0.0009
323.15 0.5503 0.0010
323.15 0.6772 0.0010
323.15 0.7654 0.0010
323.15 0.8304 0.0010
323.15 0.8801 0.0009
323.15 0.9195 0.0008
323.15 0.9514 0.0007
323.15 0.9778 0.0006
323.15 1.0000 0.0005

Apparent molar heat capacity, J/K/mol [ref]

Operational condition: Pressure, kPa = 350 (Liquid)

Fixed Measured
Temperature, K - Liquid Molality, mol/kg of 1,4-Dioxane (1) - Liquid Apparent molar heat capacity, J/K/mol - Liquid
278.15 0.0150 192.0
278.15 0.0404 189.5
278.15 0.0794 203.9
278.15 0.1988 197.3
278.15 0.4994 191.8
278.15 0.9995 185.3
278.15 1.5006 179.9
278.15 2.0855 173.4
283.15 0.0150 202.0
283.15 0.0404 197.3
283.15 0.0794 211.7
283.15 0.1988 205.8
283.15 0.4994 201.1
283.15 0.9995 195.2
283.15 1.5006 190.8
283.15 2.0855 184.4
288.15 0.0150 214.0
288.15 0.0404 217.5
288.15 0.0794 217.6
288.15 0.1988 212.1
288.15 0.4994 208.2
288.15 0.9995 202.9
288.15 1.5006 198.7
288.15 2.0855 192.8
293.15 0.0150 221.0
293.15 0.0404 220.4
293.15 0.0794 221.9
293.15 0.1988 217.7
293.15 0.4994 214.4
293.15 0.9995 209.5
293.15 1.5006 205.6
293.15 2.0855 200.2
298.15 0.0150 225.0
298.15 0.0404 223.1
298.15 0.0794 225.6
298.15 0.1988 222.8
298.15 0.4994 219.8
298.15 0.9995 215.22
298.15 1.5006 211.4
298.15 2.0855 206.6
303.15 0.0150 229.0
303.15 0.0404 226.8
303.15 0.0794 229.2
303.15 0.1988 227.6
303.15 0.4994 224.6
303.15 0.9995 220.36
303.15 1.5006 216.54
303.15 2.0855 212.5
308.15 0.0150 233.0
308.15 0.0404 229.7
308.15 0.0794 232.4
308.15 0.1988 231.9
308.15 0.4994 229.0
308.15 0.9995 225.05
308.15 1.5006 221.15
308.15 2.0855 217.75
313.15 0.0150 236.0
313.15 0.0404 233.2
313.15 0.0794 236.1
313.15 0.1988 235.9
313.15 0.4994 233.0
313.15 0.9995 229.28
313.15 1.5006 225.51
313.15 2.0855 222.51
318.15 0.0150 240.0
318.15 0.0404 236.7
318.15 0.0794 239.6
318.15 0.1988 239.6
318.15 0.4994 236.8
318.15 0.9995 233.27
318.15 1.5006 229.68
318.15 2.0855 226.98
323.15 0.0150 243.0
323.15 0.0404 240.6
323.15 0.0794 243.1
323.15 0.1988 243.1
323.15 0.4994 240.37
323.15 0.9995 237.05
323.15 1.5006 233.67
323.15 2.0855 231.19
328.15 0.0150 246.2
328.15 0.0404 244.6
328.15 0.0794 246.6
328.15 0.1988 246.6
328.15 0.4994 243.88
328.15 0.9995 240.67
328.15 1.5006 237.45
328.15 2.0855 235.19
333.15 0.0150 249.2
333.15 0.0404 249.5
333.15 0.0794 250.3
333.15 0.1988 250.2
333.15 0.4994 247.43
333.15 0.9995 244.28
333.15 1.5006 241.15
333.15 2.0855 239.16
338.15 0.0150 252.5
338.15 0.0404 254.2
338.15 0.0794 254.0
338.15 0.1988 253.6
338.15 0.4994 250.96
338.15 0.9995 247.85
338.15 1.5006 244.81
338.15 2.0855 243.09
343.15 0.0150 255.0
343.15 0.0404 257.3
343.15 0.0794 257.3
343.15 0.1988 256.8
343.15 0.4994 254.27
343.15 0.9995 251.24
343.15 1.5006 248.29
343.15 2.0855 246.88
348.15 0.0150 257.5
348.15 0.0404 260.2
348.15 0.0794 260.6
348.15 0.1988 259.9
348.15 0.4994 257.59
348.15 0.9995 254.6
348.15 1.5006 251.71
348.15 2.0855 250.67
353.15 0.0150 260.4
353.15 0.0404 263.4
353.15 0.0794 263.7
353.15 0.1988 263.1
353.15 0.4994 260.83
353.15 0.9995 257.83
353.15 1.5006 255.05
353.15 2.0855 254.47
358.15 0.0150 263.3
358.15 0.0404 266.7
358.15 0.0794 267.0
358.15 0.1988 266.3
358.15 0.4994 264.06
358.15 0.9995 261.07
358.15 1.5006 258.33
358.15 2.0855 258.38
363.15 0.0150 266.0
363.15 0.0404 269.9
363.15 0.0794 270.1
363.15 0.1988 269.5
363.15 0.4994 267.24
363.15 0.9995 264.25
363.15 1.5006 261.56
363.15 2.0855 262.4
368.15 0.0150 268.7
368.15 0.0404 272.9
368.15 0.0794 273.0
368.15 0.1988 272.7
368.15 0.4994 270.24
368.15 0.9995 267.23
368.15 1.5006 264.55
368.15 2.0855 266.49
373.15 0.0150 270.9
373.15 0.0404 276.7
373.15 0.0794 276.7
373.15 0.1988 276.0
373.15 0.4994 273.37
373.15 0.9995 270.3
373.15 1.5006 267.6
373.15 2.0855 271.08
378.15 0.0150 273.6
378.15 0.0404 281.4
378.15 0.0794 280.3
378.15 0.1988 279.2
378.15 0.4994 276.36
378.15 0.9995 273.22
378.15 1.5006 270.52
378.15 2.0855 276.42
383.15 0.0150 276.2
383.15 0.0404 285.5
383.15 0.0794 283.9
383.15 0.1988 282.2
383.15 0.4994 279.27
383.15 0.9995 276.04
383.15 1.5006 273.28
383.15 2.0855 283.18
388.15 0.0150 278.4
388.15 0.0404 289.0
388.15 0.0794 287.0
388.15 0.1988 285.1
388.15 0.4994 282.1
388.15 0.9995 278.82
388.15 1.5006 276.05
388.15 2.0855 292.21
393.15 0.0150 279.8
393.15 0.0404 292.4
393.15 0.0794 290.1
393.15 0.1988 287.8
393.15 0.4994 284.73
393.15 0.9995 281.51
393.15 1.5006 279.02
393.15 2.0855 304.31

