Datasets
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Mole fraction (4)
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Excess molar enthalpy (molar enthalpy (2)
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Pvap - Vapor or sublimation pressure, kPa (2)
-
Tboil - Boiling temperature at pressure P, K (2)
Mole fraction of Propane, 2-methoxy-2-methyl- (2)
[ref]
Operational condition: Pressure, kPa =
90.1 (Liquid)
Mole fraction of Propane, 2-methoxy-2-methyl- (2) - Liquid |
Mole fraction of Propane, 2-methoxy-2-methyl- (2) - Gas |
0.0000 |
0.0000 |
0.0640 |
0.2480 |
0.0900 |
0.3470 |
0.1100 |
0.3890 |
0.1430 |
0.4720 |
0.1850 |
0.5440 |
0.2170 |
0.5970 |
0.2380 |
0.6300 |
0.2650 |
0.6690 |
0.2980 |
0.7010 |
0.3000 |
0.7030 |
0.3210 |
0.7250 |
0.3410 |
0.7480 |
0.3720 |
0.7750 |
0.4100 |
0.8100 |
0.4470 |
0.8360 |
0.5120 |
0.8680 |
0.6780 |
0.9280 |
0.7680 |
0.9500 |
0.8460 |
0.9680 |
0.9090 |
0.9810 |
0.9750 |
0.9950 |
1.0000 |
1.0000 |
Mole fraction of Propane, 2-methoxy-2-methyl- (2)
[ref]
Fixed |
Measured |
Mole fraction of Propane, 2-methoxy-2-methyl- (2) - Liquid |
Temperature, K - Liquid |
Mole fraction of Propane, 2-methoxy-2-methyl- (2) - Gas |
1.0000 |
323.20 |
1.0000 |
0.9350 |
323.20 |
0.9880 |
0.8720 |
323.16 |
0.9760 |
0.7970 |
323.16 |
0.9620 |
0.7100 |
322.94 |
0.9450 |
0.7250 |
323.15 |
0.9480 |
0.6070 |
323.14 |
0.9220 |
0.5090 |
323.19 |
0.8950 |
0.3790 |
323.16 |
0.8440 |
0.3320 |
323.20 |
0.8240 |
0.2590 |
323.22 |
0.7640 |
Mole fraction of Propane, 2-methoxy-2-methyl- (2)
[ref]
Operational condition: Pressure, kPa =
90.1 (Liquid)
Mole fraction of Propane, 2-methoxy-2-methyl- (2) - Liquid |
Mole fraction of Propane, 2-methoxy-2-methyl- (2) - Gas |
0.0000 |
0.0000 |
0.0640 |
0.2480 |
0.0900 |
0.3470 |
0.1100 |
0.3890 |
0.1430 |
0.4720 |
0.1850 |
0.5440 |
0.2170 |
0.5970 |
0.2380 |
0.6300 |
0.2650 |
0.6690 |
0.2980 |
0.7010 |
0.3000 |
0.7030 |
0.3210 |
0.7250 |
0.3410 |
0.7480 |
0.3720 |
0.7750 |
0.4100 |
0.8100 |
0.4470 |
0.8360 |
0.5120 |
0.8680 |
0.6780 |
0.9280 |
0.7680 |
0.9500 |
0.8460 |
0.9680 |
0.9090 |
0.9810 |
0.9750 |
0.9950 |
1.0000 |
1.0000 |
Mole fraction of Propane, 2-methoxy-2-methyl- (2)
[ref]
Fixed |
Measured |
Mole fraction of Propane, 2-methoxy-2-methyl- (2) - Liquid |
Temperature, K - Liquid |
Mole fraction of Propane, 2-methoxy-2-methyl- (2) - Gas |
1.0000 |
323.20 |
1.0000 |
0.9350 |
323.20 |
0.9880 |
0.8720 |
323.16 |
0.9760 |
0.7970 |
323.16 |
0.9620 |
0.7100 |
322.94 |
0.9450 |
0.7250 |
323.15 |
0.9480 |
0.6070 |
323.14 |
0.9220 |
0.5090 |
323.19 |
0.8950 |
0.3790 |
323.16 |
0.8440 |
0.3320 |
323.20 |
0.8240 |
0.2590 |
323.22 |
0.7640 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
[ref]
Fixed |
