Datasets
-
Activity coefficient (8)
-
Henry's Law constant (mole fraction scale), kPa (2)
-
Apparent molar heat capacity, J/K/mol (2)
-
ρl - Mass density, kg/m3 (2)
-
γ - Surface tension liquid-gas, N/m (2)
Activity coefficient of Ethane, 1,2-dimethoxy- (1)
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethane, 1,2-dimethoxy- (1) - Liquid |
Activity coefficient of Ethane, 1,2-dimethoxy- (1) - Liquid |
318.15 |
0.0000 |
7.25 |
Activity coefficient of Ethane, 1,2-dimethoxy- (1)
[ref]
Operational condition: Mole fraction =
0 (Liquid)
Temperature, K - Liquid |
Activity coefficient of Ethane, 1,2-dimethoxy- (1) - Liquid |
328.15 |
9.12 |
328.15 |
8.81 |
338.15 |
11.2 |
338.15 |
11.1 |
Activity coefficient of Ethane, 1,2-dimethoxy- (1)
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethane, 1,2-dimethoxy- (1) - Liquid |
Activity coefficient of Ethane, 1,2-dimethoxy- (1) - Liquid |
348.15 |
0.0000 |
12.2 |
Activity coefficient of Ethane, 1,2-dimethoxy- (1)
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethane, 1,2-dimethoxy- (1) - Liquid |
Activity coefficient of Ethane, 1,2-dimethoxy- (1) - Liquid |
372.50 |
0.0000 |
14.9 |
Activity coefficient of Ethane, 1,2-dimethoxy- (1)
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethane, 1,2-dimethoxy- (1) - Liquid |
Activity coefficient of Ethane, 1,2-dimethoxy- (1) - Liquid |
318.15 |
0.0000 |
7.25 |
Activity coefficient of Ethane, 1,2-dimethoxy- (1)
[ref]
Operational condition: Mole fraction =
0 (Liquid)
Temperature, K - Liquid |
Activity coefficient of Ethane, 1,2-dimethoxy- (1) - Liquid |
328.15 |
9.12 |
328.15 |
8.81 |
338.15 |
11.2 |
338.15 |
11.1 |
Activity coefficient of Ethane, 1,2-dimethoxy- (1)
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethane, 1,2-dimethoxy- (1) - Liquid |
Activity coefficient of Ethane, 1,2-dimethoxy- (1) - Liquid |
348.15 |
0.0000 |
12.2 |
Activity coefficient of Ethane, 1,2-dimethoxy- (1)
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethane, 1,2-dimethoxy- (1) - Liquid |
Activity coefficient of Ethane, 1,2-dimethoxy- (1) - Liquid |
372.50 |
0.0000 |
14.9 |
Henry's Law constant (mole fraction scale), kPa of Ethane, 1,2-dimethoxy- (1)
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethane, 1,2-dimethoxy- (1) - Liquid |
Henry's Law constant (mole fraction scale), kPa of Ethane, 1,2-dimethoxy- (1) - Liquid |
293.20 |
0.0000 |
26.0 |
Henry's Law constant (mole fraction scale), kPa of Ethane, 1,2-dimethoxy- (1)
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethane, 1,2-dimethoxy- (1) - Liquid |