Apparent molar heat capacity, J/K/mol [ref]

Operational condition: Pressure, kPa = 350 (Liquid)

Fixed Measured
Temperature, K - Liquid Molality, mol/kg of 1,4-Dioxane (1) - Liquid Apparent molar heat capacity, J/K/mol - Liquid
278.15 0.0150 192.0
278.15 0.0404 189.5
278.15 0.0794 203.9
278.15 0.1988 197.3
278.15 0.4994 191.8
278.15 0.9995 185.3
278.15 1.5006 179.9
278.15 2.0855 173.4
283.15 0.0150 202.0
283.15 0.0404 197.3
283.15 0.0794 211.7
283.15 0.1988 205.8
283.15 0.4994 201.1
283.15 0.9995 195.2
283.15 1.5006 190.8
283.15 2.0855 184.4
288.15 0.0150 214.0
288.15 0.0404 217.5
288.15 0.0794 217.6
288.15 0.1988 212.1
288.15 0.4994 208.2
288.15 0.9995 202.9
288.15 1.5006 198.7
288.15 2.0855 192.8
293.15 0.0150 221.0
293.15 0.0404 220.4
293.15 0.0794 221.9
293.15 0.1988 217.7
293.15 0.4994 214.4
293.15 0.9995 209.5
293.15 1.5006 205.6
293.15 2.0855 200.2
298.15 0.0150 225.0
298.15 0.0404 223.1
298.15 0.0794 225.6
298.15 0.1988 222.8
298.15 0.4994 219.8
298.15 0.9995 215.22
298.15 1.5006 211.4
298.15 2.0855 206.6
303.15 0.0150 229.0
303.15 0.0404 226.8
303.15 0.0794 229.2
303.15 0.1988 227.6
303.15 0.4994 224.6
303.15 0.9995 220.36
303.15 1.5006 216.54
303.15 2.0855 212.5
308.15 0.0150 233.0
308.15 0.0404 229.7
308.15 0.0794 232.4
308.15 0.1988 231.9
308.15 0.4994 229.0
308.15 0.9995 225.05
308.15 1.5006 221.15
308.15 2.0855 217.75
313.15 0.0150 236.0
313.15 0.0404 233.2
313.15 0.0794 236.1
313.15 0.1988 235.9
313.15 0.4994 233.0
313.15 0.9995 229.28
313.15 1.5006 225.51
313.15 2.0855 222.51
318.15 0.0150 240.0
318.15 0.0404 236.7
318.15 0.0794 239.6
318.15 0.1988 239.6
318.15 0.4994 236.8
318.15 0.9995 233.27
318.15 1.5006 229.68
318.15 2.0855 226.98
323.15 0.0150 243.0
323.15 0.0404 240.6
323.15 0.0794 243.1
323.15 0.1988 243.1
323.15 0.4994 240.37
323.15 0.9995 237.05
323.15 1.5006 233.67
323.15 2.0855 231.19
328.15 0.0150 246.2
328.15 0.0404 244.6
328.15 0.0794 246.6
328.15 0.1988 246.6
328.15 0.4994 243.88
328.15 0.9995 240.67
328.15 1.5006 237.45
328.15 2.0855 235.19
333.15 0.0150 249.2
333.15 0.0404 249.5
333.15 0.0794 250.3
333.15 0.1988 250.2
333.15 0.4994 247.43
333.15 0.9995 244.28
333.15 1.5006 241.15
333.15 2.0855 239.16
338.15 0.0150 252.5
338.15 0.0404 254.2
338.15 0.0794 254.0
338.15 0.1988 253.6
338.15 0.4994 250.96
338.15 0.9995 247.85
338.15 1.5006 244.81
338.15 2.0855 243.09