Measured |
Pressure, kPa - Liquid |
Temperature, K - Liquid |
Mole fraction of Propane, 2-methoxy-2-methyl- (2) - Liquid |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
1085.00 |
363.15 |
0.0990 |
0.1080 |
1085.00 |
363.15 |
0.0990 |
0.1050 |
1085.00 |
363.15 |
0.2000 |
0.2180 |
1085.00 |
363.15 |
0.3000 |
0.3110 |
1085.00 |
363.15 |
0.4000 |
0.3890 |
1085.00 |
363.15 |
0.4000 |
0.4000 |
1085.00 |
363.15 |
0.4800 |
0.4490 |
1085.00 |
363.15 |
0.5000 |
0.4530 |
1085.00 |
363.15 |
0.6000 |
0.4700 |
1085.00 |
363.15 |
0.7000 |
0.4510 |
1085.00 |
363.15 |
0.7990 |
0.3740 |
1085.00 |
363.15 |
0.8920 |
0.2410 |
1085.00 |
363.15 |
0.9000 |
0.2230 |
1085.00 |
363.15 |
0.9000 |
0.2330 |
1085.00 |
363.15 |
0.9160 |
0.1870 |
1085.00 |
363.15 |
0.9320 |
0.1440 |
1085.00 |
363.15 |
0.9480 |
0.0880 |
317.00 |
323.15 |
0.0830 |
0.0850 |
317.00 |
323.15 |
0.1990 |
0.2450 |
317.00 |
323.15 |
0.3000 |
0.3800 |
317.00 |
323.15 |
0.3990 |
0.5180 |
317.00 |
323.15 |
0.4760 |
0.5810 |
317.00 |
323.15 |
0.4760 |
0.5850 |
317.00 |
323.15 |
0.6000 |
0.6600 |
317.00 |
323.15 |
0.7000 |
0.6490 |
317.00 |
323.15 |
0.8000 |
0.5500 |
317.00 |
323.15 |
0.9010 |
0.3310 |
317.00 |
323.15 |
0.9010 |
0.3270 |
317.00 |
323.15 |
0.9270 |
0.2270 |
204.00 |
322.60 |
0.0990 |
0.1040 |
204.00 |
322.60 |
0.1980 |
0.2400 |
204.00 |
322.60 |
0.3000 |
0.3860 |
204.00 |
322.60 |
0.3990 |
0.5130 |
204.00 |
322.60 |
0.4980 |
0.6090 |
204.00 |
322.60 |
0.5990 |
0.6640 |
204.00 |
322.60 |
0.6980 |
0.6510 |
204.00 |
322.60 |
0.6980 |
0.6500 |
204.00 |
322.60 |
0.7990 |
0.5530 |
204.00 |
322.60 |
0.8990 |
0.3310 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
[ref]
Fixed |
Measured |
Pressure, kPa - Liquid |
Temperature, K - Liquid |
Mole fraction of Propane, 2-methoxy-2-methyl- (2) - Liquid |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
1085.00 |
363.15 |
0.0990 |
0.1080 |
1085.00 |
363.15 |
0.0990 |
0.1050 |
1085.00 |
363.15 |
0.2000 |
0.2180 |
1085.00 |
363.15 |
0.3000 |
0.3110 |
1085.00 |
363.15 |
0.4000 |
0.3890 |
1085.00 |
363.15 |
0.4000 |
0.4000 |
1085.00 |
363.15 |
0.4800 |
0.4490 |
1085.00 |
363.15 |
0.5000 |
0.4530 |
1085.00 |
363.15 |
0.6000 |
0.4700 |
1085.00 |
363.15 |
0.7000 |
0.4510 |
1085.00 |
363.15 |
0.7990 |
0.3740 |
1085.00 |
363.15 |
0.8920 |
0.2410 |
1085.00 |
363.15 |
0.9000 |
0.2230 |
1085.00 |
363.15 |
0.9000 |
0.2330 |
1085.00 |
363.15 |
0.9160 |
0.1870 |
1085.00 |
363.15 |
0.9320 |
0.1440 |
1085.00 |
363.15 |
0.9480 |
0.0880 |
317.00 |
323.15 |
0.0830 |
0.0850 |
317.00 |
323.15 |
0.1990 |
0.2450 |
317.00 |
323.15 |
0.3000 |
0.3800 |
317.00 |
323.15 |
0.3990 |
0.5180 |
317.00 |
323.15 |
0.4760 |
0.5810 |
317.00 |
323.15 |
0.4760 |
0.5850 |
317.00 |
323.15 |
