Mixture of n-Hexane + Pentane, 1-chloro-
Datasets
-
Mole fraction (2)
-
Pvap - Vapor or sublimation pressure, kPa (2)
-
γ - Surface tension liquid-gas, N/m (2)
Mole fraction of n-Hexane (1)
[ref]
Fixed |
Measured |
Mole fraction of n-Hexane (1) - Gas |
Temperature, K - Liquid |
Mole fraction of n-Hexane (1) - Liquid |
0.2359 |
308.15 |
0.0471 |
0.3178 |
288.15 |
0.0643 |
0.3178 |
298.15 |
0.0643 |
0.3706 |
308.15 |
0.0863 |
0.4075 |
288.15 |
0.0769 |
0.4289 |
298.15 |
0.1033 |
0.4480 |
308.15 |
0.1188 |
0.5479 |
288.15 |
0.1328 |
0.5497 |
308.15 |
0.1711 |
0.5969 |
298.15 |
0.1898 |
0.6274 |
288.15 |
0.1792 |
0.6520 |
308.15 |
0.2514 |
0.6902 |
308.15 |
0.3004 |
0.7251 |
288.15 |
0.2697 |
0.7387 |
298.15 |
0.3239 |
0.7940 |
308.15 |
0.4506 |
0.7966 |
298.15 |
0.4282 |
0.8005 |
288.15 |
0.3753 |
0.8407 |
308.15 |
0.5483 |
0.8467 |
298.15 |
0.5420 |
0.8488 |
288.15 |
0.4962 |
0.8727 |
288.15 |
0.5668 |
0.8741 |
298.15 |
0.5964 |
0.8812 |
308.15 |
0.6440 |
0.8983 |
298.15 |
0.6790 |
0.9044 |
288.15 |
0.6557 |
0.9200 |
308.15 |
0.7530 |
0.9287 |
298.15 |
0.7621 |
0.9294 |
288.15 |
0.7586 |
0.9417 |
288.15 |
0.7999 |
0.9423 |
308.15 |
0.8221 |
0.9445 |
298.15 |
0.8296 |
0.9683 |
298.15 |
0.8998 |
0.9728 |
308.15 |
0.9195 |
0.9799 |
298.15 |
0.9395 |
Mole fraction of n-Hexane (1)
[ref]
Fixed |
Measured |
Mole fraction of n-Hexane (1) - Gas |
Temperature, K - Liquid |
Mole fraction of n-Hexane (1) - Liquid |
0.2359 |
308.15 |
0.0471 |
0.3178 |
288.15 |
0.0643 |
0.3178 |
298.15 |
0.0643 |
0.3706 |
308.15 |
0.0863 |
0.4075 |
288.15 |
0.0769 |
0.4289 |
298.15 |
0.1033 |
0.4480 |
308.15 |
0.1188 |
0.5479 |
288.15 |
0.1328 |
0.5497 |
308.15 |
0.1711 |
0.5969 |
298.15 |
0.1898 |
0.6274 |
288.15 |
0.1792 |
0.6520 |
308.15 |
0.2514 |
0.6902 |
308.15 |
0.3004 |
0.7251 |
288.15 |
0.2697 |
0.7387 |
298.15 |
0.3239 |
0.7940 |
308.15 |
0.4506 |
0.7966 |
298.15 |
0.4282 |
0.8005 |
288.15 |
0.3753 |
0.8407 |
308.15 |
0.5483 |
0.8467 |
298.15 |
0.5420 |
0.8488 |
288.15 |
0.4962 |
0.8727 |
288.15 |
0.5668 |
0.8741 |
298.15 |
0.5964 |
0.8812 |
308.15 |
0.6440 |
0.8983 |
298.15 |
0.6790 |
0.9044 |
288.15 |
0.6557 |
0.9200 |
308.15 |
0.7530 |
0.9287 |
298.15 |
0.7621 |
0.9294 |
288.15 |
0.7586 |
0.9417 |
288.15 |
0.7999 |