343.15 0.0150 255.0
343.15 0.0404 257.3
343.15 0.0794 257.3
343.15 0.1988 256.8
343.15 0.4994 254.27
343.15 0.9995 251.24
343.15 1.5006 248.29
343.15 2.0855 246.88
348.15 0.0150 257.5
348.15 0.0404 260.2
348.15 0.0794 260.6
348.15 0.1988 259.9
348.15 0.4994 257.59
348.15 0.9995 254.6
348.15 1.5006 251.71
348.15 2.0855 250.67
353.15 0.0150 260.4
353.15 0.0404 263.4
353.15 0.0794 263.7
353.15 0.1988 263.1
353.15 0.4994 260.83
353.15 0.9995 257.83
353.15 1.5006 255.05
353.15 2.0855 254.47
358.15 0.0150 263.3
358.15 0.0404 266.7
358.15 0.0794 267.0
358.15 0.1988 266.3
358.15 0.4994 264.06
358.15 0.9995 261.07
358.15 1.5006 258.33
358.15 2.0855 258.38
363.15 0.0150 266.0
363.15 0.0404 269.9
363.15 0.0794 270.1
363.15 0.1988 269.5
363.15 0.4994 267.24
363.15 0.9995 264.25
363.15 1.5006 261.56
363.15 2.0855 262.4
368.15 0.0150 268.7
368.15 0.0404 272.9
368.15 0.0794 273.0
368.15 0.1988 272.7
368.15 0.4994 270.24
368.15 0.9995 267.23
368.15 1.5006 264.55
368.15 2.0855 266.49
373.15 0.0150 270.9
373.15 0.0404 276.7
373.15 0.0794 276.7
373.15 0.1988 276.0
373.15 0.4994 273.37
373.15 0.9995 270.3
373.15 1.5006 267.6
373.15 2.0855 271.08
378.15 0.0150 273.6
378.15 0.0404 281.4
378.15 0.0794 280.3
378.15 0.1988 279.2
378.15 0.4994 276.36
378.15 0.9995 273.22
378.15 1.5006 270.52
378.15 2.0855 276.42
383.15 0.0150 276.2
383.15 0.0404 285.5
383.15 0.0794 283.9
383.15 0.1988 282.2
383.15 0.4994 279.27
383.15 0.9995 276.04
383.15 1.5006 273.28
383.15 2.0855 283.18
388.15 0.0150 278.4
388.15 0.0404 289.0
388.15 0.0794 287.0
388.15 0.1988 285.1
388.15 0.4994 282.1
388.15 0.9995 278.82
388.15 1.5006 276.05
388.15 2.0855 292.21
393.15 0.0150 279.8
393.15 0.0404 292.4
393.15 0.0794 290.1
393.15 0.1988 287.8
393.15 0.4994 284.73
393.15 0.9995 281.51
393.15 1.5006 279.02
393.15 2.0855 304.31

Vapor or sublimation pressure, kPa [ref]

Fixed Measured
Temperature, K - Liquid Mole fraction of 1,4-Dioxane (1) - Liquid Vapor or sublimation pressure, kPa - Liquid
288.15 0.0500 2.35
288.15 0.1000 2.71
288.15 0.1700 2.98
288.15 0.5000 3.66
288.15 0.7000 3.75
288.15 0.9000 3.39
298.15 0.0500 4.16
298.15 0.1000 4.93
298.15 0.1700 5.48
298.15 0.5000 6.36
298.15 0.7000 6.36
298.15 0.9000 6.03
308.15 0.0500 7.24
308.15 0.1000 8.62
308.15 0.1700 9.70
308.15 0.5000 10.73
308.15 0.7000 10.83
308.15 0.9000 9.91

Vapor or sublimation pressure, kPa [ref]

