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Commodity and engineering plastics

Polymer / Plastics / Rubber Technology (B.Tech) · Polymer materials · free study notes for exams, placements and interviews

In short

Commodity plastics are the five high-volume, low-cost thermoplastics — polyethylene, polypropylene, PVC, polystyrene and PET — that make up roughly three-quarters of world polymer consumption and go into packaging, pipes, film and housewares. Engineering plastics (nylon, polycarbonate, POM, PBT, ABS, modified PPO, and the high-performance PEEK/PPS/PEI family) cost several times more but carry load, hold dimensions and work above 100 °C, so they replace metal in gears, housings, headlamps and under-bonnet parts. The dividing line is not chemical but a property-and-price line: strength above about 40–50 MPa, modulus above about 2 GPa and continuous service above 100 °C. This topic is examined in Polymer Materials and Polymer Technology papers and in GATE-equivalent polymer science questions on structure–property relations, and it is the core screening topic for interviews at Reliance Industries, GAIL, IOCL, OPaL, Supreme Industries, Nilkamal, Finolex, Astral, Prince Pipes, SABIC, Covestro, Lanxess and the auto-component tiers supplying Maruti, Tata Motors, Mahindra, Bajaj and TVS.

Explained

How plastics are classified

The five commodity plastics

The engineering plastics

Structure–property relations that explain every selection

Processing routes and what each polymer demands

  1. Injection moulding — PP, PS, ABS, PA, PC, POM, PBT. Steps: drying → plasticising → injection → packing/holding → cooling → ejection. Key settings: melt temperature, injection speed, holding pressure (governs shrinkage and sinks), mould temperature (governs crystallinity, gloss, warpage), back pressure.
  2. Extrusion — pipe, profile, sheet, film, wire covering: HDPE, PVC, PP, PS. Screw zones: feed → compression → metering; L/D usually 20–30:1; die swell and draw-down set final dimensions.
  3. Blown and cast film — LDPE/LLDPE/HDPE blown film with blow-up ratio 2–4; BOPP and BOPET are cast then biaxially oriented, which raises strength, clarity and barrier.
  4. Blow moulding — extrusion blow for HDPE/PP containers; injection stretch-blow (ISBM) for PET bottles, where stretching above Tg gives strain-induced crystallinity and CO₂ retention.
  5. Thermoforming — HIPS, PVC, PET sheet for trays, cups, refrigerator liners.
  6. Rotational moulding — PE powder for water tanks (the ubiquitous Indian overhead tank), large, stress-free, hollow parts.
  7. Drying is not optional for PET (<50 ppm), PA (<0.2%), PC and PBT (<0.02%) — the condensation polymers hydrolyse in the melt and lose molecular weight irreversibly.
  8. Rheology note: thermoplastic melts are pseudoplastic (shear-thinning), so viscosity falls as injection speed rises — this is why thin walls can be filled at all.

Testing, standards and Indian practice

Key points

Formulas and examples

Degree of polymerisation: DP = Mn / M0 — M0 = repeat-unit molar mass (g/mol)
Mn = Σ NiMi / Σ Ni ; Mw = Σ NiMi² / Σ NiMi ; PDI = Mw / Mn (≥ 1; 1 = monodisperse)
Carothers (step-growth): DP = 1/(1 − p), p = fractional conversion of functional groups
Mark–Houwink: [η] = K·Ma — [η] in dl/g; K, a are polymer–solvent–temperature constants
Crystallinity: Xw(wt) = ρc(ρ − ρa) / [ρ(ρc − ρa)] ; Xv(vol) = (ρ − ρa)/(ρc − ρa) — ρa, ρc = fully amorphous and fully crystalline densities (g/cm³)
Fox equation (random copolymer/miscible blend): 1/Tg = w1/Tg1 + w2/Tg2 — Tg in kelvin, w = mass fractions
Flory–Fox: Tg = Tg∞ − K/Mn — Tg rises with chain length and plateaus
Mould shrinkage: S = (L_cavity − L_part)/L_cavity ; so L_cavity = L_part/(1 − S)
Part mass m = V × ρ_solid ; shot mass = n·m + runner mass
Clamp force F = p_cavity × A_projected — p in MPa (N/mm²), A in mm², F in N; 1 tonne-force = 9.81 kN
Cooling time (plate): t = (s²/π²α)·ln[(4/π)(T_melt − T_mould)/(T_eject − T_mould)] — s = half wall thickness (m), α = thermal diffusivity (m²/s), α ≈ 0.9 × 10⁻⁷ for PP
Pipe pressure rating: p = 2σ_s/(SDR − 1), SDR = D/e, σ_s = MRS/C (C = design coefficient, 1.25 for water)

Example 1 — Molecular weight averages and DP (PP). A sample contains 2 mol of chains of 10,000 g/mol, 5 mol of 30,000 and 3 mol of 60,000.

Example 2 — Crystallinity of an HDPE pipe grade. Measured ρ = 0.956 g/cm³; for PE ρa = 0.855, ρc = 1.000.

Example 3 — Tg of a vinyl chloride–vinyl acetate copolymer (Fox). 85% VC (Tg 354 K) + 15% VAc (Tg 305 K).

Example 4 — Mould cavity size, shot weight, clamp force and cooling time (PP crate handle, 4 cavities). Part length 150.00 mm, shrinkage 1.8%, part volume 96 cm³, wall 2.5 mm, projected area 95 cm² per part plus 20 cm² runner. Melt 230 °C, mould 30 °C, ejection 90 °C, cavity pressure 30 MPa.

Example 5 — Pressure rating of a PE100 pipe (IS 4984 practice). PE100 has MRS = 10 MPa; design coefficient C = 1.25 for water → σ_s = 8 MPa. For SDR 11 (e.g. 110 mm OD, 10 mm wall): p = 2 × 8/(11 − 1) = 1.6 MPa = 16 bar (PN 16). The same pipe in PE80 (MRS 8, σ_s = 6.4 MPa) gives p = 12.8 bar — which is why PE100 lets a utility use a thinner wall for the same 16 bar duty.

PropertyHDPEPPuPVCPS (GPPS)ABSPA6PCPOM
Density, g/cm³0.950.9051.401.051.051.131.201.41
Tg / Tm, °C−120/132−5/16382/—100/—105/—50/220148/—−60/172
Tensile strength, MPa22–3130–4045–5535–5040–5070–85 (dry)60–7065–70
Notched Izod, J/m100–20025–6050–10015–25200–40050–60 (dry)600–90070–120
HDT at 1.8 MPa, °C~45~55~70~80~95~65 (dry)~130~100
Water absorption, %<0.01<0.020.10.050.31.6–30.20.2
Shrinkage, %1.5–31.2–20.3–0.60.4–0.60.4–0.70.8–1.50.5–0.71.8–2.5
Typical usePipe, jerry cansCrates, bumpersPipe, profilesDisposablesAppliance bodyGears, tiesLenses, visorsGears, cams

Where it is used

Interview questions

Common mistakes

Related topics

Polymer additives and compounding · Polymers and composites · Rubber technology: elastomers, compounding and vulcanisation · Biodegradable polymers and plastics recycling · Polymerisation processes and reaction engineering · Polymer rheology and processing (injection, extrusion, blow moulding)

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