This work deals with high-pressure phase behavior of the industrially impor
tant polymeric systems polyethylene/ethylene and polybutene/ 1-butene. New
experimental data in the pressure range 9 to 17 MPa and the temperature ran
ge 405 to 447 K are presented for the system polybutene/1-butene. The polyb
utene sample has mass-average and number-average molar masses of 1.28 x 10(
6) and 0.27 x 10(6), respectively. The polymer concentration ranges from 0.
31 to 16.65 mass percent polymer. The system is found to show LCST behavior
. The data on the polybutene/1-butene system along with data on mixtures of
polyethylene and ethylene reported by de Loos et al. [Th.W. de Loos, W. Po
ot, G.A.M. Diepen, Macromolecules 16 (1983) 111-117] are modeled using the
SAFT and Sanchez-Lacombe (SL) equations of state. Two samples of polyethyle
ne are investigated. One has a mass-average molar mass of 99 000 and number
-average molar mass of 56 000 and the other sample has mass-average and num
ber-average molar masses of 8800 and 7600, respectively. Phase equilibrium
calculations are performed for two cases: (i) the polymer is treated as mon
odisperse, and, (ii) the polydispersity of the polymer is accounted for by
characterizing the polymer by pseudocomponents. The polydispersity of the p
olymer has a significant effect on the phase behavior of the systems invest
igated in this work. Also, sometimes the polymer parameters have to be adju
sted to the mixture data to get a reasonable correlation (C) 1999 Elsevier
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