Henry's Law constant (mole fraction scale), kPa of Ethane, 1,2-dimethoxy- (1) - Liquid |
293.20 |
0.0000 |
26.0 |
Apparent molar heat capacity, J/K/mol
[ref]
Operational condition: Pressure, kPa =
350 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Molality, mol/kg of Ethane, 1,2-dimethoxy- (1) - Liquid |
Apparent molar heat capacity, J/K/mol - Liquid |
278.15 |
0.0155 |
367.0 |
278.15 |
0.2001 |
368.9 |
278.15 |
0.4986 |
363.6 |
278.15 |
0.9795 |
354.04 |
278.15 |
1.4991 |
336.54 |
278.15 |
1.989 |
333.38 |
283.15 |
0.0155 |
366.0 |
283.15 |
0.2001 |
375.7 |
283.15 |
0.4986 |
370.13 |
283.15 |
0.9795 |
361.85 |
283.15 |
1.4991 |
350.18 |
283.15 |
1.989 |
343.82 |
288.15 |
0.0100 |
369.0 |
288.15 |
0.0155 |
380.0 |
288.15 |
0.0902 |
359.3 |
288.15 |
0.2001 |
377.1 |
288.15 |
0.4986 |
372.72 |
288.15 |
0.9795 |
365.85 |
288.15 |
1.4991 |
356.4 |
288.15 |
1.989 |
349.9 |
293.15 |
0.0100 |
366.0 |
293.15 |
0.0155 |
381.0 |
293.15 |
0.0902 |
380.8 |
293.15 |
0.2001 |
378.4 |
293.15 |
0.4986 |
374.77 |
293.15 |
0.9795 |
368.89 |
293.15 |
1.4991 |
361.04 |
293.15 |
1.989 |
354.63 |
298.15 |
0.0100 |
361.0 |
298.15 |
0.0155 |
383.0 |
298.15 |
0.0902 |
381.8 |
298.15 |
0.2001 |
379.7 |
298.15 |
0.4986 |
376.49 |
298.15 |
0.9795 |
371.34 |
298.15 |
1.4991 |
364.58 |
298.15 |
1.989 |
358.33 |
303.15 |
0.0100 |
383.0 |
303.15 |
0.0155 |
383.0 |
303.15 |
0.0902 |
382.8 |
303.15 |
0.2001 |
380.9 |
303.15 |
0.4986 |
378.07 |
303.15 |
0.9795 |
373.44 |
303.15 |
1.4991 |
367.44 |
303.15 |
1.989 |
361.38 |
308.15 |
0.0100 |
382.0 |
308.15 |
0.0155 |
383.0 |
308.15 |
0.0902 |
384.3 |
308.15 |
0.2001 |
382.1 |
308.15 |
0.4986 |
379.6 |
308.15 |
0.9795 |
375.32 |
308.15 |
1.4991 |
369.85 |
308.15 |
1.989 |
363.9 |
313.15 |
0.0100 |
382.0 |
313.15 |
0.0155 |
383.0 |
313.15 |
0.0902 |
385.7 |
313.15 |
0.2001 |
383.4 |
313.15 |
0.4986 |
381.1 |
313.15 |
0.9795 |
377.04 |
313.15 |
1.4991 |
371.96 |
313.15 |
1.989 |
366.04 |
318.15 |
0.0100 |
383.0 |
318.15 |
0.0155 |
384.0 |
318.15 |
0.0902 |
386.6 |
318.15 |
0.2001 |
384.9 |
318.15 |
0.4986 |
382.6 |
318.15 |
0.9795 |
378.67 |
318.15 |
1.4991 |
373.86 |
318.15 |
1.989 |
367.9 |
323.15 |
0.0100 |
385.0 |
323.15 |
0.0155 |
386.0 |
323.15 |
0.0902 |
386.0 |
323.15 |
0.2001 |
386.4 |
323.15 |
0.4986 |
384.2 |
323.15 |
0.9795 |
380.22 |
323.15 |
1.4991 |
375.56 |
323.15 |
1.989 |
369.52 |
328.15 |
0.0100 |
386.0 |
328.15 |
0.0155 |
388.0 |
328.15 |
0.0902 |
389.7 |
328.15 |
0.2001 |
387.9 |
328.15 |
0.4986 |
385.7 |
328.15 |
0.9795 |
381.69 |
328.15 |
1.4991 |
377.11 |
328.15 |
1.989 |
370.94 |
333.15 |
0.0100 |
389.0 |
333.15 |
0.0155 |
389.0 |
333.15 |
0.0902 |
