Operational condition: Pressure, kPa = 101.3 (Liquid)
Mole fraction of Carbonic acid, dimethyl ester (2) - Liquid | Mole fraction of Carbonic acid, dimethyl ester (2) - Gas |
---|---|
0.0078 | 0.0194 |
0.0469 | 0.0940 |
0.0874 | 0.1549 |
0.1211 | 0.2014 |
0.1600 | 0.2523 |
0.1954 | 0.2975 |
0.2289 | 0.3363 |
0.2570 | 0.3663 |
0.2861 | 0.3955 |
0.3120 | 0.4243 |
0.3516 | 0.4621 |
0.3925 | 0.5052 |
0.4175 | 0.5233 |
0.4417 | 0.5482 |
0.4671 | 0.5673 |
0.4917 | 0.5873 |
0.5210 | 0.6141 |
0.5539 | 0.6413 |
0.5824 | 0.6727 |
0.6006 | 0.6869 |
0.6280 | 0.7083 |
0.6526 | 0.7245 |
0.6697 | 0.7398 |
0.6850 | 0.7527 |
0.6857 | 0.7523 |
0.7120 | 0.7716 |
0.7343 | 0.7878 |
0.7443 | 0.7953 |
0.7630 | 0.8094 |
0.7858 | 0.8277 |
0.8109 | 0.8485 |
0.8460 | 0.8722 |
0.8613 | 0.8824 |
0.8853 | 0.9033 |
0.9116 | 0.9245 |
0.9308 | 0.9405 |
0.9616 | 0.9667 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
Mole fraction of Carbonic acid, dimethyl ester (2) - Liquid | Mole fraction of Carbonic acid, dimethyl ester (2) - Gas |
---|---|
0.0078 | 0.0194 |
0.0469 | 0.0940 |
0.0874 | 0.1549 |
0.1211 | 0.2014 |
0.1600 | 0.2523 |
0.1954 | 0.2975 |
0.2289 | 0.3363 |
0.2570 | 0.3663 |
0.2861 | 0.3955 |
0.3120 | 0.4243 |
0.3516 | 0.4621 |
0.3925 | 0.5052 |
0.4175 | 0.5233 |
0.4417 | 0.5482 |
0.4671 | 0.5673 |
0.4917 | 0.5873 |
0.5210 | 0.6141 |
0.5539 | 0.6413 |
0.5824 | 0.6727 |
0.6006 | 0.6869 |
0.6280 | 0.7083 |
0.6526 | 0.7245 |
0.6697 | 0.7398 |
0.6850 | 0.7527 |
0.6857 | 0.7523 |
0.7120 | 0.7716 |
0.7343 | 0.7878 |
0.7443 | 0.7953 |
0.7630 | 0.8094 |
0.7858 | 0.8277 |
0.8109 | 0.8485 |
0.8460 | 0.8722 |
0.8613 | 0.8824 |
0.8853 | 0.9033 |
0.9116 | 0.9245 |
0.9308 | 0.9405 |
0.9616 | 0.9667 |
Operational conditions:
Mole fraction of 2-Pentanone (1) - Liquid | Mass density, kg/m3 - Liquid |
---|---|
0.0000 | 1063.33 |
0.0498 | 1046.71 |
0.1004 | 1030.33 |
0.1996 | 999.49 |
0.3009 | 969.77 |
0.3980 | 942.67 |
0.5036 | 914.75 |
0.6017 | 890.1 |
0.7046 | 865.52 |
0.8012 | 843.59 |
0.9010 | 821.94 |
0.9504 | 811.55 |
1.0000 | 801.39 |
Operational conditions:
Mole fraction of 2-Pentanone (1) - Liquid | Mass density, kg/m3 - Liquid |
---|---|
0.0000 | 1063.33 |
0.0498 | 1046.71 |
0.1004 | 1030.33 |
0.1996 | 999.49 |
0.3009 | 969.77 |
0.3980 | 942.67 |
0.5036 | 914.75 |
0.6017 | 890.1 |
0.7046 | 865.52 |
0.8012 | 843.59 |
0.9010 | 821.94 |
0.9504 | 811.55 |