0.9423 |
308.15 |
0.8221 |
0.9445 |
298.15 |
0.8296 |
0.9683 |
298.15 |
0.8998 |
0.9728 |
308.15 |
0.9195 |
0.9799 |
298.15 |
0.9395 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Mole fraction of n-Hexane (1) - Gas |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
0.2359 |
308.15 |
8.49 |
0.3178 |
288.15 |
5.62 |
0.3178 |
298.15 |
5.62 |
0.3706 |
308.15 |
9.90 |
0.4075 |
288.15 |
3.68 |
0.4289 |
298.15 |
6.57 |
0.4480 |
308.15 |
10.90 |
0.5479 |
288.15 |
4.38 |
0.5497 |
308.15 |
12.47 |
0.5969 |
298.15 |
8.32 |
0.6274 |
288.15 |
5.07 |
0.6520 |
308.15 |
15.00 |
0.6902 |
308.15 |
16.16 |
0.7251 |
288.15 |
6.21 |
0.7387 |
298.15 |
10.93 |
0.7940 |
308.15 |
20.00 |
0.7966 |
298.15 |
12.76 |
0.8005 |
288.15 |
7.50 |
0.8407 |
308.15 |
22.05 |
0.8467 |
298.15 |
14.34 |
0.8488 |
288.15 |
8.64 |
0.8727 |
288.15 |
9.30 |
0.8741 |
298.15 |
15.05 |
0.8812 |
308.15 |
23.90 |
0.8983 |
298.15 |
16.25 |
0.9044 |
288.15 |
10.11 |
0.9200 |
308.15 |
26.12 |
0.9287 |
298.15 |
17.27 |
0.9294 |
288.15 |
11.00 |
0.9417 |
288.15 |
11.29 |
0.9423 |
308.15 |
27.32 |
0.9445 |
298.15 |
18.09 |
0.9683 |
298.15 |
18.91 |
0.9728 |
308.15 |
29.11 |
0.9799 |
298.15 |
19.42 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Mole fraction of n-Hexane (1) - Gas |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
0.2359 |
308.15 |
8.49 |
0.3178 |
288.15 |
5.62 |
0.3178 |
298.15 |
5.62 |
0.3706 |
308.15 |
9.90 |
0.4075 |
288.15 |
3.68 |
0.4289 |
298.15 |
6.57 |
0.4480 |
308.15 |
10.90 |
0.5479 |
288.15 |
4.38 |
0.5497 |
308.15 |
12.47 |
0.5969 |
298.15 |
8.32 |
0.6274 |
288.15 |
5.07 |
0.6520 |
308.15 |
15.00 |
0.6902 |
308.15 |
16.16 |
0.7251 |
288.15 |
6.21 |
0.7387 |
298.15 |
10.93 |
0.7940 |
308.15 |
20.00 |
0.7966 |
298.15 |
12.76 |
0.8005 |
288.15 |
7.50 |
0.8407 |
308.15 |
22.05 |
0.8467 |
298.15 |
14.34 |
0.8488 |
288.15 |
8.64 |
0.8727 |
288.15 |
9.30 |
0.8741 |
298.15 |
15.05 |
0.8812 |
308.15 |
23.90 |
0.8983 |
298.15 |
16.25 |
0.9044 |
288.15 |
10.11 |
0.9200 |
308.15 |
26.12 |
0.9287 |
298.15 |
17.27 |
0.9294 |
288.15 |
11.00 |
0.9417 |
288.15 |
11.29 |
0.9423 |
308.15 |
27.32 |
0.9445 |
298.15 |
18.09 |
0.9683 |
298.15 |
18.91 |
0.9728 |
308.15 |
29.11 |
0.9799 |
298.15 |
19.42 |