391.3 |
333.15 |
0.2001 |
389.5 |
333.15 |
0.4986 |
387.2 |
333.15 |
0.9795 |
383.05 |
333.15 |
1.4991 |
378.57 |
333.15 |
1.989 |
372.23 |
338.15 |
0.0100 |
391.0 |
338.15 |
0.0155 |
391.0 |
338.15 |
0.0902 |
393.0 |
338.15 |
0.2001 |
391.1 |
338.15 |
0.4986 |
388.7 |
338.15 |
0.9795 |
384.41 |
338.15 |
1.4991 |
379.92 |
338.15 |
1.989 |
373.39 |
343.15 |
0.0100 |
392.0 |
343.15 |
0.0155 |
393.0 |
343.15 |
0.0902 |
394.6 |
343.15 |
0.2001 |
392.7 |
343.15 |
0.4986 |
390.1 |
343.15 |
0.9795 |
385.68 |
343.15 |
1.4991 |
381.12 |
343.15 |
1.989 |
374.38 |
348.15 |
0.0100 |
394.0 |
348.15 |
0.0155 |
394.0 |
348.15 |
0.0902 |
396.2 |
348.15 |
0.2001 |
394.3 |
348.15 |
0.4986 |
391.5 |
348.15 |
0.9795 |
386.89 |
348.15 |
1.4991 |
382.24 |
348.15 |
1.989 |
375.27 |
353.15 |
0.0100 |
396.0 |
353.15 |
0.0155 |
396.0 |
353.15 |
0.0902 |
397.8 |
353.15 |
0.2001 |
395.8 |
353.15 |
0.4986 |
392.9 |
353.15 |
0.9795 |
388.03 |
353.15 |
1.4991 |
383.26 |
353.15 |
1.989 |
376.06 |
358.15 |
0.0100 |
398.0 |
358.15 |
0.0155 |
397.0 |
358.15 |
0.0902 |
399.5 |
358.15 |
0.2001 |
397.4 |
358.15 |
0.4986 |
394.2 |
358.15 |
0.9795 |
389.13 |
358.15 |
1.4991 |
384.23 |
358.15 |
1.989 |
376.77 |
363.15 |
0.0100 |
399.0 |
363.15 |
0.0155 |
399.0 |
363.15 |
0.0902 |
401.1 |
363.15 |
0.2001 |
398.9 |
363.15 |
0.4986 |
395.6 |
363.15 |
0.9795 |
390.18 |
363.15 |
1.4991 |
385.14 |
363.15 |
1.989 |
377.41 |
368.15 |
0.0100 |
401.0 |
368.15 |
0.0155 |
401.0 |
368.15 |
0.0902 |
402.7 |
368.15 |
0.2001 |
400.4 |
368.15 |
0.4986 |
396.8 |
368.15 |
0.9795 |
391.14 |
368.15 |
1.4991 |
385.96 |
368.15 |
1.989 |
377.93 |
373.15 |
0.0100 |
402.0 |
373.15 |
0.0155 |
402.0 |
373.15 |
0.0902 |
404.2 |
373.15 |
0.2001 |
401.9 |
373.15 |
0.4986 |
398.0 |
373.15 |
0.9795 |
392.07 |
373.15 |
1.4991 |
386.68 |
373.15 |
1.989 |
378.28 |
378.15 |
0.0100 |
404.0 |
378.15 |
0.0155 |
403.0 |
378.15 |
0.0902 |
405.8 |
378.15 |
0.2001 |
403.4 |
378.15 |
0.4986 |
399.2 |
378.15 |
0.9795 |
392.92 |
378.15 |
1.4991 |
387.13 |
378.15 |
1.989 |
378.47 |
383.15 |
0.0100 |
405.0 |
383.15 |
0.0155 |
404.0 |
383.15 |
0.0902 |
407.3 |
383.15 |
0.2001 |
404.8 |
383.15 |
0.4986 |
400.2 |
383.15 |
0.9795 |
393.67 |
383.15 |
1.4991 |
387.62 |
383.15 |
1.989 |
378.73 |
388.15 |
0.0100 |
406.0 |
388.15 |
0.0155 |
405.0 |
388.15 |
0.0902 |
408.8 |
388.15 |
0.2001 |
406.0 |
388.15 |
0.4986 |
401.1 |
388.15 |
0.9795 |
394.25 |
388.15 |
1.4991 |
388.02 |
388.15 |
1.989 |
378.88 |
393.15 |
0.0100 |
406.0 |
393.15 |
0.0155 |
405.0 |
393.15 |
0.0902 |
409.4 |
393.15 |
0.2001 |
406.4 |
393.15 |
0.4986 |
400.5 |
393.15 |
