PHASE-EQUILIBRIA OF BINARY AND TERNARY N-ALKANE SOLUTIONS IN SUPERCRITICAL ETHYLENE, 1-BUTENE, AND ETHYLENE PLUS 1-BUTENE - TRANSITION FROMTYPE-A THROUGH LCST TO U-LCST BEHAVIOR PREDICTED AND CONFIRMED EXPERIMENTALLY
Cj. Gregg et al., PHASE-EQUILIBRIA OF BINARY AND TERNARY N-ALKANE SOLUTIONS IN SUPERCRITICAL ETHYLENE, 1-BUTENE, AND ETHYLENE PLUS 1-BUTENE - TRANSITION FROMTYPE-A THROUGH LCST TO U-LCST BEHAVIOR PREDICTED AND CONFIRMED EXPERIMENTALLY, Industrial & engineering chemistry research, 32(7), 1993, pp. 1442-1448
Binary phase equilibria of C20 +, C30 +, and C40 + ethylene are correl
ated with three equations of state, the Redlich-Kwong-Soave (Soave), t
he generalized van der Waals-Prigogine (vdW-P), and the statistical as
sociating fluid theory (SAFT), with special emphasis on the mixture cr
itical region. The SAFT correlation is found to be the most reliable.
SAFT predictive powers are tested on C26 + ethylene and a new set of e
xperimental data taken in this work for C36 + 1-butene and C36 + ethyl
ene + 1-butene. The SAFT predictions are found to be in good agreement
with the experimental data. Equally important, the SAFT predictions a
llow for understanding the continuous transition of phase behavior, fr
om type A (C36 + 1-butene) through LCST (C36 + ethylene + 1-butene) to
U-LCST (C36 + ethylene).