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 44.914
0.4016 38.713
0.4517 37.717
0.4518 37.672
0.5017 36.487
0.5019 36.529
0.5517 35.097
0.5521 35.144
0.6021 33.446
0.6024 33.498
0.6527 31.526
0.0492 43.855
0.7025 29.174
0.7528 26.304
0.8028 22.866
0.8526 18.716
0.8999 14.05
0.9493 8.159
1 0.913
0.0995 43.191
0.1503 42.546
0.2007 41.892
0.2511 41.184
0.3014 40.452
0.3516 39.624
0.4014 38.751
35906; pentan-1-ol + hex-1-ene; 00113:00650