Mixture of Propane + Ethyl ether
Datasets
-
Pvap - Vapor or sublimation pressure, kPa (2)
-
ρl - Mass density, kg/m3 (4)
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Propane (1) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
362.80 |
0.6510 |
2080.00 |
394.90 |
0.6550 |
4010.00 |
409.20 |
0.6510 |
4620.00 |
351.80 |
0.7480 |
2080.00 |
372.00 |
0.7430 |
3100.00 |
399.90 |
0.7420 |
4420.00 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Propane (1) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
362.80 |
0.6510 |
2080.00 |
394.90 |
0.6550 |
4010.00 |
409.20 |
0.6510 |
4620.00 |
351.80 |
0.7480 |
2080.00 |
372.00 |
0.7430 |
3100.00 |
399.90 |
0.7420 |
4420.00 |
Mass density, kg/m3
[ref]
Fixed |
Measured |
Mole fraction of Propane (1) - Fluid (supercritical or subcritical phases) |
Temperature, K - Fluid (supercritical or subcritical phases) |
Pressure, kPa - Fluid (supercritical or subcritical phases) |
Mass density, kg/m3 - Fluid (supercritical or subcritical phases) |
0.6510 |
370.30 |
3910.00 |
474.0 |
0.6510 |
379.40 |
6660.00 |
474.0 |
0.6510 |
387.90 |
9300.00 |
474.0 |
0.6510 |
397.10 |
12250.00 |
474.0 |
0.6510 |
407.70 |
15710.00 |
474.0 |
0.6510 |
419.20 |
19360.00 |
474.0 |
0.6550 |
401.90 |
5030.00 |
401.0 |
0.6550 |
405.60 |
5640.00 |
401.0 |
0.6550 |
412.00 |
6760.00 |
401.0 |
0.6550 |
422.60 |
8790.00 |
401.0 |
0.6550 |
429.60 |
10210.00 |
401.0 |
0.6550 |
437.50 |
11740.00 |
401.0 |
0.6550 |
447.60 |
13670.00 |
401.0 |
0.6550 |
455.00 |
15200.00 |
401.0 |
0.6510 |
418.50 |
5130.00 |
311.0 |
0.6510 |
429.10 |
6250.00 |
311.0 |
0.6510 |
438.50 |
7270.00 |
311.0 |
0.6510 |
449.00 |
8390.00 |
311.0 |
0.6510 |
458.50 |
9500.00 |
311.0 |
0.6510 |
467.40 |
10620.00 |
311.0 |
0.6510 |
470.00 |
10930.00 |
311.0 |
0.7480 |
359.20 |
4110.00 |
474.0 |
0.7480 |
369.50 |
7470.00 |
474.0 |
0.7480 |
379.40 |
10830.00 |
474.0 |
0.7480 |
391.10 |
14590.00 |
474.0 |
0.7480 |
401.10 |
17840.00 |
474.0 |
0.7480 |
411.40 |
21600.00 |
474.0 |
0.7430 |
382.70 |
4110.00 |
401.0 |
0.7430 |
390.10 |
5340.00 |
401.0 |
0.7430 |
401.10 |
7670.00 |
401.0 |
0.7430 |
410.70 |
9710.00 |
401.0 |
0.7430 |
419.70 |
11640.00 |
401.0 |
0.7430 |
430.40 |
13770.00 |
401.0 |
0.7430 |
437.50 |
15300.00 |
401.0 |
0.7430 |
452.40 |
18650.00 |
401.0 |
0.7420 |
407.50 |
5130.00 |
311.0 |
0.7420 |
417.70 |
6250.00 |
311.0 |
0.7420 |
429.10 |
7570.00 |
311.0 |
0.7420 |
437.80 |
8590.00 |
311.0 |
0.7420 |
447.30 |
9710.00 |
311.0 |
0.7420 |
459.00 |
11220.00 |
311.0 |
0.7420 |
466.10 |
12150.00 |
311.0 |
Mass density, kg/m3
[ref]
Fixed |
Measured |
