2000
DOI: 10.1016/s0378-3812(00)00319-8
|View full text |Cite
|
Sign up to set email alerts
|

Vapor–liquid equilibrium ratios for hexane at infinite dilution in ethylene+impact polypropylene copolymer and propylene+impact polypropylene copolymer

Help me understand this report

Search citation statements

Order By: Relevance

Paper Sections

Select...
3
1
1

Citation Types

2
23
0

Year Published

2004
2004
2023
2023

Publication Types

Select...
9

Relationship

0
9

Authors

Journals

citations
Cited by 33 publications
(25 citation statements)
references
References 36 publications
2
23
0
Order By: Relevance
“…This variable was chosen for three reasons: (i) diffusion of n-pentane in PS is concentration dependent, so the starting pressure and the end pressure do not correctly characterize the pressure-step, (ii) the use of activity enables better comparison of the individual experiments, and (iii) the activity was used by other authors studying the diffusion of n-pentane in PS. 41,55,67,68 The value of a mid is calculated as (18) where p st and p end are the pressures before and after the pressure-step, respectively, and p sat is the saturated vapor pressure at the relevant temperature. Figure 6 shows diffusion coefficients increasing with T and a mid in agreement with theoretical expectations and previous studies.…”
Section: Diffusion In Thin Polystyrenementioning
confidence: 99%
“…This variable was chosen for three reasons: (i) diffusion of n-pentane in PS is concentration dependent, so the starting pressure and the end pressure do not correctly characterize the pressure-step, (ii) the use of activity enables better comparison of the individual experiments, and (iii) the activity was used by other authors studying the diffusion of n-pentane in PS. 41,55,67,68 The value of a mid is calculated as (18) where p st and p end are the pressures before and after the pressure-step, respectively, and p sat is the saturated vapor pressure at the relevant temperature. Figure 6 shows diffusion coefficients increasing with T and a mid in agreement with theoretical expectations and previous studies.…”
Section: Diffusion In Thin Polystyrenementioning
confidence: 99%
“…Different thermodynamics models have been developed and tested for the validation and prediction of monomer solubility in polymers. Activity coefficient models (ACM) and equations of state (EOS) models are well established classes of thermodynamic models that have been used extensively for the prediction of equilibrium monomer solubility in polymers 1–13. However, there is no universal thermodynamic model for the prediction of monomer(s) solubility in polymers at commonly implemented process conditions.…”
Section: Introductionmentioning
confidence: 99%
“…These parameters are considered as an alternative to critical constants used by other EOS for light compounds24, 25 and, therefore, the precise estimation of these parameters is of high importance for the SL EOS predictions in monomer/polymer systems. In general, the pure component characteristic parameters used in SL EOS can be estimated by: i) regressing the PVT data of pure components,2, 8, 11, 20, 21, 26, 27 ii) using group contribution methods,24, 25 iii) using parameterization method28 and iv) using molecular dynamics simulations 1. Depending on the accuracy of these methods, different values for the characteristic parameters are obtained.…”
Section: Introductionmentioning
confidence: 99%
“…First, two binary systems have to be studied in order to accurately determine the solubility of different propylene–hexane mixtures in PP at 343.2 K: Propylene–PP and hexane–PP. Our model was fitted to the experimental data from Sato et al The binary interaction parameters for each case are shown in Table .…”
Section: Methodsmentioning
confidence: 99%