0.9795 |
393.3 |
393.15 |
1.4991 |
388.64 |
393.15 |
1.989 |
377.6 |
Apparent molar heat capacity, J/K/mol
[ref]
Operational condition: Pressure, kPa =
350 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Molality, mol/kg of Ethane, 1,2-dimethoxy- (1) - Liquid |
Apparent molar heat capacity, J/K/mol - Liquid |
278.15 |
0.0155 |
367.0 |
278.15 |
0.2001 |
368.9 |
278.15 |
0.4986 |
363.6 |
278.15 |
0.9795 |
354.04 |
278.15 |
1.4991 |
336.54 |
278.15 |
1.989 |
333.38 |
283.15 |
0.0155 |
366.0 |
283.15 |
0.2001 |
375.7 |
283.15 |
0.4986 |
370.13 |
283.15 |
0.9795 |
361.85 |
283.15 |
1.4991 |
350.18 |
283.15 |
1.989 |
343.82 |
288.15 |
0.0100 |
369.0 |
288.15 |
0.0155 |
380.0 |
288.15 |
0.0902 |
359.3 |
288.15 |
0.2001 |
377.1 |
288.15 |
0.4986 |
372.72 |
288.15 |
0.9795 |
365.85 |
288.15 |
1.4991 |
356.4 |
288.15 |
1.989 |
349.9 |
293.15 |
0.0100 |
366.0 |
293.15 |
0.0155 |
381.0 |
293.15 |
0.0902 |
380.8 |
293.15 |
0.2001 |
378.4 |
293.15 |
0.4986 |
374.77 |
293.15 |
0.9795 |
368.89 |
293.15 |
1.4991 |
361.04 |
293.15 |
1.989 |
354.63 |
298.15 |
0.0100 |
361.0 |
298.15 |
0.0155 |
383.0 |
298.15 |
0.0902 |
381.8 |
298.15 |
0.2001 |
379.7 |
298.15 |
0.4986 |
376.49 |
298.15 |
0.9795 |
371.34 |
298.15 |
1.4991 |
364.58 |
298.15 |
1.989 |
358.33 |
303.15 |
0.0100 |
383.0 |
303.15 |
0.0155 |
383.0 |
303.15 |
0.0902 |
382.8 |
303.15 |
0.2001 |
380.9 |
303.15 |
0.4986 |
378.07 |
303.15 |
0.9795 |
373.44 |
303.15 |
1.4991 |
367.44 |
303.15 |
1.989 |
361.38 |
308.15 |
0.0100 |
382.0 |
308.15 |
0.0155 |
383.0 |
308.15 |
0.0902 |
384.3 |
308.15 |
0.2001 |
382.1 |
308.15 |
0.4986 |
379.6 |
308.15 |
0.9795 |
375.32 |
308.15 |
1.4991 |
369.85 |
308.15 |
1.989 |
363.9 |
313.15 |
0.0100 |
382.0 |
313.15 |
0.0155 |
383.0 |
313.15 |
0.0902 |
385.7 |
313.15 |
0.2001 |
383.4 |
313.15 |
0.4986 |
381.1 |
313.15 |
0.9795 |
377.04 |
313.15 |
1.4991 |
371.96 |
313.15 |
1.989 |
366.04 |
318.15 |
0.0100 |
383.0 |
318.15 |
0.0155 |
384.0 |
318.15 |
0.0902 |
386.6 |
318.15 |
0.2001 |
384.9 |
318.15 |
0.4986 |
382.6 |
318.15 |
0.9795 |
378.67 |
318.15 |
1.4991 |
373.86 |
318.15 |
1.989 |
367.9 |
323.15 |
0.0100 |
385.0 |
323.15 |
0.0155 |
386.0 |
323.15 |
0.0902 |
386.0 |
323.15 |
0.2001 |
386.4 |
323.15 |
0.4986 |
384.2 |
323.15 |
0.9795 |
380.22 |
323.15 |
1.4991 |
375.56 |
323.15 |
1.989 |
369.52 |
328.15 |
0.0100 |
386.0 |
328.15 |
0.0155 |
388.0 |
328.15 |
0.0902 |
389.7 |
328.15 |
0.2001 |
387.9 |
328.15 |
0.4986 |
385.7 |
328.15 |
0.9795 |
381.69 |
328.15 |
1.4991 |
377.11 |
328.15 |
1.989 |
370.94 |
333.15 |
0.0100 |
389.0 |
333.15 |
0.0155 |
389.0 |
333.15 |
0.0902 |
