2004
DOI: 10.1016/j.polymer.2004.09.076
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Mechanism and kinetics of transesterification in poly(ethylene terephthalate) and poly(ethylene 2,6-naphthalene dicarboxylate) polymer blends

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Cited by 16 publications
(16 citation statements)
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“…Several authors have given attention to the kinetics of thistransesterification reaction describing it as a second order reversible reaction [Chen et al 1996, Lee et al, 1999, Alexandrova et al 2000. However, the equilibrium constant was considered in those works as equal to one, which presumes that the reaction of equimolar amounts of thereactants leads to equal concentrations of molar fractions of the species when the transesterification reaction reaches equilibrium.…”
Section: Wwwintechopencommentioning
confidence: 99%
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“…Several authors have given attention to the kinetics of thistransesterification reaction describing it as a second order reversible reaction [Chen et al 1996, Lee et al, 1999, Alexandrova et al 2000. However, the equilibrium constant was considered in those works as equal to one, which presumes that the reaction of equimolar amounts of thereactants leads to equal concentrations of molar fractions of the species when the transesterification reaction reaches equilibrium.…”
Section: Wwwintechopencommentioning
confidence: 99%
“…However, the equilibrium constant was considered in those works as equal to one, which presumes that the reaction of equimolar amounts of thereactants leads to equal concentrations of molar fractions of the species when the transesterification reaction reaches equilibrium. Based on the results above mentioned, the mechanism and kinetics of the transesterification reaction in poly(ethylene terephthalate) and poly(ethylene 2,6-naphthalene dicarboxylate) polymer blends was simulated using model compounds of ethylenedibenzoate (BEB) and ethylene dinaphthoate (NEN) [Alexandrova et al 2000]. An additional investigation dealt with the actual melt extrusion of the blend below the critical reaction temperature in the extruder [Medina et al 2004] Prior to melt compounding in the extruder, the PET and PEN polymers were previously dried in a Cole-Palmer vacuum oven at 120 °C with-45mm Hg pressure during 10 h. Extrusion was carried out in a Haake-Rheocord 90 TW-100 twin-screw conical counter-rotating extruder of 331 mm length, with temperature profile of 230, 240 and 250 °C and screw speed of 30RPM.…”
Section: Wwwintechopencommentioning
confidence: 99%
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“…In this state, there is a simple relation between the forward and backward rate constants which simplifies the situation. [13] However, assuming an equilibrium state under the melt mixing processing conditions is far from reality. Therefore, in this work, an attempt has been made to solve the above equation from the first stage of mixing till it reaches to the equilibrium state.…”
Section: Mathematical Approach For Calculation Of the X And Rdmentioning
confidence: 99%
“…By controlling the extent of the interchange reactions, tailored block and random copolyesters can be formed with desirable properties. Several examples of transesterification reactions in polyester blends have been reported in literature [1][2][3][4][5][6][7][8][9][10][11][12][13][14][15][16][17].…”
Section: Introductionmentioning
confidence: 99%