Surface tension liquid-gas, N/m
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of n-Hexane (1) - Liquid |
Surface tension liquid-gas, N/m - Liquid |
283.15 |
0.0482 |
0.0254 |
283.15 |
0.1185 |
0.0247 |
283.15 |
0.1991 |
0.0240 |
283.15 |
0.3080 |
0.0232 |
283.15 |
0.3925 |
0.0226 |
283.15 |
0.5087 |
0.0219 |
283.15 |
0.5953 |
0.0214 |
283.15 |
0.7076 |
0.0209 |
283.15 |
0.7889 |
0.0205 |
283.15 |
0.9069 |
0.0200 |
283.15 |
0.9474 |
0.0198 |
288.15 |
0.0482 |
0.0250 |
288.15 |
0.1185 |
0.0243 |
288.15 |
0.1991 |
0.0236 |
288.15 |
0.3080 |
0.0228 |
288.15 |
0.3925 |
0.0222 |
288.15 |
0.5087 |
0.0214 |
288.15 |
0.5953 |
0.0209 |
288.15 |
0.7076 |
0.0204 |
288.15 |
0.7889 |
0.0200 |
288.15 |
0.9069 |
0.0194 |
288.15 |
0.9474 |
0.0192 |
293.15 |
0.0482 |
0.0245 |
293.15 |
0.1185 |
0.0238 |
293.15 |
0.1991 |
0.0231 |
293.15 |
0.3080 |
0.0222 |
293.15 |
0.3925 |
0.0217 |
293.15 |
0.5087 |
0.0209 |
293.15 |
0.5953 |
0.0205 |
293.15 |
0.7076 |
0.0199 |
293.15 |
0.7889 |
0.0195 |
293.15 |
0.9069 |
0.0189 |
293.15 |
0.9474 |
0.0187 |
298.15 |
0.0482 |
0.0240 |
298.15 |
0.1185 |
0.0233 |
298.15 |
0.1991 |
0.0226 |
298.15 |
0.3080 |
0.0218 |
298.15 |
0.3925 |
0.0212 |
298.15 |
0.5087 |
0.0205 |
298.15 |
0.5953 |
0.0200 |
298.15 |
0.7076 |
0.0194 |
298.15 |
0.7889 |
0.0190 |
298.15 |
0.9069 |
0.0185 |
298.15 |
0.9474 |
0.0183 |
303.15 |
0.0482 |
0.0236 |
303.15 |
0.1185 |
0.0230 |
303.15 |
0.1991 |
0.0222 |
303.15 |
0.3080 |
0.0214 |
303.15 |
0.3925 |
0.0208 |
303.15 |
0.5087 |
0.0200 |
303.15 |
0.5953 |
0.0196 |
303.15 |
0.7076 |
0.0190 |
303.15 |
0.7889 |
0.0186 |
303.15 |
0.9069 |
0.0180 |
303.15 |
0.9474 |
0.0178 |
308.15 |
0.0482 |
0.0231 |
308.15 |
0.1185 |
0.0225 |
308.15 |
0.1991 |
0.0217 |
308.15 |
0.3080 |
0.0208 |
308.15 |
0.3925 |
0.0202 |
308.15 |
0.5087 |
0.0194 |
308.15 |
0.5953 |
0.0189 |
308.15 |
0.7076 |
0.0183 |
308.15 |
0.7889 |
0.0179 |
308.15 |
0.9069 |
0.0173 |
308.15 |
0.9474 |
0.0170 |
313.15 |
0.0482 |
0.0226 |
313.15 |
0.1185 |
0.0220 |
313.15 |
0.1991 |
0.0213 |
313.15 |
0.3080 |
0.0204 |
313.15 |
0.3925 |
0.0198 |
313.15 |
0.5087 |
0.0191 |
313.15 |
0.5953 |
0.0186 |
313.15 |
0.7076 |
0.0180 |
313.15 |
0.7889 |
0.0176 |
313.15 |
0.9069 |
0.0170 |
313.15 |
0.9474 |
0.0168 |
