Fuel 162 (2015) 91–100 Contents lists available at ScienceDirect Fuel journal homepage: www.elsevier.com/locate/fuel Minimization of Gibbs energy with phase stability test for determining vapor–liquid equilibrium of hydrogen-middle distillate systems at hydrotreating conditions Luz M. Chávez , Rodolfo A. Aguilar, Fernando Alonso, Jorge Ancheyta Instituto Mexicano del Petróleo, Eje Central Lázaro Cárdenas Norte 152, Col. San Bartolo Atepehuacan, C.P. 07730 México, D.F., Mexico highl i ghts graphical a bstrac t Good reproducibility of VLE values of 90 the trans-2-hexen-1-ol/CO system. Accurate and reliable prediction of TotalRelative the amount of vaporized LCO. Error (%) . Chen et al.  50.6 Setting of the interaction parameters This work 33.6 . taking into account the stable states. Pseudocomponents distribution in both phases at various temperatures. Experimental data Chen et al.  Min of Gibbs energy + stability test 240260 280300 320340 360 380 400 Temperature (T ), °C VLE article i nfo abstract Article history: The effect of applying the minimization of the Gibbs energy with phase stability tests on the prediction of Received 27 March 2015 the amount of vaporized middle distillate in presence of hydrogen at hydrotreating (HDT) conditions Received in revised form 21 August 2015 (70.9 bars and 250–420 C)
Fuel – Elsevier
Published: Dec 15, 2015
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