1.0000 | 801.39 |
Operational conditions:
Mole fraction of 2-Pentanone (1) - Liquid | Speed of sound, m/s - Liquid |
---|---|
0.0000 | 1198.0 |
0.0498 | 1199.0 |
0.1004 | 1198.0 |
0.1996 | 1197.0 |
0.3009 | 1198.0 |
0.3980 | 1198.0 |
0.5036 | 1200.0 |
0.6017 | 1201.0 |
0.7046 | 1203.0 |
0.8012 | 1206.0 |
0.9010 | 1209.0 |
0.9504 | 1211.0 |
1.0000 | 1212.0 |
Operational conditions:
Mole fraction of 2-Pentanone (1) - Liquid | Speed of sound, m/s - Liquid |
---|---|
0.0000 | 1198.0 |
0.0498 | 1199.0 |
0.1004 | 1198.0 |
0.1996 | 1197.0 |
0.3009 | 1198.0 |
0.3980 | 1198.0 |
0.5036 | 1200.0 |
0.6017 | 1201.0 |
0.7046 | 1203.0 |
0.8012 | 1206.0 |
0.9010 | 1209.0 |
0.9504 | 1211.0 |
1.0000 | 1212.0 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
Mole fraction of Carbonic acid, dimethyl ester (2) - Liquid | Boiling temperature at pressure P, K - Liquid |
---|---|
0.0078 | 375.12 |
0.0469 | 374.04 |
0.0874 | 373.13 |
0.1211 | 372.33 |
0.1600 | 371.56 |
0.1954 | 370.95 |
0.2289 | 370.43 |
0.2570 | 369.98 |
0.2861 | 369.61 |
0.3120 | 369.19 |
0.3516 | 368.69 |
0.3925 | 368.05 |
0.4175 | 367.85 |
0.4417 | 367.52 |
0.4671 | 367.29 |
0.4917 | 367.03 |
0.5210 | 366.71 |
0.5539 | 366.39 |
0.5824 | 366.02 |
0.6006 | 365.86 |
0.6280 | 365.60 |
0.6526 | 365.48 |
0.6697 | 365.33 |
0.6850 | 365.24 |
0.6857 | 365.25 |
0.7120 | 365.02 |
0.7343 | 364.86 |
0.7443 | 364.78 |
0.7630 | 364.65 |
0.7858 | 364.50 |
0.8109 | 364.31 |
0.8460 | 364.08 |
0.8613 | 363.99 |
0.8853 | 363.84 |
0.9116 | 363.67 |
0.9308 | 363.59 |
0.9616 | 363.54 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
Mole fraction of Carbonic acid, dimethyl ester (2) - Liquid | Boiling temperature at pressure P, K - Liquid |
---|---|
0.0078 | 375.12 |
0.0469 | 374.04 |
0.0874 | 373.13 |
0.1211 | 372.33 |
0.1600 | 371.56 |
0.1954 | 370.95 |
0.2289 | 370.43 |
0.2570 | 369.98 |
0.2861 | 369.61 |
0.3120 | 369.19 |
0.3516 | 368.69 |
0.3925 | 368.05 |
0.4175 | 367.85 |
0.4417 | 367.52 |
0.4671 | 367.29 |
0.4917 | 367.03 |
0.5210 | 366.71 |
0.5539 | 366.39 |
0.5824 | 366.02 |
0.6006 | 365.86 |
0.6280 | 365.60 |
0.6526 | 365.48 |
0.6697 | 365.33 |
0.6850 | 365.24 |
0.6857 | 365.25 |
0.7120 | 365.02 |
0.7343 | 364.86 |
0.7443 | 364.78 |
0.7630 | 364.65 |
0.7858 | 364.50 |
0.8109 | 364.31 |
0.8460 | 364.08 |
0.8613 | 363.99 |
0.8853 | 363.84 |
0.9116 | 363.67 |
0.9308 | 363.59 |
0.9616 | 363.54 |