391.3 |
333.15 |
0.2001 |
389.5 |
333.15 |
0.4986 |
387.2 |
333.15 |
0.9795 |
383.05 |
333.15 |
1.4991 |
378.57 |
333.15 |
1.989 |
372.23 |
338.15 |
0.0100 |
391.0 |
338.15 |
0.0155 |
391.0 |
338.15 |
0.0902 |
393.0 |
338.15 |
0.2001 |
391.1 |
338.15 |
0.4986 |
388.7 |
338.15 |
0.9795 |
384.41 |
338.15 |
1.4991 |
379.92 |
338.15 |
1.989 |
373.39 |
343.15 |
0.0100 |
392.0 |
343.15 |
0.0155 |
393.0 |
343.15 |
0.0902 |
394.6 |
343.15 |
0.2001 |
392.7 |
343.15 |
0.4986 |
390.1 |
343.15 |
0.9795 |
385.68 |
343.15 |
1.4991 |
381.12 |
343.15 |
1.989 |
374.38 |
348.15 |
0.0100 |
394.0 |
348.15 |
0.0155 |
394.0 |
348.15 |
0.0902 |
396.2 |
348.15 |
0.2001 |
394.3 |
348.15 |
0.4986 |
391.5 |
348.15 |
0.9795 |
386.89 |
348.15 |
1.4991 |
382.24 |
348.15 |
1.989 |
375.27 |
353.15 |
0.0100 |
396.0 |
353.15 |
0.0155 |
396.0 |
353.15 |
0.0902 |
397.8 |
353.15 |
0.2001 |
395.8 |
353.15 |
0.4986 |
392.9 |
353.15 |
0.9795 |
388.03 |
353.15 |
1.4991 |
383.26 |
353.15 |
1.989 |
376.06 |
358.15 |
0.0100 |
398.0 |
358.15 |
0.0155 |
397.0 |
358.15 |
0.0902 |
399.5 |
358.15 |
0.2001 |
397.4 |
358.15 |
0.4986 |
394.2 |
358.15 |
0.9795 |
389.13 |
358.15 |
1.4991 |
384.23 |
358.15 |
1.989 |
376.77 |
363.15 |
0.0100 |
399.0 |
363.15 |
0.0155 |
399.0 |
363.15 |
0.0902 |
401.1 |
363.15 |
0.2001 |
398.9 |
363.15 |
0.4986 |
395.6 |
363.15 |
0.9795 |
390.18 |
363.15 |
1.4991 |
385.14 |
363.15 |
1.989 |
377.41 |
368.15 |
0.0100 |
401.0 |
368.15 |
0.0155 |
401.0 |
368.15 |
0.0902 |
402.7 |
368.15 |
0.2001 |
400.4 |
368.15 |
0.4986 |
396.8 |
368.15 |
0.9795 |
391.14 |
368.15 |
1.4991 |
385.96 |
368.15 |
1.989 |
377.93 |
373.15 |
0.0100 |
402.0 |
373.15 |
0.0155 |
402.0 |
373.15 |
0.0902 |
404.2 |
373.15 |
0.2001 |
401.9 |
373.15 |
0.4986 |
398.0 |
373.15 |
0.9795 |
392.07 |
373.15 |
1.4991 |
386.68 |
373.15 |
1.989 |
378.28 |
378.15 |
0.0100 |
404.0 |
378.15 |
0.0155 |
403.0 |
378.15 |
0.0902 |
405.8 |
378.15 |
0.2001 |
403.4 |
378.15 |
0.4986 |
399.2 |
378.15 |
0.9795 |
392.92 |
378.15 |
1.4991 |
387.13 |
378.15 |
1.989 |
378.47 |
383.15 |
0.0100 |
405.0 |
383.15 |
0.0155 |
404.0 |
383.15 |
0.0902 |
407.3 |
383.15 |
0.2001 |
404.8 |
383.15 |
0.4986 |
400.2 |
383.15 |
0.9795 |
393.67 |
383.15 |
1.4991 |
387.62 |
383.15 |
1.989 |
378.73 |
388.15 |
0.0100 |
406.0 |
388.15 |
0.0155 |
405.0 |
388.15 |
0.0902 |
408.8 |
388.15 |
0.2001 |
406.0 |
388.15 |
0.4986 |
401.1 |
388.15 |
0.9795 |
394.25 |
388.15 |
1.4991 |
388.02 |
388.15 |
1.989 |
378.88 |
393.15 |
0.0100 |
406.0 |
393.15 |
0.0155 |
405.0 |
393.15 |
0.0902 |
409.4 |
393.15 |
0.2001 |
406.4 |
393.15 |
0.4986 |
400.5 |
393.15 |
0.9795 |