0.6000 |
0.6600 |
317.00 |
323.15 |
0.7000 |
0.6490 |
317.00 |
323.15 |
0.8000 |
0.5500 |
317.00 |
323.15 |
0.9010 |
0.3310 |
317.00 |
323.15 |
0.9010 |
0.3270 |
317.00 |
323.15 |
0.9270 |
0.2270 |
204.00 |
322.60 |
0.0990 |
0.1040 |
204.00 |
322.60 |
0.1980 |
0.2400 |
204.00 |
322.60 |
0.3000 |
0.3860 |
204.00 |
322.60 |
0.3990 |
0.5130 |
204.00 |
322.60 |
0.4980 |
0.6090 |
204.00 |
322.60 |
0.5990 |
0.6640 |
204.00 |
322.60 |
0.6980 |
0.6510 |
204.00 |
322.60 |
0.6980 |
0.6500 |
204.00 |
322.60 |
0.7990 |
0.5530 |
204.00 |
322.60 |
0.8990 |
0.3310 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Mole fraction of Propane, 2-methoxy-2-methyl- (2) - Liquid |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
1.0000 |
323.20 |
86.00 |
0.9350 |
323.20 |
81.10 |
0.8720 |
323.16 |
76.60 |
0.7970 |
323.16 |
71.50 |
0.7100 |
322.94 |
65.30 |
0.7250 |
323.15 |
66.90 |
0.6070 |
323.14 |
59.20 |
0.5090 |
323.19 |
52.80 |
0.3790 |
323.16 |
43.30 |
0.3320 |
323.20 |
39.50 |
0.2590 |
323.22 |
33.60 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Mole fraction of Propane, 2-methoxy-2-methyl- (2) - Liquid |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
1.0000 |
323.20 |
86.00 |
0.9350 |
323.20 |
81.10 |
0.8720 |
323.16 |
76.60 |
0.7970 |
323.16 |
71.50 |
0.7100 |
322.94 |
65.30 |
0.7250 |
323.15 |
66.90 |
0.6070 |
323.14 |
59.20 |
0.5090 |
323.19 |
52.80 |
0.3790 |
323.16 |
43.30 |
0.3320 |
323.20 |
39.50 |
0.2590 |
323.22 |
33.60 |
Boiling temperature at pressure P, K
[ref]
Operational condition: Pressure, kPa =
90.1 (Liquid)
Mole fraction of Propane, 2-methoxy-2-methyl- (2) - Liquid |
Boiling temperature at pressure P, K - Liquid |
0.0000 |
371.85 |
0.0640 |
365.95 |
0.0900 |
363.25 |
0.1100 |
361.95 |
0.1430 |
359.35 |
0.1850 |
356.35 |
0.2170 |
354.15 |
0.2380 |
352.65 |
0.2650 |
351.05 |
0.2980 |
349.25 |
0.3000 |
348.85 |
0.3210 |
347.65 |
0.3410 |
346.35 |
0.3720 |
344.55 |
0.4100 |
342.65 |
0.4470 |
340.95 |
0.5120 |
338.45 |
0.6780 |
332.95 |
0.7680 |
330.45 |
0.8460 |
328.45 |
0.9090 |
326.75 |
0.9750 |
325.05 |
1.0000 |
324.45 |
Boiling temperature at pressure P, K
[ref]
Operational condition: Pressure, kPa =
90.1 (Liquid)
Mole fraction of Propane, 2-methoxy-2-methyl- (2) - Liquid |
Boiling temperature at pressure P, K - Liquid |
0.0000 |
371.85 |
0.0640 |
365.95 |
0.0900 |
363.25 |
0.1100 |
361.95 |
0.1430 |
359.35 |
0.1850 |
356.35 |
0.2170 |
354.15 |
0.2380 |
352.65 |
0.2650 |
351.05 |
0.2980 |
349.25 |
0.3000 |
348.85 |
0.3210 |
347.65 |
0.3410 |
346.35 |
0.3720 |
344.55 |
0.4100 |
342.65 |
0.4470 |
340.95 |
0.5120 |
338.45 |
0.6780 |
332.95 |
0.7680 |
330.45 |
0.8460 |
328.45 |
0.9090 |
326.75 |
0.9750 |
325.05 |
1.0000 |
324.45 |
Sources