Fixed Measured
Temperature, K - Liquid Mole fraction of 1,4-Dioxane (1) - Liquid Vapor or sublimation pressure, kPa - Liquid
288.15 0.0500 2.35
288.15 0.1000 2.71
288.15 0.1700 2.98
288.15 0.5000 3.66
288.15 0.7000 3.75
288.15 0.9000 3.39
298.15 0.0500 4.16
298.15 0.1000 4.93
298.15 0.1700 5.48
298.15 0.5000 6.36
298.15 0.7000 6.36
298.15 0.9000 6.03
308.15 0.0500 7.24
308.15 0.1000 8.62
308.15 0.1700 9.70
308.15 0.5000 10.73
308.15 0.7000 10.83
308.15 0.9000 9.91

Refractive index (Na D-line) [ref]

Operational conditions:

Mole fraction of Water (2) - Liquid Refractive index (Na D-line) - Liquid
0.0000 1.4181
0.3523 1.4116
0.5503 1.4046
0.6772 1.3972
0.7654 1.391
0.8304 1.3865
0.8801 1.3798
0.9195 1.3698
0.9514 1.3517
0.9778 1.3417
1.0000 1.3326

Refractive index (Na D-line) [ref]

Operational conditions:

Mole fraction of Water (2) - Liquid Refractive index (Na D-line) - Liquid
0.0000 1.4181
0.3523 1.4116
0.5503 1.4046
0.6772 1.3972
0.7654 1.391
0.8304 1.3865
0.8801 1.3798
0.9195 1.3698
0.9514 1.3517
0.9778 1.3417
1.0000 1.3326

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Water (2) - Liquid Mass density, kg/m3 - Liquid
288.15 0.0348 1039.25
288.15 0.0430 1039.3
288.15 0.0630 1039.39
288.15 0.0889 1039.69
288.15 0.1109 1039.8
288.15 0.1556 1040.09
288.15 0.1993 1040.88
288.15 0.2577 1041.6
288.15 0.3017 1042.14
288.15 0.3508 1042.6
288.15 0.4013 1043.4
288.15 0.4489 1043.84
288.15 0.5006 1044.46
288.15 0.5511 1045.07
288.15 0.6022 1045.22
288.15 0.6491 1045.78
288.15 0.7003 1045.49
288.15 0.7495 1044.83
288.15 0.7999 1042.65
288.15 0.8461 1038.95
288.15 0.9001 1030.74
288.15 0.9196 1027.33
288.15 0.9500 1018.57
288.15 0.9694 1011.99
288.15 0.9974 1000.05
293.15 0.0348 1033.65
293.15 0.0430 1033.66
293.15 0.0630 1033.81
293.15 0.0889 1034.1
293.15 0.1109 1034.27
293.15 0.1556 1034.59
293.15 0.1993 1035.46
293.15 0.2577 1036.22
293.15 0.3017 1036.86
293.15 0.3508 1037.37
293.15 0.4013 1038.31
293.15 0.4489 1038.87
293.15 0.5006 1039.54
293.15 0.5511 1040.29
293.15 0.6022 1040.55
293.15 0.6491 1041.25
293.15 0.7003 1040.92
293.15 0.7495 1040.66
293.15 0.7999 1038.82
293.15 0.8461 1034.45
293.15 0.9001 1027.39
293.15 0.9196 1024.97
293.15 0.9500 1016.49
293.15 0.9694 1009.89
293.15 0.9974 999.11
298.15 0.0348 1028.03
298.15 0.0430 1028.05
298.15 0.0630 1028.19
298.15 0.0889 1028.52
298.15 0.1109 1028.7
298.15 0.1556 1029.07
298.15 0.1993 1029.96
298.15 0.2577 1030.83
298.15 0.3017 1031.53
298.15 0.3508 1032.13
298.15 0.4013 1033.16
298.15 0.4489 1033.81
298.15 0.5006 1034.58
298.15 0.5511 1035.43
298.15 0.6022 1035.85
298.15 0.6491 1036.65
298.15 0.7003 1036.89
298.15 0.7495 1036.49
298.15 0.7999 1034.81
298.15 0.8461 1032.25
298.15 0.9001 1024.54
298.15 0.9196 1022.09
298.15 0.9500 1013.6
298.15 0.9694 1008.3
298.15 0.9974 997.91
303.15 0.0348 1022.4
303.15 0.0430 1022.44
303.15 0.0630 1022.58
303.15 0.0889 1022.95
303.15 0.1109 1023.12
303.15 0.1556 1023.55
303.15 0.1993 1024.48
303.15 0.2577 1025.42
303.15 0.3017 1026.19
303.15 0.3508 1026.86
303.15 0.4013 1027.98
303.15 0.4489 1028.72
303.15 0.5006 1029.6
303.15 0.5511 1030.54
303.15 0.6022 1031.1
303.15 0.6491 1032.01
303.15 0.7003 1032.43
303.15 0.7495 1032.27
303.15 0.7999 1030.74
303.15 0.8461 1028.98
303.15 0.9001 1021.62
303.15 0.9196 1018.06
303.15 0.9500 1010.87
303.15 0.9694 1006.43
303.15 0.9974 996.4