Mole fraction of Propane (1) - Liquid |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mass density, kg/m3 - Liquid |
0.6510 |
362.80 |
2080.00 |
474.0 |
0.6550 |
394.90 |
4010.00 |
401.0 |
0.6510 |
409.20 |
4620.00 |
311.0 |
0.7480 |
351.80 |
2080.00 |
474.0 |
0.7430 |
372.00 |
3100.00 |
401.0 |
0.7420 |
399.90 |
4420.00 |
311.0 |
Mass density, kg/m3
[ref]
Fixed |
Measured |
Mole fraction of Propane (1) - Fluid (supercritical or subcritical phases) |
Temperature, K - Fluid (supercritical or subcritical phases) |
Pressure, kPa - Fluid (supercritical or subcritical phases) |
Mass density, kg/m3 - Fluid (supercritical or subcritical phases) |
0.6510 |
370.30 |
3910.00 |
474.0 |
0.6510 |
379.40 |
6660.00 |
474.0 |
0.6510 |
387.90 |
9300.00 |
474.0 |
0.6510 |
397.10 |
12250.00 |
474.0 |
0.6510 |
407.70 |
15710.00 |
474.0 |
0.6510 |
419.20 |
19360.00 |
474.0 |
0.6550 |
401.90 |
5030.00 |
401.0 |
0.6550 |
405.60 |
5640.00 |
401.0 |
0.6550 |
412.00 |
6760.00 |
401.0 |
0.6550 |
422.60 |
8790.00 |
401.0 |
0.6550 |
429.60 |
10210.00 |
401.0 |
0.6550 |
437.50 |
11740.00 |
401.0 |
0.6550 |
447.60 |
13670.00 |
401.0 |
0.6550 |
455.00 |
15200.00 |
401.0 |
0.6510 |
418.50 |
5130.00 |
311.0 |
0.6510 |
429.10 |
6250.00 |
311.0 |
0.6510 |
438.50 |
7270.00 |
311.0 |
0.6510 |
449.00 |
8390.00 |
311.0 |
0.6510 |
458.50 |
9500.00 |
311.0 |
0.6510 |
467.40 |
10620.00 |
311.0 |
0.6510 |
470.00 |
10930.00 |
311.0 |
0.7480 |
359.20 |
4110.00 |
474.0 |
0.7480 |
369.50 |
7470.00 |
474.0 |
0.7480 |
379.40 |
10830.00 |
474.0 |
0.7480 |
391.10 |
14590.00 |
474.0 |
0.7480 |
401.10 |
17840.00 |
474.0 |
0.7480 |
411.40 |
21600.00 |
474.0 |
0.7430 |
382.70 |
4110.00 |
401.0 |
0.7430 |
390.10 |
5340.00 |
401.0 |
0.7430 |
401.10 |
7670.00 |
401.0 |
0.7430 |
410.70 |
9710.00 |
401.0 |
0.7430 |
419.70 |
11640.00 |
401.0 |
0.7430 |
430.40 |
13770.00 |
401.0 |
0.7430 |
437.50 |
15300.00 |
401.0 |
0.7430 |
452.40 |
18650.00 |
401.0 |
0.7420 |
407.50 |
5130.00 |
311.0 |
0.7420 |
417.70 |
6250.00 |
311.0 |
0.7420 |
429.10 |
7570.00 |
311.0 |
0.7420 |
437.80 |
8590.00 |
311.0 |
0.7420 |
447.30 |
9710.00 |
311.0 |
0.7420 |
459.00 |
11220.00 |
311.0 |
0.7420 |
466.10 |
12150.00 |
311.0 |
Mass density, kg/m3
[ref]
Fixed |
Measured |
Mole fraction of Propane (1) - Liquid |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mass density, kg/m3 - Liquid |
0.6510 |
362.80 |
2080.00 |
474.0 |
0.6550 |
394.90 |
4010.00 |
401.0 |
0.6510 |
409.20 |
4620.00 |
311.0 |
0.7480 |
351.80 |
2080.00 |
474.0 |
0.7430 |
372.00 |
3100.00 |
401.0 |
0.7420 |
399.90 |
4420.00 |
311.0 |
Sources