Animated industrial dedusting system mapDust travels from an enclosed source through capture ducting, a cyclone, a fabric filter and a fan before clean exhaust leaves the stack. Collected dust exits below the separators.SOURCE + HOODPRE-SEPARATORFABRIC FILTERFANSAFE EXHAUST0102030405
Swipe the diagram to explore
ANIMATED SYSTEM MAP
A dedusting system is a connected pressure and material-flow chain

Capture, duct transport, pre-separation, filtration, fan duty, discharge, and safe exhaust must work together. A strong collector cannot correct a poor source hood.

Industrial dedusting removes airborne particulate from a process or workplace by capturing it near the release point, transporting it through ducts, separating it from the gas, and discharging the collected material safely. The design question is therefore not “Which filter size do I need?” but “What complete system will control every relevant source across the real operating envelope?”

Start with the hazard assessment

Before calculating airflow, identify the dust, exposure limits, combustibility, toxicity, temperature, moisture, and process upset conditions. Combustible or hazardous dust can change the permissible collector location, recirculation strategy, equipment construction, monitoring, isolation, and explosion-protection concept.

1. Define the design duty

Build a source schedule before drawing the duct network. For every pickup point, record the process, material, release mechanism, normal and peak production rate, temperature, moisture, dust loading, particle-size distribution, operating hours, and whether sources run simultaneously.

Input groupQuestions to resolveWhy it controls design
DustPSD, true density, bulk density, abrasiveness, cohesiveness, combustibility, toxicity?Controls capture behavior, separator choice, wear, cleaning, safety, and disposal.
GasActual flow, temperature, pressure, humidity, corrosive or condensable components?Controls density, volume, pressure loss, materials, condensation risk, and fan duty.
ProcessContinuous or batch, enclosure leakage, startup, cleaning, upset and future capacity?Defines the operating envelope and simultaneity.
PerformanceWorkplace target, permitted outlet concentration, recovery objective, availability?Defines acceptance criteria and necessary measurement.

Use actual volumetric flow at each location. Gas volume changes with temperature, pressure, humidity, leakage, and air added at hoods. A normal-volume figure cannot be used directly to size ducts or the fan.

2. Capture the dust before it disperses

Local exhaust is usually most efficient when the source is enclosed as far as the process permits. A close-fitting enclosure needs less induced air than an open hood attempting to pull a contaminant cloud across a large distance.

  • Place the pickup so normal process motion carries dust toward it, not away from it.
  • Minimize unnecessary openings and use curtains, flanges, or partial enclosures where access is required.
  • Avoid drawing valuable product directly into the duct or disrupting weighing, flames, drying, or material trajectories.
  • Provide makeup air without creating cross-drafts that defeat the hood.
  • Design access so operators do not remove or leave open critical enclosure panels.

A nominal “capture velocity” by itself is not a complete hood design. The required flow depends on enclosure geometry, opening area, contaminant momentum, thermal buoyancy, cross-drafts, and how the operator uses the station. Validate difficult sources with observation, smoke visualization where safe, or measurement.

Q = v · AContinuity is a starting point: airflow equals average velocity through the relevant open area times that area. The correct boundary and velocity still require engineering judgment.

3. Establish airflow and size the duct network

Assign a design flow to each source, apply a documented simultaneity case, and create a branch-by-branch air balance. Duct velocity must be high enough to transport the dust but not so high that pressure loss, noise, erosion, and fan energy become excessive.

v = 4Q / (πD²)For a circular duct, use actual volumetric flow Q and inside diameter D.

Total system resistance combines hood entry, straight-duct friction, fittings, branch junctions, separators, filters, silencers, dampers, stacks, and discharge losses. For a preliminary calculation:

Δpsystem = Σ(f · L/D · ρv²/2) + Σ(K · ρv²/2) + ΔpequipmentUse gas properties at the relevant section and equipment pressure drops at realistic clean and dirty conditions.