Mass density, kg/m3 [ref]

Operational conditions:

Mole fraction of 1,4-Dioxane (1) - Liquid Mass density, kg/m3 - Liquid
0.0000 999.9
0.0180 1008.9
0.0480 1021.0
0.0770 1031.1
0.0960 1035.1
0.2400 1051.2
0.3870 1052.8
0.5950 1051.7

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 350 (Liquid)

Fixed Measured
Molality, mol/kg of 1,4-Dioxane (1) - Liquid Temperature, K - Liquid Mass density, kg/m3 - Liquid
0.0150 278.15 1000.24
0.0150 283.15 999.96
0.0150 288.15 999.34
0.0150 298.15 997.3
0.0150 308.15 994.28
0.0150 318.15 990.46
0.0150 328.15 985.87
0.0150 338.15 980.72
0.0150 348.15 975.03
0.0150 358.15 968.78
0.0150 368.15 962.06
0.0404 278.15 1000.45
0.0404 283.15 1000.14
0.0404 288.15 999.49
0.0404 298.15 997.4
0.0404 308.15 994.38
0.0404 318.15 990.6
0.0404 328.15 986.04
0.0404 338.15 980.88
0.0404 348.15 975.17
0.0404 358.15 968.89
0.0404 368.15 962.18
0.0794 278.15 1000.81
0.0794 283.15 1000.47
0.0794 288.15 999.81
0.0794 298.15 997.67
0.0794 308.15 994.62
0.0794 318.15 990.78
0.0794 328.15 986.26
0.0794 338.15 981.07
0.0794 348.15 975.33
0.0794 358.15 969.05
0.0794 368.15 962.36
0.1988 278.15 1001.96
0.1988 283.15 1001.55
0.1988 288.15 1000.83
0.1988 298.15 998.59
0.1988 308.15 995.43
0.1988 318.15 991.45
0.1988 328.15 986.87
0.1988 338.15 981.64
0.1988 348.15 975.85
0.1988 358.15 969.52
0.1988 368.15 962.71
0.4994 278.15 1004.65
0.4994 283.15 1004.05
0.4994 288.15 1003.16
0.4994 298.15 1000.65
0.4994 308.15 997.36
0.4994 318.15 993.25
0.4994 328.15 988.44
0.4994 338.15 983.05
0.4994 348.15 977.13
0.4994 358.15 970.67
0.4994 368.15 963.75
0.9995 278.15 1009.0
0.9995 283.15 1008.13
0.9995 288.15 1006.99
0.9995 298.15 1004.04
0.9995 308.15 1000.26
0.9995 318.15 995.89
0.9995 328.15 990.82
0.9995 338.15 985.18
0.9995 348.15 979.04
0.9995 358.15 972.36
0.9995 368.15 965.23
1.5006 278.15 1013.02
1.5006 283.15 1011.89
1.5006 288.15 1010.54
1.5006 298.15 1007.17
1.5006 308.15 1003.06
1.5006 318.15 998.28
1.5006 328.15 992.92
1.5006 338.15 987.12
1.5006 348.15 980.73
1.5006 358.15 973.87
1.5006 368.15 966.53
2.0855 278.15 1017.28
2.0855 283.15 1015.86
2.0855 288.15 1014.24
2.0855 298.15 1010.31
2.0855 308.15 1005.88
2.0855 318.15 1000.84
2.0855 328.15 995.21
2.0855 338.15 989.07
2.0855 348.15 982.42
2.0855 358.15 975.27
2.0855 368.15 967.78

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed Measured
Mole fraction of Water (2) - Liquid Temperature, K - Liquid Mass density, kg/m3 - Liquid
0.0000 303.15 1024.63
0.0000 313.15 1013.3
0.0000 323.15 1001.9
0.3523 303.15 1029.1
0.3523 313.15 1018.5
0.3523 323.15 1007.8
0.5503 303.15 1032.4
0.5503 313.15 1022.6
0.5503 323.15 1012.5
0.6772 303.15 1033.83
0.6772 313.15 1024.7
0.6772 323.15 1015.2
0.7654 303.15 1033.22
0.7654 313.15 1024.7
0.7654 323.15 1015.9
0.8304 303.15 1030.5
0.8304 313.15 1022.7
0.8304 323.15 1014.6
0.8801 303.15 1025.6
0.8801 313.15 1018.7
0.8801 323.15 1011.4
0.9195 303.15 1019.51
0.9195 313.15 1013.4
0.9195 323.15 1006.9
0.9514 303.15 1012.1
0.9514 313.15 1006.9
0.9514 323.15 1001.3
0.9778 303.15 1004.1
0.9778 313.15 999.8
0.9778 323.15 994.9
1.0000 303.15 995.71
1.0000 313.15 992.3
1.0000 323.15 988.1

