1996
DOI: 10.1002/(sici)1099-0488(199603)34:4<761::aid-polb17>3.0.co;2-f
|View full text |Cite
|
Sign up to set email alerts
|

Finite difference modeling of the gas transport process in glassy polymers

Help me understand this report

Search citation statements

Order By: Relevance

Paper Sections

Select...
2
1
1
1

Citation Types

0
5
0

Year Published

2001
2001
2015
2015

Publication Types

Select...
5

Relationship

0
5

Authors

Journals

citations
Cited by 5 publications
(5 citation statements)
references
References 9 publications
0
5
0
Order By: Relevance
“…The relationship between volume fraction of crystallinity and linear crystallinity is expressed as V = , where is the fraction of the total volume of the sample occupied by stacks of lamellae [51]. Using the densities of the crystalline ( = 1.445 g/cm 3 ) and amorphous ( = 1.331 g/cm 3 ) phases for PET [52], the volume fraction crystallinity ( V = ) was transformed into mass fraction of crystallinity , according to Swam equation [53]:…”
Section: Characterization Techniques the Inherent Viscosity [ ]mentioning
confidence: 99%
“…The relationship between volume fraction of crystallinity and linear crystallinity is expressed as V = , where is the fraction of the total volume of the sample occupied by stacks of lamellae [51]. Using the densities of the crystalline ( = 1.445 g/cm 3 ) and amorphous ( = 1.331 g/cm 3 ) phases for PET [52], the volume fraction crystallinity ( V = ) was transformed into mass fraction of crystallinity , according to Swam equation [53]:…”
Section: Characterization Techniques the Inherent Viscosity [ ]mentioning
confidence: 99%
“…Intermediate values of n suggest a combination of these two mechanisms. On the other hand, the discrepancies between the experimental sorption and desorption curves are representative of different kinetics and then, of a concentration-dependent diffusion coefficient (Crank, 1975;Brolly et al, 1996aBrolly et al, , 1996b). …”
Section: Mechanisms Of Diffusionmentioning
confidence: 99%
“…According to them, the dualmode sorption model is based on a correct mathematical description but on invalid physical assumptions, which are the existence of two different populations of diffusing molecules and the absence of gas-polymer interactions. Also, let us quote Brolly et al (1996aBrolly et al ( , 1996b who determined experimentally the effective coefficients of solubility and diffusion of CO 2 in PET and in PEN, at room temperature, the pressure varying from 0.0125 to 0.5 MPa. These authors used the finite difference modelling for obtaining the parameters relative to the two models and so the variations of the effective diffusion coefficient with the penetrant concentration.…”
Section: Comparison Of These Two Modelsmentioning
confidence: 99%
“…The desorption experiments, Figure 2 (right) and Table 1, show remarkably large effective diffusivities, particularly after equilibration at the higher pressures. However, if the local diffusivity was to decrease during desorption instantaneously to the value from eq 17 corresponding to the local C D , then desorption would be slower than sorption 14, 26. In the specimen's skin region, where C D is smallest and ∂ C D /∂ X is largest, D D would be the least; a layer of low permeability near the surface would hinder the loss of vapor from the interior.…”
Section: Resultsmentioning
confidence: 99%
“…Similar observations of the effect of pressure on the diffusion coefficient were made by Kumar and Stolarczuk24 for the CO 2 ‐poly(ethylene terephthalate) system and by Kumar and Weller25 for the CO 2 ‐polycarbonate system. Brolly et al26 investigated the variation in the diffusion coefficients with penetrant pressure for the CO 2 ‐poly(ethylene terephthalate) and CO 2 ‐poly(ethylene naphthalate) systems. They found a significant rise in the effective diffusion coefficient as a result of an increase in pressure.…”
Section: Resultsmentioning
confidence: 99%