393.3 |
393.15 |
1.4991 |
388.64 |
393.15 |
1.989 |
377.6 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
350 (Liquid)
Fixed |
Measured |
Molality, mol/kg of Ethane, 1,2-dimethoxy- (1) - Liquid |
Temperature, K - Liquid |
Mass density, kg/m3 - Liquid |
0.0100 |
278.15 |
1000.27 |
0.0100 |
283.15 |
1000.04 |
0.0100 |
288.15 |
999.45 |
0.0100 |
298.15 |
997.42 |
0.0100 |
308.15 |
994.42 |
0.0100 |
318.15 |
990.61 |
0.0100 |
328.15 |
986.1 |
0.0100 |
338.15 |
980.89 |
0.0100 |
348.15 |
975.15 |
0.0100 |
358.15 |
968.9 |
0.0100 |
368.15 |
962.17 |
0.0155 |
278.15 |
1000.29 |
0.0155 |
283.15 |
1000.05 |
0.0155 |
288.15 |
999.44 |
0.0155 |
298.15 |
997.39 |
0.0155 |
308.15 |
994.38 |
0.0155 |
318.15 |
990.56 |
0.0155 |
328.15 |
986.07 |
0.0155 |
338.15 |
980.95 |
0.0155 |
348.15 |
975.19 |
0.0155 |
358.15 |
968.97 |
0.0155 |
368.15 |
962.22 |
0.0902 |
278.15 |
999.86 |
0.0902 |
283.15 |
999.6 |
0.0902 |
288.15 |
998.99 |
0.0902 |
298.15 |
996.92 |
0.0902 |
308.15 |
993.88 |
0.0902 |
318.15 |
990.0 |
0.0902 |
328.15 |
985.44 |
0.0902 |
338.15 |
980.29 |
0.0902 |
348.15 |
974.57 |
0.0902 |
358.15 |
968.3 |
0.0902 |
368.15 |
961.53 |
0.2001 |
278.15 |
999.51 |
0.2001 |
283.15 |
999.2 |
0.2001 |
288.15 |
998.53 |
0.2001 |
298.15 |
996.37 |
0.2001 |
308.15 |
993.27 |
0.2001 |
318.15 |
989.32 |
0.2001 |
328.15 |
984.71 |
0.2001 |
338.15 |
979.53 |
0.2001 |
348.15 |
973.8 |
0.2001 |
358.15 |
967.52 |
0.2001 |
368.15 |
960.78 |
0.4986 |
278.15 |
998.31 |
0.4986 |
283.15 |
997.85 |
0.4986 |
288.15 |
997.08 |
0.4986 |
298.15 |
994.73 |
0.4986 |
308.15 |
991.54 |
0.4986 |
318.15 |
987.52 |
0.4986 |
328.15 |
982.76 |
0.4986 |
338.15 |
977.37 |
0.4986 |
348.15 |
971.41 |
0.4986 |
358.15 |
964.92 |
0.4986 |
368.15 |
957.93 |
0.9795 |
278.15 |
997.51 |
0.9795 |
283.15 |
996.82 |
0.9795 |
288.15 |
995.85 |
0.9795 |
298.15 |
993.13 |
0.9795 |
308.15 |
989.55 |
0.9795 |
318.15 |
985.15 |
0.9795 |
328.15 |
980.1 |
0.9795 |
338.15 |
974.48 |
0.9795 |
348.15 |
968.28 |
0.9795 |
358.15 |
961.52 |
0.9795 |
368.15 |
954.28 |
1.4991 |
278.15 |
997.34 |
1.4991 |
283.15 |
996.31 |
1.4991 |
288.15 |
995.03 |
1.4991 |
298.15 |
991.81 |
1.4991 |
308.15 |
987.8 |
1.4991 |
318.15 |
983.04 |
1.4991 |
328.15 |
977.65 |
1.4991 |
338.15 |
971.68 |
1.4991 |
348.15 |
965.19 |
1.4991 |
358.15 |
958.12 |
1.4991 |
368.15 |
950.59 |
1.989 |
278.15 |
997.25 |
1.989 |
283.15 |
995.91 |
1.989 |
288.15 |
994.35 |
1.989 |
298.15 |
990.62 |
1.989 |
308.15 |
986.16 |
1.989 |
318.15 |
981.03 |
1.989 |
328.15 |
975.32 |
1.989 |
338.15 |
969.05 |
1.989 |
348.15 |
962.26 |
1.989 |
358.15 |
954.95 |
