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Tyre technology and rubber product manufacture

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

In short

Tyre technology is the design, compounding, assembly and vulcanisation of a composite of rubber compounds, textile and steel cord into a pressure vessel that carries load, transmits traction and braking, absorbs road shock and steers a vehicle. The same compounding and curing science makes hoses, belts, seals, gloves, footwear, anti-vibration mounts and rubber linings. It is examined in polymer processing and rubber technology papers (compound recipes in phr, cure kinetics from rheometer curves, tyre construction, defects) and in GATE-level questions on vulcanisation and filler reinforcement. India is the world's largest natural rubber-consuming tyre market after China, and MRF, Apollo, JK Tyre, CEAT, BKT, TVS Srichakra, Bridgestone India and Yokohama India recruit heavily for mixing, building, curing, quality and R&D roles. Tyres carry mandatory BIS certification under the pneumatic tyres and tubes Quality Control Order, and performance (rolling resistance, wet grip, rolling sound) is governed through AIS-142 under the CMVR.

Explained

Rubbers and compounding ingredients

Vulcanisation: chemistry, systems and kinetics

Mixing, shaping and semi-finished components

  1. Mastication (NR only): shear in a mixer or mill breaks chains, drops Mooney viscosity to a processable level; peptisers assist.
  2. Internal mixer (tangential Banbury or intermeshing), 100-400 L chamber, fill factor 0.65-0.75, ram pressure 0.4-0.8 MPa, rotor 20-60 rpm. Non-productive/masterbatch stage: polymer, filler, oil, ZnO, stearic acid, antidegradants — dumped at 150-165 °C to complete filler dispersion and silica silanisation. Remill if needed. Productive/final stage: sulphur and accelerators at low speed, dumped below ~105 °C.
  3. Specific mixing energy (kWh/kg) and dump temperature are the control variables; dispersion checked by dispergrader, Mooney and rheometer on every batch.
  4. Dump mill / twin-screw sheeter → sheet or strip → batch-off with antitack dip and cooling festoon.
  5. Extrusion: hot-feed or cold-feed, vented extruders; quadruplex/triplex heads co-extrude tread cap, base, wing and sidewall in one profile; profiles, hose tubes, bead apex and innerliner by extrusion or calendering.
  6. Calendering: 3- or 4-roll, inverted-L or Z; topping/skim-coating textile or steel cord fabric on both sides, plus friction calendering; roll-bending and crown correct deflection.
  7. Bead: high-tensile brass-coated steel wire, rubber-coated, wound into a hexagonal/round bundle and wrapped; apex (bead filler) is a hard extruded triangle.
  8. Cutting/bias-cutting of plies to the required cord angle; steel belt plies cut at 18-25° to the circumference.

Tyre construction, building and curing

Other rubber products and their processes

Testing, standards and Indian regulation

Key points

Formulas and examples

Compound specific gravity: SG = Σ(phr)ᵢ / Σ(phrᵢ / SGᵢ) — phr in parts by mass, SGᵢ the ingredient specific gravity (dimensionless).
Mixer batch mass: m = V_chamber × f × SG — V in litres, f = fill factor (0.65-0.75), SG in kg/L → m in kg.
Ingredient weight: wᵢ = m × phrᵢ / Σphr (kg).
Compound cost: ₹/kg = Σ(phrᵢ × rateᵢ) / Σphrᵢ — rate in ₹/kg.
Cure rate index: CRI = 100 / (t90 − ts2) — t in minutes, CRI in min⁻¹.
Temperature scaling (rule of thumb): t₂ = t₁ × Q(T₁−T₂)/10, Q ≈ 2, T in °C.
Arrhenius form: ln(t₁/t₂) = (Ea/R)(1/T₁ − 1/T₂) — T in K, R = 8.314 J/mol·K, Ea in J/mol.
Heat-conduction scaling: cure time ∝ L²/α — L = half-thickness (m), α = thermal diffusivity (≈1.1 × 10⁻⁷ m²/s for rubber).
Tyre outer diameter: OD = rim dia + 2 × (section width × aspect ratio/100); 1 inch = 25.4 mm.
Revolutions per km: N = 1000 / (loaded rolling circumference in m); LRC ≈ 0.96-0.97 × π × OD.
Rolling resistance: F_r = C_rr × F_z; power P = F_r × v — F in N, F_z = vertical load (N), v in m/s, P in W.
Abrasion loss (volume): ΔV = Δm / ρ — mm³ per standard test run; abrasion resistance index = reference loss/sample loss.
Press capacity: tyres/day = 1440 × cavities / cycle time (min).

