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FREE-RADICAL POLYMERIZATION
At the end of this lecture, you should be able to:
- Understand the kinetic of free-radical polymerization.
- Learn what is meant by kinetic-chain length.
- Understand the calculation of kinetic-chain length.
- Understand the chain-transfer reactions
- Solving problems including chain-transfer reactions
APRIL 2020
Mustansiriyah University/ Materials Eng. Dept.
Dr Ahmed A. AYASH
1
Kinetics of Free Radical Polymerization
1. Initiation
I 2 R. Radical Generation
kd
R. + M M1
. Initiation
ki
Assuming that ki >>kd and accounting for the fact that two Radicals are formed
during every initiator decomposition,
The rate of initiation, Ri is given by:
Ri = d[Mi] = 2f kd [I]
dt
f = efficiency of the initiator and is usually 0.3< f >0.8.
2
2. Propagation
M1
. + M M2
.
M2
. + M M3
.
M3
. + M M4
.
.
.
.
Mx
. + M Mx+1
.
Rp = - d[M] = kp[M .][M]
dt
kp
kp
kp
kp
3
3. Termination
Mx
. + . My Mx-My (Combination)
Mx
. + . My Mx + My (Disproportionation)
kt
ktd
Since two radicals are consumed in every termination, then:
Rt = 2kt [M .]2
4. Steady-state Assumption
Very early in the polymerization, the concentration of radicals becomes constant
because Ri = Rt
 2fkd[I] = 2kt [M .]2
4
2fkd [I] = 2kt [M .]2
Solve this equation for [M .]:
[M .] = (fkd [I]/kt)1/2
Substituting the above equation into the propagation expression:
Rp = kp[M .][M] = kp [M](fkd [I]/kt)1/2
Since the rate of propagation, Rp, is essentially the rate of polymerization, the rate of
polymerization is proportional to [I]1/2 and [M].
5
5. KINETIC CHAIN LENGTH
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.,:
At Steady – State:
We know that :
1
2
4
[M·] [M] 3
6
It follows on substitution for Rp and Rt in equation (2):
Substituting for [M·] from Equation(3) yields:
Equations (5) and (6) are 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,
5
6
[M·] [M]
7
Thus,
Now, the number-average degree of polymerization can be calculated as follows::
So,
Xn (or DPn) = 2Rp / Rt = 2 Rp/Ri for termination by combination
Xn = Rp / Rt = Rp/Ri for termination by disproportionation
Xn = 2 ν for termination by combination
Xn = ν for termination by disproportionation
NOTE: Xn is sometimes represented by Dp as we did in the previous lectures. 8
Example: For pure styrene polymerized at 60°C, the value of the ratio kp2/kt is 0.0012 l/mol.s.
The corresponding value for pure vinyl acetate polymerized at 60°C is 0.125 l/mol.s.
a. Estimate their relative kinetic 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:
Assume the rates of polymerization and monomer concentrations are the same for styrene(s),
and vinyl acetate (VA).
a)
b)
9
HOMEWORK (2)
10
Re-derive the rate of propagation for a free radical polymerization at steady-state condition
as function of the initiator and monomer concentration
Hint: you must get, Rp = kp [M](fkd [I]/kt)1/2
THANK YOU FOR LISTENING
11

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5_2020_04_07!11_06_37_PM.pptx

  • 1. FREE-RADICAL POLYMERIZATION At the end of this lecture, you should be able to: - Understand the kinetic of free-radical polymerization. - Learn what is meant by kinetic-chain length. - Understand the calculation of kinetic-chain length. - Understand the chain-transfer reactions - Solving problems including chain-transfer reactions APRIL 2020 Mustansiriyah University/ Materials Eng. Dept. Dr Ahmed A. AYASH 1
  • 2. Kinetics of Free Radical Polymerization 1. Initiation I 2 R. Radical Generation kd R. + M M1 . Initiation ki Assuming that ki >>kd and accounting for the fact that two Radicals are formed during every initiator decomposition, The rate of initiation, Ri is given by: Ri = d[Mi] = 2f kd [I] dt f = efficiency of the initiator and is usually 0.3< f >0.8. 2
  • 3. 2. Propagation M1 . + M M2 . M2 . + M M3 . M3 . + M M4 . . . . Mx . + M Mx+1 . Rp = - d[M] = kp[M .][M] dt kp kp kp kp 3
  • 4. 3. Termination Mx . + . My Mx-My (Combination) Mx . + . My Mx + My (Disproportionation) kt ktd Since two radicals are consumed in every termination, then: Rt = 2kt [M .]2 4. Steady-state Assumption Very early in the polymerization, the concentration of radicals becomes constant because Ri = Rt  2fkd[I] = 2kt [M .]2 4
  • 5. 2fkd [I] = 2kt [M .]2 Solve this equation for [M .]: [M .] = (fkd [I]/kt)1/2 Substituting the above equation into the propagation expression: Rp = kp[M .][M] = kp [M](fkd [I]/kt)1/2 Since the rate of propagation, Rp, is essentially the rate of polymerization, the rate of polymerization is proportional to [I]1/2 and [M]. 5
  • 6. 5. KINETIC CHAIN LENGTH 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.,: At Steady – State: We know that : 1 2 4 [M·] [M] 3 6
  • 7. It follows on substitution for Rp and Rt in equation (2): Substituting for [M·] from Equation(3) yields: Equations (5) and (6) are 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, 5 6 [M·] [M] 7
  • 8. Thus, Now, the number-average degree of polymerization can be calculated as follows:: So, Xn (or DPn) = 2Rp / Rt = 2 Rp/Ri for termination by combination Xn = Rp / Rt = Rp/Ri for termination by disproportionation Xn = 2 ν for termination by combination Xn = ν for termination by disproportionation NOTE: Xn is sometimes represented by Dp as we did in the previous lectures. 8
  • 9. Example: For pure styrene polymerized at 60°C, the value of the ratio kp2/kt is 0.0012 l/mol.s. The corresponding value for pure vinyl acetate polymerized at 60°C is 0.125 l/mol.s. a. Estimate their relative kinetic 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: Assume the rates of polymerization and monomer concentrations are the same for styrene(s), and vinyl acetate (VA). a) b) 9
  • 10. HOMEWORK (2) 10 Re-derive the rate of propagation for a free radical polymerization at steady-state condition as function of the initiator and monomer concentration Hint: you must get, Rp = kp [M](fkd [I]/kt)1/2
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