Operational condition: Mole fraction = 0 (Liquid)
Temperature, K - Liquid | Activity coefficient of Tetrahydropyran (1) - Liquid |
---|---|
273.35 | 39.6 |
283.15 | 44.9 |
Operational condition: Mole fraction = 0 (Liquid)
Temperature, K - Liquid | Activity coefficient of Tetrahydropyran (1) - Liquid |
---|---|
288.15 | 58.0 |
298.15 | 70.5 |
308.15 | 83.4 |
318.15 | 96.2 |
328.15 | 107.5 |
Operational condition: Mole fraction = 0 (Liquid)
Temperature, K - Liquid | Activity coefficient of Tetrahydropyran (1) - Liquid |
---|---|
273.35 | 39.6 |
283.15 | 44.9 |
Operational condition: Mole fraction = 0 (Liquid)
Temperature, K - Liquid | Activity coefficient of Tetrahydropyran (1) - Liquid |
---|---|
288.15 | 58.0 |
298.15 | 70.5 |
308.15 | 83.4 |
318.15 | 96.2 |
328.15 | 107.5 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 | Interfacial tension, N/m - Liquid mixture 1 |
---|---|
278.15 | 0.0046 |
288.15 | 0.0052 |
298.15 | 0.0058 |
308.15 | 0.0063 |
318.15 | 0.0067 |
328.15 | 0.0073 |
338.15 | 0.0075 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 | Interfacial tension, N/m - Liquid mixture 1 |
---|---|
278.15 | 0.0046 |
288.15 | 0.0052 |
298.15 | 0.0058 |
308.15 | 0.0063 |
318.15 | 0.0067 |
328.15 | 0.0073 |
338.15 | 0.0075 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 | Mass density, kg/m3 - Liquid mixture 1 |
---|---|
278.15 | 997.68 |
288.15 | 995.72 |
298.15 | 993.18 |
308.15 | 990.25 |
318.15 | 986.57 |
328.15 | 982.26 |
338.15 | 977.44 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 2)
Temperature, K - Liquid mixture 2 | Mass density, kg/m3 - Liquid mixture 2 |
---|---|
278.15 | 903.11 |
288.15 | 893.25 |
298.15 | 883.58 |
308.15 | 873.71 |
318.15 | 863.97 |
328.15 | 854.1 |
338.15 | 844.19 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 | Mass density, kg/m3 - Liquid mixture 1 |
---|---|
278.15 | 997.68 |
288.15 | 995.72 |
298.15 | 993.18 |
308.15 | 990.25 |
318.15 | 986.57 |
328.15 | 982.26 |
338.15 | 977.44 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 2)
Temperature, K - Liquid mixture 2 | Mass density, kg/m3 - Liquid mixture 2 |
---|---|
278.15 | 903.11 |
288.15 | 893.25 |
298.15 | 883.58 |
308.15 | 873.71 |
318.15 | 863.97 |
328.15 | 854.1 |
338.15 | 844.19 |
Operational condition: Mole fraction = 0 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Pressure, kPa - Liquid | Partial molar volume, m3/mol of Tetrahydropyran (1) - Liquid |
298.16 | 15040.00 | 0.0001 |
298.16 | 30080.00 | 0.0001 |
318.16 | 15040.00 | 0.0001 |
318.16 | 30060.00 | 0.0001 |
338.15 | 15050.00 | 0.0001 |
338.15 | 30040.00 | 0.0001 |
358.17 | 30020.00 | 0.0001 |
358.18 | 15050.00 | 0.0001 |
373.18 | 30040.00 | 0.0001 |
373.19 | 15030.00 | 0.0001 |
398.18 | 2030.00 | 0.0001 |
398.18 | 15030.00 | 0.0001 |
398.18 | 30050.00 | 0.0001 |
423.17 | 2040.00 | 0.0001 |
423.17 | 15060.00 | 0.0001 |
423.18 | 30050.00 | 0.0001 |
448.16 | 2060.00 | 0.0001 |
448.16 | 30030.00 | 0.0001 |
448.17 | 15050.00 | 0.0001 |
473.17 | 30040.00 | 0.0001 |
473.18 | 2070.00 | 0.0001 |
473.18 | 15030.00 | 0.0001 |
498.16 | 2990.00 | 0.0001 |
498.17 | 15030.00 | 0.0001 |
498.17 | 30060.00 | 0.0001 |
523.14 | 5020.00 | 0.0001 |
523.14 | 14990.00 | 0.0001 |
523.14 | 30030.00 | 0.0001 |
548.19 | 7050.00 | 0.0002 |
548.20 | 15040.00 | 0.0001 |
548.20 | 30040.00 | 0.0001 |
573.17 | 30030.00 | 0.0002 |
573.18 | 10170.00 | 0.0002 |
573.18 | 15020.00 | 0.0002 |
Operational condition: Mole fraction = 0 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Pressure, kPa - Liquid | Partial molar volume, m3/mol of Tetrahydropyran (1) - Liquid |
298.16 | 15040.00 | 0.0001 |
298.16 | 30080.00 | 0.0001 |
318.16 | 15040.00 | 0.0001 |
318.16 | 30060.00 | 0.0001 |
338.15 | 15050.00 | 0.0001 |
338.15 | 30040.00 | 0.0001 |
358.17 | 30020.00 | 0.0001 |
358.18 | 15050.00 | 0.0001 |
373.18 | 30040.00 | 0.0001 |
373.19 | 15030.00 | 0.0001 |
398.18 | 2030.00 | 0.0001 |
398.18 | 15030.00 | 0.0001 |
398.18 | 30050.00 | 0.0001 |
423.17 | 2040.00 | 0.0001 |
423.17 | 15060.00 | 0.0001 |
423.18 | 30050.00 | 0.0001 |
448.16 | 2060.00 | 0.0001 |
448.16 | 30030.00 | 0.0001 |
448.17 | 15050.00 | 0.0001 |
473.17 | 30040.00 | 0.0001 |
473.18 | 2070.00 | 0.0001 |
473.18 | 15030.00 | 0.0001 |
498.16 | 2990.00 | 0.0001 |
498.17 | 15030.00 | 0.0001 |
498.17 | 30060.00 | 0.0001 |
523.14 | 5020.00 | 0.0001 |
523.14 | 14990.00 | 0.0001 |
523.14 | 30030.00 | 0.0001 |
548.19 | 7050.00 | 0.0002 |
548.20 | 15040.00 | 0.0001 |
548.20 | 30040.00 | 0.0001 |
573.17 | 30030.00 | 0.0002 |
573.18 | 10170.00 | 0.0002 |
573.18 | 15020.00 | 0.0002 |