A.
INITIATION
   This is a two-step process involving:
   (1) The decomposition of the initiator into primary radicalsb
   (2) The addition of a monomer to the primary free radical
   The constants kd and ka are the rate constants for initiator dissociation and monomer
   addition, respectively
   Where [I] represents the initiator concentration.
B. PROPAGATION
    The successive addition of monomers during propagation may be represented as follows
   This means that all the propagation steps have the same rate constants kp. In addition,
   propagation is a fast process.
   Where [M*] =ΣRMx• i.e., the sum of the concentrations of all chain radicals of type RM
C. TERMINATION
   Chain growth may be terminated at any point during polymerization by either or both of
   two mechanism.
    Combination (coupling)                                     Disproportionation
   If there is no need to distinguish between the two types of termination, which in any case
   are kinetically equivalent, then termination may be represented as:
       Where kt (ktc+ ktd), ktc, and ktd are the rate constants for overall termination process,
       termination by coupling, and termination by disproportionation, respectively. The
       termination rate is given by:
       The factor of 2 arises from the fact that at each incidence of termination reaction, two
       radicals disappear. Over the course of polymerization (at steady state), the total radical
       concentration remains constant.
       This means that radicals are being produced and destroyed at equal rates (i.e., Ri= Rt)
       Since the overall polymerization rate is essentially the rate of monomer consumption
       during propagation.
Example
The data for the bulk polymerization of styrene at 60°C with benzoyl peroxide as initiator are
       [M] = 8.35 × 103 mol/m3
       [I] = 4.0 mol/m3
       kp2/kd = 1.2 × 10–6 m3/mol-s
       If the initial rate of polymerization of styrene is 0.026 mol/m 3-s and the spontaneous
       decomposition of benzoyl peroxide in styrene is 2.8×10–6 s–1, what is the efficiency of the
       initiator?
       Solution
              The kinetic chain length, ν, is defined as the average number of monomers
               consumed by each primary radical. Obviously from this definition, the magnitude
               of the kinetic chain length will depend on the rate of the propagation relative to the
               termination rate, i.e.,
                                                        Equation 1
   At the steady state the kinetic chain length as
   Since at steady state the rate of initiation equals the rate of termination, Equation above can also
    be written as
    Substituting for [M·]
    Equations quite general and do not depend on the nature of initiation. Notice the
    inverse relation between the kinetic chain length and the radical concentration. For
    reactions initiated by the decomposition of an initiator, thus
    Recall that the rate of consumption of monomers by an active center (disappearance
    of monomers) is, by definition, the rate of propagation, Rp. Now, in termination by
    combination, two growing chains undergo mutual annihilation to produce a single
    inactive polymer molecule, whereas for termination by disproportionation, a
    biomolecular annihilation of active polymer chains results in two polymers.
    But kinetic chain length is given by Equation 2
    Example: - For pure styrene polymerized at 60°C, the value of the ratio k p2/kt is
    0.0012 1/mol-s. The corresponding value for pure vinyl acetate polymerized at
    60°C is 0.125 l/mol-s.
       a. Estimate their relative kinetic length chain lengths.
       b. Calculate the kinetic chain length for polystyrene if the rate of
       polymerization is 10–4 mol/l-s and monomer concentration is 8.35 mol/l.
Solution