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Kinetic Model of Radical Polymerization

If the transfer reaction to the initiator and monomer is neglected, the overall mechanism of polymerization can be expressed as follows  [Pg.197]

The mole balance equations for batch reactors are written for the species I2,1, Pi, [Pg.198]

Assuming that the quasi-steady-state approximation (QSSA) is valid, the concentration of the intermediate species I can be found from Eq. (5.3.3)  [Pg.198]

In radical polymerization, the slowest reaction is the dissociation of initiator molecules. As soon as a primary radical is produced, it is consumed by the reactions of Eq. (5.3.1). Thus, the concentration off is expected to be much less than that of P that is. [Pg.199]


To verify the kinetic model of radical polymerization presented in the last section, the following assumptions must be confirmed ... [Pg.201]


See other pages where Kinetic Model of Radical Polymerization is mentioned: [Pg.197]   


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