Example 1 — Recipe, specific gravity, batch weight and cost. Tread masterbatch: NR 100 (SG 0.93), N330 50 (1.80), ZnO 5 (5.60), stearic acid 2 (0.92), TDAE oil 5 (0.95), 6PPD 2 (1.00), sulphur 2.5 (2.07), CBS 1 (1.27). Σphr = 167.5. Volumes (cm³ per 167.5 g): 107.53 + 27.78 + 0.89 + 2.17 + 5.26 + 2.00 + 1.21 + 0.79 = 147.63. SG = 167.5/147.63 = 1.135. Batch in a 250 L mixer at f = 0.70: m = 250 × 0.70 × 1.135 = 198.6 kg. NR charge = 198.6 × 100/167.5 = 118.6 kg; N330 = 59.3 kg; sulphur = 198.6 × 2.5/167.5 = 2.96 kg. Cost at illustrative rates (₹/kg): NR 170, N330 95, ZnO 290, stearic 130, oil 75, 6PPD 450, S 45, CBS 520 → Σ(phr × rate) = 17,000 + 4,750 + 1,450 + 260 + 375 + 900 + 112.5 + 520 = ₹25,367.5 → ₹151.4 per kg of compound (rates fluctuate; use current purchase prices).

Example 2 — Cure kinetics. MDR at 150 °C gives ts2 = 3.5 min, t90 = 12.0 min. CRI = 100/(12.0 − 3.5) = 11.8 min⁻¹. Q₁₀ = 2 rule at 160 °C: t90 = 12.0 × 2−1 = 6.0 min. Arrhenius with Ea = 90 kJ/mol: (90,000/8.314)(1/423.15 − 1/433.15) = 10,825 × 5.456 × 10⁻⁵ = 0.591 → ratio e0.591 = 1.805 → t90 = 12.0/1.805 = 6.65 min. The Q₁₀ rule is about 10% optimistic here, so press time is set from the Arrhenius value plus a heat-up allowance.

Example 3 — Tyre geometry. 205/55 R16 91V: section height = 205 × 0.55 = 112.75 mm; rim = 16 × 25.4 = 406.4 mm. OD = 406.4 + 2 × 112.75 = 631.9 mm; free circumference = π × 0.6319 = 1.985 m. Loaded rolling circumference ≈ 0.97 × 1.985 = 1.926 m → N = 1000/1.926 = 519 rev/km. Load index 91 = 615 kg per tyre → four tyres carry 2,460 kg; speed symbol V = 240 km/h.

Example 4 — Rolling resistance and fuel. Car of 1,400 kg, load shared equally, at 100 km/h (27.78 m/s). F_z total = 1400 × 9.81 = 13,734 N. Tyre A, C_rr = 0.0095: F_r = 130.5 N → P = 130.5 × 27.78 = 3.63 kW. Tyre B, C_rr = 0.0120: F_r = 164.8 N → P = 4.58 kW. Extra work of B over 100 km = (164.8 − 130.5) × 10⁵ = 3.43 MJ at the wheels; at 30% tank-to-wheel efficiency that is 11.4 MJ of fuel; petrol ≈ 32.4 MJ/L → about 0.35 L per 100 km — the basis of rolling-resistance labelling under AIS-142.

Example 5 — Press and extruder capacity. PCR cure 11 min + 1 min load/unload = 12 min cycle, twin-cavity press: 1440 × 2/12 = 240 tyres/press/day; for 6,000 tyres/day, 6000/240 = 25 presses. Tread extrusion: cross-section 2,400 mm² = 24 cm², SG 1.15 → 24 × 100 × 1.15 = 2,760 g/m = 2.76 kg/m; tread length 1.99 m → 5.49 kg/tyre. A quadruplex line at 1,200 kg/h feeds 1200/5.49 = 218 treads/h ≈ 5,240/day — one line supports the 6,000/day plant only with an extra shift or a second line.

FeatureBias (diagonal)Radial
Carcass cord angle30-40° crossed plies~90° radial
BeltNone (or breaker)Steel belts at 18-25°
Rolling resistanceHigh20-30% lower
Tread life, heat build-upLower life, more heatLonger life, cooler
Ride and handlingStiff sidewall, poorer corneringFlexible sidewall, better grip
Retreadability, costCheaper to buildCostlier, better casing life
Typical Indian useSome farm, OTR, small two-wheeler sizesCars, TBR, most new fitment
Cure systemS : acceleratorCrosslink typeStrength
Conventional (CV)2.0-2.5 : 0.5Mainly polysulphidicBest flex fatigue, high tear
Semi-EV1.0-1.7 : 1.0-1.5MixedBalanced
Efficient (EV)0.3-0.5 : 2.5-5Mono/disulphidicBest heat ageing, low set
Peroxide—C-CNo reversion, poor fatigue

Where it is used

Interview questions

Common mistakes

Related topics

Polymer chemistry and elastomers · Mechanical behaviour of polymers and viscoelasticity · Extrusion and blow moulding · Mould and die design for plastics · Polymer testing and characterisation · Composites and fibre reinforcement

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