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23-Chem-B8 Polymer Engineering · May 2017

Question 2 of 6: Living Anionic Polymerization — Chain Lengths and Poisson Kinetics

Nivaar worked solution (AI-drafted; not reviewed by a licensed engineer)

Notes on this paper

Paper format: Open-book, 3 hours; six numbered problems of equal value (20 points each), of which five constitute a complete paper (only the first five in the answer book are marked). All six problems are solved below so the set is complete for study.

Reference texts: Odian, Principles of Polymerization (4th ed., Wiley) — chain-growth & living/anionic kinetics, molecular-weight distributions; Rudin & Choi, The Elements of Polymer Science and Engineering (3rd ed., Academic Press) — dilute-solution rheology, MWD averages, capillary viscometry; Tadmor & Gogos, Principles of Polymer Processing (2nd ed., Wiley) — calendering, injection filling, die flow; Sperling, Introduction to Physical Polymer Science (4th ed., Wiley) — viscoelasticity; Young & Lovell, Introduction to Polymers (3rd ed.) — polyolefin processing; Middleman, Fundamentals of Polymer Processing — power-law tube/runner flow.

Question 2: Living Anionic Polymerization — Chain Lengths and Poisson Kinetics (20 points: 12.5 + 12.5)

Question text not reproduced: the examination questions are © Engineers and Geoscientists BC. Open the official past paper (linked at the top of this page) to read the question, then follow the worked solution below.

Given.

QuantitySymbolValue
Initial monomer concentration[M]02 mol/dm3
Initiator concentration[I]00.01 mol/dm3
Initiation rate coefficientki∞ (instantaneous)
Propagation rate coefficientkp100 dm3·mol-1s-1

Find. (a) X̄n, X̄w, M̄n, M̄w, conversion and PDI at complete reaction; (b) the concentration of living j-mers [Pj](t) for j = 3, 7, 10.

Approach. With ki = ∞ every initiator becomes a living chain at t = 0, so the number of chains is fixed and X̄n is just the monomer-to-initiator ratio; the absence of termination makes the length distribution Poisson, which fixes X̄w/X̄n; the time evolution follows from a constant active-centre concentration driving first-order monomer decay.

Check

The monomer is not named, so molecular weights are given as X̄·M0; a representative value uses styrene, M0 = 104.15 g/mol (the archetypal anionic monomer). Chain-transfer and termination are absent (ideal living system).

Part (a) — final averages.

  1. Number-average chain length. Instantaneous initiation means all [I]0 chains start together and none are created or destroyed thereafter, so at complete conversion every monomer is shared equally among the chains:$$\bar X_n=\frac{[M]_0}{[I]_0}=\frac{2}{0.01}=\boxed{200}$$
  2. Poisson breadth. A living chain adds monomers one at a time with no termination, so the number of added units is Poisson-distributed with mean λ = X̄n−1 = 199. The weight average and PDI are$$\bar X_w=\frac{\lambda^2+3\lambda+1}{\lambda+1}=201.0,\qquad \text{PDI}=\frac{\bar X_w}{\bar X_n}=1+\frac{\lambda}{(\lambda+1)^2}=\boxed{1.005}$$the hallmark near-monodispersity of living polymerization.
  3. Molecular weights. With styrene as the reference monomer,$$\bar M_n=\bar X_n M_0=200(104.15)=2.08\times10^{4}\ \text{g/mol},\quad \bar M_w=\bar X_w M_0=2.09\times10^{4}\ \text{g/mol}$$
  4. Extent of polymerization. Living chains consume monomer until it is exhausted, so the final fractional conversion is $p=1-[M]_\infty/[M]_0\to\boxed{1.0\ (100\%)}$ — the X̄n above is the complete-conversion limit.

Part (b) — time evolution of the living j-mers.

  1. Monomer decay. The total active-centre concentration is constant, [P*] = [I]0, so monomer disappears by first-order kinetics:$$-\frac{d[M]}{dt}=k_p[I]_0[M]\ \Rightarrow\ [M]=[M]_0e^{-k_p[I]_0t},\qquad k_p[I]_0=100(0.01)=1\ \text{s}^{-1}$$so [M] = 2e−t mol/dm3.
  2. Poisson kinetics of the distribution. The population balance for the living j-mer, $d[P_j]/dt=k_p[M]([P_{j-1}]-[P_j])$, is solved by a Poisson form in the “monomer clock” $\nu(t)=\int_0^t k_p[M]\,dt'=\dfrac{[M]_0}{[I]_0}\left(1-e^{-k_p[I]_0t}\right)$:$$[P_j](t)=[I]_0\,e^{-\nu}\,\frac{\nu^{\,j-1}}{(j-1)!}$$Because there is no termination, this active-centre concentration is the concentration of j-mer polymer at that instant.
  3. Peaks for j = 3, 7, 10. Each curve is a travelling wave that peaks when ν = j−1:$$[P_j]_{max}=[I]_0\,e^{-(j-1)}\frac{(j-1)^{\,j-1}}{(j-1)!}$$giving 2.71×10-3, 1.61×10-3 and 1.32×10-3 mol/dm3 at t = 0.0101, 0.0305 and 0.0460 s respectively. Longer chains appear later and their peak is broader and lower, because the population disperses as ν grows.
Living-chain distribution [Pⱼ](t) for j = 3, 7, 10 (Poisson wave)time t (s)active j-mer conc. [Pⱼ] (mol/dm³)0.0e+007.4e-041.5e-032.2e-033.0e-030.0000.0150.0310.0460.0620.077j=3j=7j=10
Fig. 2 — concentration of living j-mers vs time. Each j rises then falls as chains grow past that length; the peak height drops and shifts later with increasing j.
QuantityValue
Number-average chain length, X̄n200
Weight-average chain length, X̄w201
M̄n (styrene basis)2.08×104 g/mol
M̄w (styrene basis)2.09×104 g/mol
Polydispersity, PDI1.005
Extent of polymerization, p1.0 (100%)
[P3]max2.71×10-3 M at t = 0.0101 s
[P7]max1.61×10-3 M at t = 0.0305 s
[P10]max1.32×10-3 M at t = 0.0460 s