This paper deals with the kinetic study of bulk free radical polymerization of styrene initiated with the commercial bifunctional initiator 2,5-dimethyl-2,5-bis(2-ethyl hexanoyl peroxy)hexane (Lupersol 256). The polymerization kinetics is investigated by DSC measurement for temperatures between 80 and 110°C and for initiator initial concentration from 0.115 up to 0.46 mol%. The experimental conversion and reaction rate are compared and discussed with the calculated values. For modeling the polymerization rate, a reaction scheme similar to the one given by Yoon and Choi (Polymer 1992;33(21):4582–4591) has been used and adapted. A detailed diffusional and semi-empirical model proposed by Chiu et al. (Macromolecules 1983;16(3):348–357) has bee...
In this work the problem of determining the dependencies on conversion of the initiation rate (R1), ...
In free radical polymerization diffusion-controlled processes take place simultaneously to the norma...
In this work the problem of determining the dependencies on conversion of the initiation rate (R1), ...
A detailed kinetic model of the bulk styrene polymerization initiated by diperoxide bifunctional ini...
Polymerization of styrene in presence of two monofunctional initiators is studied kinetically in an ...
A detailed, comprehensive mathematical model for bulk polymerization of styrene using multifunctiona...
A comprehensive kinetic model for the thermal polymerization of styrene at temperature values betwee...
A comprehensive kinetic model for the thermal polymerization of styrene at temperature values betwee...
A comprehensive kinetic model for the thermal polymerization of styrene at temperature values betwee...
A comprehensive kinetic model for the thermal polymerization of styrene at temperature values betwee...
In this study, we experimentally and theoretically investigated the use of the symmetrical cyclic tr...
Mathematical Modeling of Styrene/Divinylbenzene Copolymerization Comprising Diffusional Effects and ...
Styrene was polymerized using different amounts of azoisobutyronitrile as initiator at temperatures ...
This work experimentally and theoretically investigates the use of the symmetrical cyclic trifunctio...
An investigation was carried out to discover the effects of high conversion on the kinetic rate coef...
In this work the problem of determining the dependencies on conversion of the initiation rate (R1), ...
In free radical polymerization diffusion-controlled processes take place simultaneously to the norma...
In this work the problem of determining the dependencies on conversion of the initiation rate (R1), ...
A detailed kinetic model of the bulk styrene polymerization initiated by diperoxide bifunctional ini...
Polymerization of styrene in presence of two monofunctional initiators is studied kinetically in an ...
A detailed, comprehensive mathematical model for bulk polymerization of styrene using multifunctiona...
A comprehensive kinetic model for the thermal polymerization of styrene at temperature values betwee...
A comprehensive kinetic model for the thermal polymerization of styrene at temperature values betwee...
A comprehensive kinetic model for the thermal polymerization of styrene at temperature values betwee...
A comprehensive kinetic model for the thermal polymerization of styrene at temperature values betwee...
In this study, we experimentally and theoretically investigated the use of the symmetrical cyclic tr...
Mathematical Modeling of Styrene/Divinylbenzene Copolymerization Comprising Diffusional Effects and ...
Styrene was polymerized using different amounts of azoisobutyronitrile as initiator at temperatures ...
This work experimentally and theoretically investigates the use of the symmetrical cyclic trifunctio...
An investigation was carried out to discover the effects of high conversion on the kinetic rate coef...
In this work the problem of determining the dependencies on conversion of the initiation rate (R1), ...
In free radical polymerization diffusion-controlled processes take place simultaneously to the norma...
In this work the problem of determining the dependencies on conversion of the initiation rate (R1), ...