1.989 |
368.15 |
947.18 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
350 (Liquid)
Fixed |
Measured |
Molality, mol/kg of Ethane, 1,2-dimethoxy- (1) - Liquid |
Temperature, K - Liquid |
Mass density, kg/m3 - Liquid |
0.0100 |
278.15 |
1000.27 |
0.0100 |
283.15 |
1000.04 |
0.0100 |
288.15 |
999.45 |
0.0100 |
298.15 |
997.42 |
0.0100 |
308.15 |
994.42 |
0.0100 |
318.15 |
990.61 |
0.0100 |
328.15 |
986.1 |
0.0100 |
338.15 |
980.89 |
0.0100 |
348.15 |
975.15 |
0.0100 |
358.15 |
968.9 |
0.0100 |
368.15 |
962.17 |
0.0155 |
278.15 |
1000.29 |
0.0155 |
283.15 |
1000.05 |
0.0155 |
288.15 |
999.44 |
0.0155 |
298.15 |
997.39 |
0.0155 |
308.15 |
994.38 |
0.0155 |
318.15 |
990.56 |
0.0155 |
328.15 |
986.07 |
0.0155 |
338.15 |
980.95 |
0.0155 |
348.15 |
975.19 |
0.0155 |
358.15 |
968.97 |
0.0155 |
368.15 |
962.22 |
0.0902 |
278.15 |
999.86 |
0.0902 |
283.15 |
999.6 |
0.0902 |
288.15 |
998.99 |
0.0902 |
298.15 |
996.92 |
0.0902 |
308.15 |
993.88 |
0.0902 |
318.15 |
990.0 |
0.0902 |
328.15 |
985.44 |
0.0902 |
338.15 |
980.29 |
0.0902 |
348.15 |
974.57 |
0.0902 |
358.15 |
968.3 |
0.0902 |
368.15 |
961.53 |
0.2001 |
278.15 |
999.51 |
0.2001 |
283.15 |
999.2 |
0.2001 |
288.15 |
998.53 |
0.2001 |
298.15 |
996.37 |
0.2001 |
308.15 |
993.27 |
0.2001 |
318.15 |
989.32 |
0.2001 |
328.15 |
984.71 |
0.2001 |
338.15 |
979.53 |
0.2001 |
348.15 |
973.8 |
0.2001 |
358.15 |
967.52 |
0.2001 |
368.15 |
960.78 |
0.4986 |
278.15 |
998.31 |
0.4986 |
283.15 |
997.85 |
0.4986 |
288.15 |
997.08 |
0.4986 |
298.15 |
994.73 |
0.4986 |
308.15 |
991.54 |
0.4986 |
318.15 |
987.52 |
0.4986 |
328.15 |
982.76 |
0.4986 |
338.15 |
977.37 |
0.4986 |
348.15 |
971.41 |
0.4986 |
358.15 |
964.92 |
0.4986 |
368.15 |
957.93 |
0.9795 |
278.15 |
997.51 |
0.9795 |
283.15 |
996.82 |
0.9795 |
288.15 |
995.85 |
0.9795 |
298.15 |
993.13 |
0.9795 |
308.15 |
989.55 |
0.9795 |
318.15 |
985.15 |
0.9795 |
328.15 |
980.1 |
0.9795 |
338.15 |
974.48 |
0.9795 |
348.15 |
968.28 |
0.9795 |
358.15 |
961.52 |
0.9795 |
368.15 |
954.28 |
1.4991 |
278.15 |
997.34 |
1.4991 |
283.15 |
996.31 |
1.4991 |
288.15 |
995.03 |
1.4991 |
298.15 |
991.81 |
1.4991 |
308.15 |
987.8 |
1.4991 |
318.15 |
983.04 |
1.4991 |
328.15 |
977.65 |
1.4991 |
338.15 |
971.68 |
1.4991 |
348.15 |
965.19 |
1.4991 |
358.15 |
958.12 |
1.4991 |
368.15 |
950.59 |
1.989 |
278.15 |
997.25 |
1.989 |
283.15 |
995.91 |
1.989 |
288.15 |
994.35 |
1.989 |
298.15 |
990.62 |
1.989 |
308.15 |
986.16 |
1.989 |
318.15 |
981.03 |
1.989 |
328.15 |
975.32 |
1.989 |
338.15 |
969.05 |
1.989 |
348.15 |
962.26 |
1.989 |
358.15 |
954.95 |
1.989 |
368.15 |
947.18 |
