23-Chem-B8 Polymer Engineering · December 2014
Nivaar worked solution (AI-drafted; not reviewed by a licensed engineer)
National Exam 04-Chem-B8, Polymer Engineering — December 2014. Three hours, OPEN BOOK (any non-communicating calculator). The paper is in four parts: Part A (Q1–2, 20 marks each), Part B (Q3–4, 30 marks each), Part C (Q5–6, 30 marks each) and Part D (Q7, 20 marks). A candidate answers ONE question from each of A, B, C and the single question in D — four questions constitute a complete paper. For completeness this solution works all seven questions in full.
Reference texts: Rudin & Choi, The Elements of Polymer Science and Engineering, 3rd ed.; Sperling, Introduction to Physical Polymer Science, 4th ed.; Odian, Principles of Polymerization, 4th ed.; Young & Lovell, Introduction to Polymers, 3rd ed.; Painter & Coleman, Fundamentals of Polymer Science, 2nd ed.
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.
The polydispersity index is \(\text{PDI}=\overline{M}_w/\overline{M}_n\). The stated numbers give \(25{,}000/50{,}000=0.5\), which is physically impossible — by definition \(\overline{M}_w\ge\overline{M}_n\) always. The two values are evidently transposed; reading them as \(\overline{M}_n=25{,}000\), \(\overline{M}_w=50{,}000\) gives
\(\displaystyle \boxed{\text{PDI}=\overline{M}_w/\overline{M}_n=2.0.}\)
A polydispersity of 2.0 is the signature of the “most-probable” (Flory) distribution obtained in step-growth polymerization at high conversion, where \(\text{PDI}=1+p\to2\) as \(p\to1\). Chain-growth (free-radical) polymer gives PDI ≈ 1.5 for termination by combination or 2.0 for pure disproportionation, and living/ionic chains give PDI ≈ 1. A clean PDI of 2.0 is therefore most consistent with step-growth polymerization.
Given. Two calibration samples of known crystallinity and a two-phase (crystalline + amorphous) density model, in which density is linear in the degree of crystallinity.
(i) Glass-transition temperature — \(T_g\) increases with pressure. Applying hydrostatic pressure compresses the polymer and reduces its free volume. Since the glass transition occurs at an iso-free-volume state, a melt/rubber squeezed to smaller free volume must be heated more to regain the segmental mobility needed for the transition; thus \(T_g\) rises, typically \(dT_g/dP\approx+0.15\)–\(0.3\ \text{K/MPa}\) (consistent with the Ehrenfest relation \(dT_g/dP=TV\Delta\beta/\Delta C_p>0\)).
(ii) Melt viscosity — increases with pressure. By the same free-volume argument (WLF/Doolittle, \(\eta\propto\exp(B/f)\)), raising pressure lowers the fractional free volume \(f\) and raises the effective \(T_g\), pushing the melt closer to its glassy state; segmental friction and hence melt viscosity increase with pressure. This is a real processing concern — injection-moulding pressures can raise melt viscosity appreciably.
(Equivalent alternatives: uniaxial drawing/orientation, which greatly stiffens PE along the draw direction; or copolymer/nucleation strategies that raise crystallinity.)
| Part | Answer |
|---|---|
| (a) Mechanism | PDI = 2.0 → step-growth |
| (b) Crystallinity of C | ≈ 76.7 % (\(\rho_a=0.720,\ \rho_c=1.020\)) |
| (c-i) Pressure on \(T_g\) | increases (free-volume reduction) |
| (c-ii) Pressure on melt \(\eta\) | increases (free-volume reduction) |
| (d) Stiffen PE | ↑ crystallinity; add filler/fibre; cross-link (or draw/orient) |