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) x (mol mol-1)
0 0.0
0.4002 0.4641
0.4499 0.4781
0.4502 0.4782
0.5000 0.497
0.5003 0.4971
0.5500 0.5214
0.5502 0.5215
0.6000 0.5507
0.6002 0.5508
0.6503 0.5832
0.0500 0.3638
0.6912 0.6102
0.7503 0.6488
0.8004 0.6823
0.8505 0.7228
0.9005 0.7825
0.9503 0.8769
1 1.0
0.0997 0.3928
0.1499 0.4053
0.1997 0.4184
0.2498 0.4314
0.2996 0.4427
0.3498 0.4529
0.3999 0.464
35907; pentan-1-ol + 1,2,4-trimethylbenzene; 00113:00923