Introduction & Context

Belt extractors (or belt feeders) are widely used in process plants to withdraw bulk solids from hoppers, bins, or silos at a controlled rate. The capacity calculation converts a required mass flow (t day^–1) into the corresponding linear belt speed (m min^–1) that must be maintained to achieve that throughput. Correct sizing prevents both starvation (under-feed) and flooding (over-feed) of downstream equipment such as mills, kilns, or reactors.

Methodology & Formulas

Convert the daily target to an hourly basis: \[ \dot{m}_{\text{target}} = \frac{\text{target}_{\text{t day}^{-1}}}{24} \quad [\text{t h}^{-1}] \]
Express bulk density in t m^–3: \[ \rho_{\text{t m}^{-3}} = \rho_{\text{kg m}^{-3}} \cdot 0.001 \]
Compute the volumetric flow rate required on the belt: \[ Q = \frac{\dot{m}_{\text{target}}}{\rho_{\text{t m}^{-3}}} \quad [\text{m}^{3}\text{ h}^{-1}] \]
Relate volumetric flow to belt geometry and speed. For a rectangular cross-section of width \(W\) and bed depth \(H\): \[ Q = W \cdot H \cdot v_{\text{m h}^{-1}} \] Solving for belt speed: \[ v_{\text{m h}^{-1}} = \frac{Q}{W \cdot H} \]
Convert to the more common unit of m min^–1: \[ v_{\text{m min}^{-1}} = \frac{v_{\text{m h}^{-1}}}{60} \]

Parameter	Acceptable Range	Remarks
Belt speed, \(v_{\text{m min}^{-1}}\)	1 – 5 m min^–1	Below 1 m min^–1 pulley slip risk; above 5 m min^–1 spillage & skirt wear rise
Bed depth, \(H\)	0.25 – 0.50 m	Shallower beds give poor live storage; deeper beds raise load on belt & idlers
Bulk density, \(\rho_{\text{kg m}^{-3}}\)	550 – 650 kg m^–3	Typical for grains, meals, light powders; outside range recalibrate for material

Use the rule-of-thumb volumetric loading: 0.3–0.5 m³ of solids per m² of effective belt area per hour. Multiply this by the active extraction area (length × effective belt width) to obtain a first-pass capacity. Later refine with bed porosity, solvent ratio, and drainage rate.

Particle size distribution: Finer particles reduce permeability → lower drainage velocity → derate capacity by 10–30 %.
Bulk density: Convert volumetric to mass capacity; use loose, not tapped, density.
Porosity & bed height: Higher porosity increases drainage but lowers residence time; adjust bed thickness to keep 30–60 s contact.
Oil/solvent viscosity: Double viscosity ≈ 15 % lower drainage; apply Darcy-based correction factor.

Measure (or assume) solvent-to-solids ratio from lab Soxhlet data (e.g., 1.2 L kg⁻¹).
Multiply volumetric capacity (m³ h⁻¹) by loose bulk density (kg m⁻³) to get dry solids throughput.
Multiply solids throughput by solvent ratio to obtain total liquor flow; add 5–10 % safety for uneven distribution.
Report this liquor rate as the design basis for the evaporator or desolventiser.

Maximum belt speed: Usually 0.02–0.08 m s⁻¹; faster speeds cut residence time below extraction kinetics.
Drive motor power: Ensure torque can pull loaded belt plus 20 % overload for start-ups.
Wash zone pumps: Check available head; high bed resistance can starve sprays.
Track & seal wear: Uneven loading reduces effective area—derate capacity 5 % per 1 mm of belt wander.

Worked Example – Sizing a Belt Extractor for Dried Beet Pulp

A beet-sugar plant needs to convey 2 000 t d^–1 of dried pulp from the dryers to the pelletising line. The process engineer must check whether an existing belt extractor (2 m wide, 0.4 m deep) can handle this duty when running 24 h d^–1.

Design throughput: 2 000 t d^–1
Bulk density of dried pulp: 600 kg m^–3 (0.6 t m^–3)
Belt width: 2 m
Effective load height: 0.4 m
Operating time: 24 h d^–1

Convert daily rate to hourly rate: \[ Q_{\text{h}} = \frac{2\,000\ \text{t d}^{-1}}{24\ \text{h d}^{-1}} = 83.333\ \text{t h}^{-1} \]
Calculate the cross-sectional area of the load: \[ A = W \cdot H = 2\ \text{m} \cdot 0.4\ \text{m} = 0.8\ \text{m}^{2} \]
Relate mass flow to belt velocity: \[ Q_{\text{h}} = A \cdot v \cdot \rho \quad \Rightarrow \quad v = \frac{Q_{\text{h}}}{A \cdot \rho} \] \[ v = \frac{83.333\ \text{t h}^{-1}}{0.8\ \text{m}^{2} \cdot 0.6\ \text{t m}^{-3}} = 173.611\ \text{m h}^{-1} \]
Convert velocity to m min^–1 for operator readability: \[ v = \frac{173.611}{60} = 2.894\ \text{m min}^{-1} \]

Final Answer: The belt extractor must run at 2.89 m min^–1 to achieve the required 2 000 t d^–1 of dried pulp.

"Un projet n'est jamais trop grand s'il est bien conçu." — André Citroën

"La difficulté attire l'homme de caractère, car c'est en l'étreignant qu'il se réalise." — Charles de Gaulle

Belt Extractor Capacity Calculation

Introduction & Context

🚀 Skip the Manual Math!

Methodology & Formulas

Worked Example – Sizing a Belt Extractor for Dried Beet Pulp