1995
DOI: 10.1021/ie00044a033
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Prediction of Liquid-Liquid Equilibrium for Binary Polymer Solutions with Simple Activity Coefficient Models

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Cited by 49 publications
(34 citation statements)
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“…The experimental solvent weight‐fraction activity coefficients at 298.15 K, Ω 2exp ∞ , presented in Table 8 are, for example, 5.83 for iPBu‐1/cyclohexane and 9.55 for iPBu‐1/benzene. These data are comparable to the literature values for polyisobutylene (PIB) at 323.2 K: 4.56 for PIB(53 000)/cyclohexane17b and 5.90 PIB(53 000)/benzene 17c. Recently it was stated17a that the infinite dilution solvent weight‐fraction‐based activity coefficients, Ω 2pred ∞ , of a polyolefin could be assumed to be constant (4.39), independent of the system, the polymer molecular weight and temperature.…”
Section: Resultssupporting
confidence: 88%
“…The experimental solvent weight‐fraction activity coefficients at 298.15 K, Ω 2exp ∞ , presented in Table 8 are, for example, 5.83 for iPBu‐1/cyclohexane and 9.55 for iPBu‐1/benzene. These data are comparable to the literature values for polyisobutylene (PIB) at 323.2 K: 4.56 for PIB(53 000)/cyclohexane17b and 5.90 PIB(53 000)/benzene 17c. Recently it was stated17a that the infinite dilution solvent weight‐fraction‐based activity coefficients, Ω 2pred ∞ , of a polyolefin could be assumed to be constant (4.39), independent of the system, the polymer molecular weight and temperature.…”
Section: Resultssupporting
confidence: 88%
“…Adjustable characteristic energy parameters of the various models were regressed using binary experimental LLE data available in (12) where w exp i and w cal i are experimental and calculated mass fractions, respectively, for all components. The summations are extended to the number of experimental tie lines, nexp, and to the number of components, ncomp.…”
Section: Results and Discussion For Liquid-liquid Equilibriummentioning
confidence: 99%
“…The activity of the polymer is a predominant factor in LLE (liquid-liquid equilibrium) calculations for polymer solutions. A large number of equations of state and activity coefficient models capable of describing phase equilibrium in polymer solutions are available today, but only a few of these models have been tested for several different systems [9,12,13]. The studies in the literature normally focus on the residual contribution for a fixed free-volume contribution [14,15].…”
Section: Introductionmentioning
confidence: 99%
“…In spite of this limitation, a database including temperature-dependent segmental interaction energies is expected to be valuable not only for practical reasons but also for testing new copolymer blend theories [37]. At least for mixtures of low molecular weight compounds, such a compilation has been found to be very successful [39]. In this paper, the binary interaction model with temperature-dependent v ij parameters is employed for the modeling of the phase behavior of binary and ternary blends involving copolymers of styrene (S), methyl methacrylate (MMA) and cyclohexyl methacrylate (CHMA).…”
Section: Introductionmentioning
confidence: 99%