2003
DOI: 10.1021/ie030092b
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Sorption Thermodynamics and Mutual Diffusivity of Carbon Dioxide in Molten Polycaprolactone

Abstract: Solution thermodynamics and mutual diffusivity of the system carbon dioxide-molten poly(caprolactone) (PCL) have been investigated experimentally in the temperature range 70-85 °C and at pressures up to 6.5 MPa. Sorption data have been interpreted on the basis of Sanchez-Lacombe lattice theory. Sanchez-Lacombe parameters for pure PCL have been evaluated by fitting experimental pressure-volume-temperature data obtained by using a high-pressure dilatometer, while parameters for carbon dioxide have been taken fro… Show more

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Cited by 37 publications
(35 citation statements)
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“…The depression in melting point (T m ) or glass transition (T g ) temperature in polymers due to the sorption of CO 2 is a well-known phenomenon which is dependent on various factors such as crystallinity and presence of CO 2 -philic moieties [9][10][11][12][13][14] . Amorphous polymers are reported to show higher interactions with CO 2 than crystalline polymers 15,16 .…”
Section: Introduction-mentioning
confidence: 99%
“…The depression in melting point (T m ) or glass transition (T g ) temperature in polymers due to the sorption of CO 2 is a well-known phenomenon which is dependent on various factors such as crystallinity and presence of CO 2 -philic moieties [9][10][11][12][13][14] . Amorphous polymers are reported to show higher interactions with CO 2 than crystalline polymers 15,16 .…”
Section: Introduction-mentioning
confidence: 99%
“…Full details about the experimental procedure are given elsewhere (see Supporting Information Fig. S1) . The spring (Ruska, Houston, TX), whose sensibility is 0.0005 g/mm, is inserted in a water jacketed glass column, to keep the temperature constant within to ±0.1°C.…”
Section: Methodsmentioning
confidence: 99%
“…As expected, the rheological curves of both the mixture containing 2.3% of CO 2 and the mixture containing 1.5% of N 2 are shifted to lower values with respect to pure PCL, maintaining a similar dependence on shear rate. To use eq 15 to predict these experimental data, the following parameters were used for the pure PCL T = 100 °C, P = 40bar, V 1 = 0.9609 cm 3 /g, from experimental data ( T is set in the capillary zone of the extrusion line, P is the mean pressure inside of the capillary, V 1 is measured by PVT tests51) h 1 = 0.1049, obtained from the experimental PVT data and eq 10, h = 1− y for the mixture with ω c = 2.3 wt % of CO 2 T = 100 °C, P = 80 bar, from experimental, extrusion data V 2 = 0.9585; h 2 = 0.1092, obtained theoretically using the SS‐EOS For the mixture with ω c = 1.5 wt % of N 2 T = 100 °C, P = 120 bar, from experimental, extrusion data V 2 = 0.9647; h 2 = 0.1064, obtained theoretically using the SS‐EOS …”
Section: Methodsmentioning
confidence: 99%
“…for the pure PCL T = 100 °C, P = 40bar, V 1 = 0.9609 cm 3 /g, from experimental data ( T is set in the capillary zone of the extrusion line, P is the mean pressure inside of the capillary, V 1 is measured by PVT tests51) h 1 = 0.1049, obtained from the experimental PVT data and eq 10, h = 1− y …”
Section: Methodsmentioning
confidence: 99%