Mass density, kg/m3 [ref]

Operational conditions:

Molality, mol/kg of Water (2) - Liquid Mass density, kg/m3 - Liquid
0.0000 1028.337
0.0717 1028.349
0.1214 1028.361
0.1625 1028.371
0.2272 1028.39
0.3262 1028.424
0.4214 1028.463
0.6512 1028.573
0.8375 1028.675
1.0222 1028.782

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Water (2) - Liquid Mass density, kg/m3 - Liquid
288.15 0.0348 1039.25
288.15 0.0430 1039.3
288.15 0.0630 1039.39
288.15 0.0889 1039.69
288.15 0.1109 1039.8
288.15 0.1556 1040.09
288.15 0.1993 1040.88
288.15 0.2577 1041.6
288.15 0.3017 1042.14
288.15 0.3508 1042.6
288.15 0.4013 1043.4
288.15 0.4489 1043.84
288.15 0.5006 1044.46
288.15 0.5511 1045.07
288.15 0.6022 1045.22
288.15 0.6491 1045.78
288.15 0.7003 1045.49
288.15 0.7495 1044.83
288.15 0.7999 1042.65
288.15 0.8461 1038.95
288.15 0.9001 1030.74
288.15 0.9196 1027.33
288.15 0.9500 1018.57
288.15 0.9694 1011.99
288.15 0.9974 1000.05
293.15 0.0348 1033.65
293.15 0.0430 1033.66
293.15 0.0630 1033.81
293.15 0.0889 1034.1
293.15 0.1109 1034.27
293.15 0.1556 1034.59
293.15 0.1993 1035.46
293.15 0.2577 1036.22
293.15 0.3017 1036.86
293.15 0.3508 1037.37
293.15 0.4013 1038.31
293.15 0.4489 1038.87
293.15 0.5006 1039.54
293.15 0.5511 1040.29
293.15 0.6022 1040.55
293.15 0.6491 1041.25
293.15 0.7003 1040.92
293.15 0.7495 1040.66
293.15 0.7999 1038.82
293.15 0.8461 1034.45
293.15 0.9001 1027.39
293.15 0.9196 1024.97
293.15 0.9500 1016.49
293.15 0.9694 1009.89
293.15 0.9974 999.11
298.15 0.0348 1028.03
298.15 0.0430 1028.05
298.15 0.0630 1028.19
298.15 0.0889 1028.52
298.15 0.1109 1028.7
298.15 0.1556 1029.07
298.15 0.1993 1029.96
298.15 0.2577 1030.83
298.15 0.3017 1031.53
298.15 0.3508 1032.13
298.15 0.4013 1033.16
298.15 0.4489 1033.81
298.15 0.5006 1034.58
298.15 0.5511 1035.43
298.15 0.6022 1035.85
298.15 0.6491 1036.65
298.15 0.7003 1036.89
298.15 0.7495 1036.49
298.15 0.7999 1034.81
298.15 0.8461 1032.25
298.15 0.9001 1024.54
298.15 0.9196 1022.09
298.15 0.9500 1013.6
298.15 0.9694 1008.3
298.15 0.9974 997.91
303.15 0.0348 1022.4
303.15 0.0430 1022.44
303.15 0.0630 1022.58
303.15 0.0889 1022.95
303.15 0.1109 1023.12
303.15 0.1556 1023.55
303.15 0.1993 1024.48
303.15 0.2577 1025.42
303.15 0.3017 1026.19
303.15 0.3508 1026.86
303.15 0.4013 1027.98
303.15 0.4489 1028.72
303.15 0.5006 1029.6
303.15 0.5511 1030.54
303.15 0.6022 1031.1
303.15 0.6491 1032.01
303.15 0.7003 1032.43
303.15 0.7495 1032.27
303.15 0.7999 1030.74
303.15 0.8461 1028.98
303.15 0.9001 1021.62
303.15 0.9196 1018.06
303.15 0.9500 1010.87
303.15 0.9694 1006.43
303.15 0.9974 996.4

Mass density, kg/m3 [ref]

Operational conditions:

Mole fraction of 1,4-Dioxane (1) - Liquid Mass density, kg/m3 - Liquid
0.0000 999.9
0.0180 1008.9
0.0480 1021.0
0.0770 1031.1
0.0960 1035.1
0.2400 1051.2
0.3870 1052.8
0.5950 1051.7

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 350 (Liquid)