Surface tension liquid-gas, N/m
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of n-Hexane (1) - Liquid |
Surface tension liquid-gas, N/m - Liquid |
283.15 |
0.0482 |
0.0254 |
283.15 |
0.1185 |
0.0247 |
283.15 |
0.1991 |
0.0240 |
283.15 |
0.3080 |
0.0232 |
283.15 |
0.3925 |
0.0226 |
283.15 |
0.5087 |
0.0219 |
283.15 |
0.5953 |
0.0214 |
283.15 |
0.7076 |
0.0209 |
283.15 |
0.7889 |
0.0205 |
283.15 |
0.9069 |
0.0200 |
283.15 |
0.9474 |
0.0198 |
288.15 |
0.0482 |
0.0250 |
288.15 |
0.1185 |
0.0243 |
288.15 |
0.1991 |
0.0236 |
288.15 |
0.3080 |
0.0228 |
288.15 |
0.3925 |
0.0222 |
288.15 |
0.5087 |
0.0214 |
288.15 |
0.5953 |
0.0209 |
288.15 |
0.7076 |
0.0204 |
288.15 |
0.7889 |
0.0200 |
288.15 |
0.9069 |
0.0194 |
288.15 |
0.9474 |
0.0192 |
293.15 |
0.0482 |
0.0245 |
293.15 |
0.1185 |
0.0238 |
293.15 |
0.1991 |
0.0231 |
293.15 |
0.3080 |
0.0222 |
293.15 |
0.3925 |
0.0217 |
293.15 |
0.5087 |
0.0209 |
293.15 |
0.5953 |
0.0205 |
293.15 |
0.7076 |
0.0199 |
293.15 |
0.7889 |
0.0195 |
293.15 |
0.9069 |
0.0189 |
293.15 |
0.9474 |
0.0187 |
298.15 |
0.0482 |
0.0240 |
298.15 |
0.1185 |
0.0233 |
298.15 |
0.1991 |
0.0226 |
298.15 |
0.3080 |
0.0218 |
298.15 |
0.3925 |
0.0212 |
298.15 |
0.5087 |
0.0205 |
298.15 |
0.5953 |
0.0200 |
298.15 |
0.7076 |
0.0194 |
298.15 |
0.7889 |
0.0190 |
298.15 |
0.9069 |
0.0185 |
298.15 |
0.9474 |
0.0183 |
303.15 |
0.0482 |
0.0236 |
303.15 |
0.1185 |
0.0230 |
303.15 |
0.1991 |
0.0222 |
303.15 |
0.3080 |
0.0214 |
303.15 |
0.3925 |
0.0208 |
303.15 |
0.5087 |
0.0200 |
303.15 |
0.5953 |
0.0196 |
303.15 |
0.7076 |
0.0190 |
303.15 |
0.7889 |
0.0186 |
303.15 |
0.9069 |
0.0180 |
303.15 |
0.9474 |
0.0178 |
308.15 |
0.0482 |
0.0231 |
308.15 |
0.1185 |
0.0225 |
308.15 |
0.1991 |
0.0217 |
308.15 |
0.3080 |
0.0208 |
308.15 |
0.3925 |
0.0202 |
308.15 |
0.5087 |
0.0194 |
308.15 |
0.5953 |
0.0189 |
308.15 |
0.7076 |
0.0183 |
308.15 |
0.7889 |
0.0179 |
308.15 |
0.9069 |
0.0173 |
308.15 |
0.9474 |
0.0170 |
313.15 |
0.0482 |
0.0226 |
313.15 |
0.1185 |
0.0220 |
313.15 |
0.1991 |
0.0213 |
313.15 |
0.3080 |
0.0204 |
313.15 |
0.3925 |
0.0198 |
313.15 |
0.5087 |
0.0191 |
313.15 |
0.5953 |
0.0186 |
313.15 |
0.7076 |
0.0180 |
313.15 |
0.7889 |
0.0176 |
313.15 |
0.9069 |
0.0170 |
313.15 |
0.9474 |
0.0168 |
Sources