Vapor-liquid equilibria and excess enthalpies of the binary systems 1-pentanol or 2-pentanol and 1-hexene or 1,2,4-trimethylbenzene for the development of biofuels Moreau, A.; Segovia, J.J.; Bermejo, M.D.; Martí­n, M.C.; Fluid Phase Equilibria 2018, 460, 85-94
Data
T = 313.15 K
x (mol mol-1) P (kPa)
0 44.954
0.4015 37.838
0.4514 36.671
0.4516 36.656
0.5016 35.363
0.5018 35.35
0.5514 33.891
0.5519 33.874
0.6014 32.194
0.6022 32.175
0.6522 30.22
0.0498 43.919
0.7024 27.937
0.7523 25.288
0.8022 22.18
0.8520 18.481
0.9018 14.0
0.9509 8.634
1 2.281
0.1004 43.129
0.1502 42.445
0.2007 41.709
0.2521 40.857
0.3011 39.951
0.3513 38.94
0.4013 37.85
7324; 1-hexene + 2-pentanol; 00487:00650