Fixed Measured
Molality, mol/kg of 1,4-Dioxane (1) - Liquid Temperature, K - Liquid Mass density, kg/m3 - Liquid
0.0150 278.15 1000.24
0.0150 283.15 999.96
0.0150 288.15 999.34
0.0150 298.15 997.3
0.0150 308.15 994.28
0.0150 318.15 990.46
0.0150 328.15 985.87
0.0150 338.15 980.72
0.0150 348.15 975.03
0.0150 358.15 968.78
0.0150 368.15 962.06
0.0404 278.15 1000.45
0.0404 283.15 1000.14
0.0404 288.15 999.49
0.0404 298.15 997.4
0.0404 308.15 994.38
0.0404 318.15 990.6
0.0404 328.15 986.04
0.0404 338.15 980.88
0.0404 348.15 975.17
0.0404 358.15 968.89
0.0404 368.15 962.18
0.0794 278.15 1000.81
0.0794 283.15 1000.47
0.0794 288.15 999.81
0.0794 298.15 997.67
0.0794 308.15 994.62
0.0794 318.15 990.78
0.0794 328.15 986.26
0.0794 338.15 981.07
0.0794 348.15 975.33
0.0794 358.15 969.05
0.0794 368.15 962.36
0.1988 278.15 1001.96
0.1988 283.15 1001.55
0.1988 288.15 1000.83
0.1988 298.15 998.59
0.1988 308.15 995.43
0.1988 318.15 991.45
0.1988 328.15 986.87
0.1988 338.15 981.64
0.1988 348.15 975.85
0.1988 358.15 969.52
0.1988 368.15 962.71
0.4994 278.15 1004.65
0.4994 283.15 1004.05
0.4994 288.15 1003.16
0.4994 298.15 1000.65
0.4994 308.15 997.36
0.4994 318.15 993.25
0.4994 328.15 988.44
0.4994 338.15 983.05
0.4994 348.15 977.13
0.4994 358.15 970.67
0.4994 368.15 963.75
0.9995 278.15 1009.0
0.9995 283.15 1008.13
0.9995 288.15 1006.99
0.9995 298.15 1004.04
0.9995 308.15 1000.26
0.9995 318.15 995.89
0.9995 328.15 990.82
0.9995 338.15 985.18
0.9995 348.15 979.04
0.9995 358.15 972.36
0.9995 368.15 965.23
1.5006 278.15 1013.02
1.5006 283.15 1011.89
1.5006 288.15 1010.54
1.5006 298.15 1007.17
1.5006 308.15 1003.06
1.5006 318.15 998.28
1.5006 328.15 992.92
1.5006 338.15 987.12
1.5006 348.15 980.73
1.5006 358.15 973.87
1.5006 368.15 966.53
2.0855 278.15 1017.28
2.0855 283.15 1015.86
2.0855 288.15 1014.24
2.0855 298.15 1010.31
2.0855 308.15 1005.88
2.0855 318.15 1000.84
2.0855 328.15 995.21
2.0855 338.15 989.07
2.0855 348.15 982.42
2.0855 358.15 975.27
2.0855 368.15 967.78

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed Measured
Mole fraction of Water (2) - Liquid Temperature, K - Liquid Mass density, kg/m3 - Liquid
0.0000 303.15 1024.63
0.0000 313.15 1013.3
0.0000 323.15 1001.9
0.3523 303.15 1029.1
0.3523 313.15 1018.5
0.3523 323.15 1007.8
0.5503 303.15 1032.4
0.5503 313.15 1022.6
0.5503 323.15 1012.5
0.6772 303.15 1033.83
0.6772 313.15 1024.7
0.6772 323.15 1015.2
0.7654 303.15 1033.22
0.7654 313.15 1024.7
0.7654 323.15 1015.9
0.8304 303.15 1030.5
0.8304 313.15 1022.7
0.8304 323.15 1014.6
0.8801 303.15 1025.6
0.8801 313.15 1018.7
0.8801 323.15 1011.4
0.9195 303.15 1019.51
0.9195 313.15 1013.4
0.9195 323.15 1006.9
0.9514 303.15 1012.1
0.9514 313.15 1006.9
0.9514 323.15 1001.3
0.9778 303.15 1004.1
0.9778 313.15 999.8
0.9778 323.15 994.9
1.0000 303.15 995.71
1.0000 313.15 992.3
1.0000 323.15 988.1

Mass density, kg/m3 [ref]

Operational conditions:

Molality, mol/kg of Water (2) - Liquid Mass density, kg/m3 - Liquid
0.0000 1028.337
0.0717 1028.349
0.1214 1028.361
0.1625 1028.371
0.2272 1028.39
0.3262 1028.424
0.4214 1028.463
0.6512 1028.573
0.8375 1028.675
1.0222 1028.782

Speed of sound, m/s [ref]

Operational conditions:

Mole fraction of 1,4-Dioxane (1) - Liquid Speed of sound, m/s - Liquid
0.0000 1430.4
0.0180 1490.0
0.0480 1544.4
0.0770 1580.0
0.0960 1590.4
0.2400 1587.6
0.3870 1531.6
0.5950 1479.4

