In a DIY filament extruder (for example, a community-scale plastic recycling setup), a rotating screw must generate enough axial force to push molten polymer through the die/nozzle. That resisting load is usually described as an extrusion (melt) pressure. The motor and gearbox must supply torque to the screw to create that force.
This calculator provides a first-order torque estimate from three inputs:
The output is an estimated motor torque requirement in N·m (newton-meters). Use it for early motor/gearbox sizing and sanity checks—not as a substitute for detailed screw-extrusion design.
A). In many builds this is closest to the barrel internal diameter (or the diameter of the melt “piston” you are effectively pressurizing). If you enter the screw OD but the pressurized area is smaller (or larger), the torque estimate will be off.The model uses a pressure-to-force conversion and then converts force to torque using the screw radius as a lever arm, with an efficiency correction.
Step 1: Cross-sectional area
The pressurized area is modeled as a circle:
Step 2: Force from pressure
Pressure times area gives axial force:
F = P · A
Step 3: Torque at the screw
A simple torque estimate uses T = F · r. The calculator then divides by drivetrain efficiency (η) to estimate required motor torque:
T_motor = (F · r) / η
Unit conversions
d in mm → radius in meters: r = (d / 2) / 1000P(Pa) = P(MPa) × 1,000,000η = eff% / 100Important scaling note: because A ∝ r² and torque uses F·r, the estimate scales approximately with r³ (or diameter cubed). Small changes in diameter can change torque a lot.
The reported torque is best interpreted as a baseline running torque implied by the pressure you entered. In real extruders, the motor must usually be sized with margin for:
Practical sizing often uses a safety factor (for example, 1.5× to 3×) depending on how variable the feedstock and process are.
Suppose you have:
η = 0.8)1) Radius: r = (20/2)/1000 = 0.01 m
2) Area: A = π·r² = π·(0.01)² ≈ 3.1416×10⁻4 m²
3) Pressure in Pa: P = 5×10⁶ Pa
4) Force: F = P·A ≈ 5×10⁶ · 3.1416×10⁻4 ≈ 1570.8 N
5) Screw torque: T_screw = F·r ≈ 1570.8 · 0.01 ≈ 15.7 N·m
6) Motor torque with efficiency: T_motor = T_screw/0.8 ≈ 19.6 N·m
So, you’d look for a motor+gearbox combination that can deliver roughly 20 N·m continuous at your target screw RPM, then apply an additional margin for start-up and pressure spikes.
Extrusion pressure depends strongly on melt temperature, viscosity, die/nozzle geometry (length, taper, screen packs), and throughput. The ranges below are ballpark values people may see in small-scale filament extrusion, not guarantees.
| Material (common filament polymers) | Rough pressure range (MPa) | Notes |
|---|---|---|
| HDPE / LDPE | 2–5 | Often flows easily when hot; pressure rises quickly if die is restrictive. |
| PLA | 3–7 | Sensitive to temperature and degradation; keep melt control stable. |
| PETG / PET | 4–9 | Can be more viscous; drying and consistent feedstock help. |
| ABS | 4–10+ | Wide variability by grade; die and screen packs can push pressures higher. |
If you can measure force (for example, with a load cell on a plunger test) you can estimate pressure using P = F/A and then feed that pressure into this calculator.
Note: The pressure ranges table is illustrative and should be validated against your specific die geometry, melt temperature, and throughput.