Surface tension liquid-gas, N/m
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethane, 1,2-dimethoxy- (1) - Liquid |
Surface tension liquid-gas, N/m - Liquid |
298.15 |
0.0000 |
0.0720 |
298.15 |
0.0470 |
0.0483 |
298.15 |
0.0660 |
0.0424 |
298.15 |
0.0759 |
0.0406 |
298.15 |
0.1286 |
0.0320 |
298.15 |
0.1942 |
0.0285 |
298.15 |
0.2612 |
0.0278 |
298.15 |
0.4132 |
0.0261 |
298.15 |
0.6313 |
0.0254 |
298.15 |
1.0000 |
0.0238 |
308.15 |
0.0000 |
0.0704 |
308.15 |
0.0470 |
0.0468 |
308.15 |
0.0660 |
0.0410 |
308.15 |
0.0759 |
0.0393 |
308.15 |
0.1286 |
0.0307 |
308.15 |
0.1942 |
0.0274 |
308.15 |
0.2612 |
0.0268 |
308.15 |
0.4132 |
0.0251 |
308.15 |
0.6313 |
0.0245 |
308.15 |
1.0000 |
0.0229 |
318.15 |
0.0000 |
0.0688 |
318.15 |
0.0470 |
0.0465 |
318.15 |
0.0660 |
0.0406 |
318.15 |
0.0759 |
0.0377 |
318.15 |
0.1286 |
0.0293 |
318.15 |
0.1942 |
0.0265 |
318.15 |
0.2612 |
0.0259 |
318.15 |
0.4132 |
0.0248 |
318.15 |
0.6313 |
0.0236 |
318.15 |
1.0000 |
0.0219 |
Surface tension liquid-gas, N/m
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethane, 1,2-dimethoxy- (1) - Liquid |
Surface tension liquid-gas, N/m - Liquid |
298.15 |
0.0000 |
0.0720 |
298.15 |
0.0470 |
0.0483 |
298.15 |
0.0660 |
0.0424 |
298.15 |
0.0759 |
0.0406 |
298.15 |
0.1286 |
0.0320 |
298.15 |
0.1942 |
0.0285 |
298.15 |
0.2612 |
0.0278 |
298.15 |
0.4132 |
0.0261 |
298.15 |
0.6313 |
0.0254 |
298.15 |
1.0000 |
0.0238 |
308.15 |
0.0000 |
0.0704 |
308.15 |
0.0470 |
0.0468 |
308.15 |
0.0660 |
0.0410 |
308.15 |
0.0759 |
0.0393 |
308.15 |
0.1286 |
0.0307 |
308.15 |
0.1942 |
0.0274 |
308.15 |
0.2612 |
0.0268 |
308.15 |
0.4132 |
0.0251 |
308.15 |
0.6313 |
0.0245 |
308.15 |
1.0000 |
0.0229 |
318.15 |
0.0000 |
0.0688 |
318.15 |
0.0470 |
0.0465 |
318.15 |
0.0660 |
0.0406 |
318.15 |
0.0759 |
0.0377 |
318.15 |
0.1286 |
0.0293 |
318.15 |
0.1942 |
0.0265 |
318.15 |
0.2612 |
0.0259 |
318.15 |
0.4132 |
0.0248 |
318.15 |
0.6313 |
0.0236 |
318.15 |
1.0000 |
0.0219 |
Sources
-
Temperature dependence of limiting activity coefficients and Henry s law constants of cyclic and open-chain ethers in water
-
Apparent molar volumes and apparent molar heat capacities of aqueous tetrahydrofuran, dimethyl sulfoxide, 1,4-dioxane, and 1,2-dimethoxyethane at temperatures from 278.15 K to 393.15 K and at the pressure 0.35 MPa
-
Experimental Surface Tensions and Derived Surface Properties of Binary Mixtures of Water + Alkoxyethanols (C1Em, m = 1, 2, 3) and Water + Ethylene Glycol Dimethyl Ether (C1E1C1) at (298.15, 308.15, and 318.15) K
-
Henry s Law Constants of Organic Compounds in Water and n-Octane at T = 293.2 K