Speed of sound, m/s [ref]

Operational conditions:

Molality, mol/kg of Water (2) - Liquid Speed of sound, m/s - Liquid
0.0000 1346.3
0.0717 1347.1
0.1214 1347.8
0.1625 1348.4
0.2272 1349.2
0.3262 1350.0
0.4214 1350.9
0.6512 1353.0
0.8375 1354.8
1.0222 1356.5

Speed of sound, m/s [ref]

Operational conditions:

Mole fraction of 1,4-Dioxane (1) - Liquid Speed of sound, m/s - Liquid
0.0000 1430.4
0.0180 1490.0
0.0480 1544.4
0.0770 1580.0
0.0960 1590.4
0.2400 1587.6
0.3870 1531.6
0.5950 1479.4

Speed of sound, m/s [ref]

Operational conditions:

Molality, mol/kg of Water (2) - Liquid Speed of sound, m/s - Liquid
0.0000 1346.3
0.0717 1347.1
0.1214 1347.8
0.1625 1348.4
0.2272 1349.2
0.3262 1350.0
0.4214 1350.9
0.6512 1353.0
0.8375 1354.8
1.0222 1356.5

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

Operational condition: Temperature, K = 298.15 (Liquid)

Volume fraction of 1,4-Dioxane (1) - Liquid Surface tension liquid-gas, N/m - Liquid
0.0000 0.0718
0.1000 0.0540
0.2000 0.0520
0.3000 0.0466

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

Operational condition: Temperature, K = 298.15 (Liquid)

Volume fraction of 1,4-Dioxane (1) - Liquid Surface tension liquid-gas, N/m - Liquid
0.0000 0.0718
0.1000 0.0540
0.2000 0.0520
0.3000 0.0466

Partial molar volume, m3/mol of 1,4-Dioxane (1) [ref]

Operational condition: Mole fraction = 0 (Liquid)

Fixed Measured
Temperature, K - Liquid Pressure, kPa - Liquid Partial molar volume, m3/mol of 1,4-Dioxane (1) - Liquid
298.16 15030.00 0.0001
298.16 30070.00 0.0001
318.16 15030.00 0.0001
318.16 30050.00 0.0001
338.15 15050.00 0.0001
338.15 30040.00 0.0001
358.17 15020.00 0.0001
358.17 30020.00 0.0001
373.18 30040.00 0.0001
373.19 15040.00 0.0001
398.18 2020.00 0.0001
398.18 15040.00 0.0001
398.18 30060.00 0.0001
423.17 2040.00 0.0001
423.17 15020.00 0.0001
423.18 30050.00 0.0001
448.16 2060.00 0.0001
448.17 15040.00 0.0001
448.17 30060.00 0.0001
473.17 15030.00 0.0001
473.17 30040.00 0.0001
473.18 2070.00 0.0001
498.16 3000.00 0.0001
498.16 15030.00 0.0001
498.17 30060.00 0.0001
523.14 5010.00 0.0001
523.15 15020.00 0.0001
523.15 30030.00 0.0001
548.21 7080.00 0.0001
548.21 15050.00 0.0001
548.22 30020.00 0.0001
573.17 30060.00 0.0001
573.18 10180.00 0.0001
573.18 15070.00 0.0001

Partial molar volume, m3/mol of 1,4-Dioxane (1) [ref]

Operational condition: Mole fraction = 0 (Liquid)

Fixed Measured
Temperature, K - Liquid Pressure, kPa - Liquid Partial molar volume, m3/mol of 1,4-Dioxane (1) - Liquid
298.16 15030.00 0.0001
298.16 30070.00 0.0001
318.16 15030.00 0.0001
318.16 30050.00 0.0001
338.15 15050.00 0.0001
338.15 30040.00 0.0001
358.17 15020.00 0.0001
358.17 30020.00 0.0001
373.18 30040.00 0.0001
373.19 15040.00 0.0001
398.18 2020.00 0.0001
398.18 15040.00 0.0001
398.18 30060.00 0.0001
423.17 2040.00 0.0001
423.17 15020.00 0.0001
423.18 30050.00 0.0001
448.16 2060.00 0.0001
448.17 15040.00 0.0001
448.17 30060.00 0.0001
473.17 15030.00 0.0001
473.17 30040.00 0.0001
473.18 2070.00 0.0001
498.16 3000.00 0.0001
498.16 15030.00 0.0001
498.17 30060.00 0.0001
523.14 5010.00 0.0001
523.15 15020.00 0.0001
523.15 30030.00 0.0001
548.21 7080.00 0.0001
548.21 15050.00 0.0001
548.22 30020.00 0.0001
573.17 30060.00 0.0001
573.18 10180.00 0.0001
573.18 15070.00 0.0001

Sources