Do not force balance by closing many dampers after construction. Design branch geometry deliberately, provide measurement points, and reserve dampers for commissioning and controlled operating changes. Check deposition at low flow and abrasion at high flow, especially at elbows, transitions, and fan inlets.

4. Select separation and filtration as a system

ComponentUseful roleKey limitations to check
Dropout boxRemoves coarse, high-momentum material and protects downstream equipment.Large footprint; poor control of fine dust.
CyclonePre-separation, product recovery, spark or coarse-load reduction where suitable.Fine-particle performance, pressure drop, erosion, air leakage, and dust discharge.
Fabric filterHigh-efficiency collection over a broad particle range.Temperature, chemistry, moisture/dew point, cleaning energy, air-to-cloth loading, and fire/explosion risks.
Wet collectorCan cool gas and handle some sticky or ignition-sensitive duties.Wastewater, corrosion, freezing, plume, disposal, and secondary contamination.

For a fabric filter, do not select only by total cloth area. Check filtration velocity by dust and media type, inlet distribution, cleaning method, residual pressure drop, emissions target, hopper behavior, maintenance access, and the consequences of one compartment being offline. Keep the gas safely away from condensation and incompatible media temperatures through all normal and transient cases.

The hopper is not a storage silo unless explicitly designed as one. Size and control the rotary valve, screw, double flap, or pneumatic discharge so collected dust leaves continuously without allowing damaging air leakage.

5. Select the fan at the operating point

The fan must deliver the required actual flow at the calculated system pressure, including appropriate allowances that are explicit rather than hidden. Plot or review the fan curve together with the system curve and confirm the expected operating region, efficiency, absorbed power, motor margin, temperature correction, and control method.

Pshaft ≈ Q · Δp / ηPreliminary shaft power equals actual flow times total pressure divided by combined fan efficiency. Final selection uses certified fan data and the specified gas state.
  • Prefer variable-speed control when operating cases vary materially and the process permits it.
  • Measure differential pressure across filters and critical network sections.
  • Interlock process equipment with confirmed extraction where loss of capture creates risk.
  • Define alarm and shutdown responses for high filter pressure, low airflow, high temperature, fire detection, discharge failure, and abnormal vibration as applicable.

6. Complete the health, fire, and explosion screen

Fine combustible dust dispersed in air may form an explosive atmosphere. Deposits and layers also matter because they can fuel a fire, be disturbed into a cloud, or insulate hot equipment. A preliminary dedusting calculation must never substitute for dust explosibility testing, hazardous-area classification, ignition-source assessment, or an engineered protection concept.

Depending on the material and jurisdiction, the system may require explosion venting or suppression, flameless venting, inlet and outlet isolation, spark detection/extinguishing, conductive bonding and earthing, suitable equipment categories, safe collector location, and documented housekeeping. These measures must be selected as one coordinated protection concept.

Recirculating cleaned air to a workplace can reduce energy use but may be restricted or require enhanced monitoring when the dust is hazardous. In Germany, the applicable Gefahrstoffverordnung and TRGS requirements must be checked for the specific substance and task; for certain carcinogenic, mutagenic, or reprotoxic substances, TRGS 560 addresses recirculation requirements.

7. Commission against measurable acceptance criteria

  1. Inspect installation, access, rotation, grounding, duct cleanliness, dampers, filter media, and discharge devices.
  2. Record fan speed, motor current, airflow or velocity at defined test points, and static/total pressures.
  3. Balance branches in the operating combinations used by production.
  4. Verify capture at each source under representative material feed and cross-draft conditions.
  5. Trend filter differential pressure and cleaning behavior through a realistic loading period.
  6. Test alarms, interlocks, discharge devices, and fire/explosion protection according to the approved plan.
  7. Measure workplace exposure and outlet emissions using the required methods where compliance is part of the duty.
  8. Issue baseline settings, inspection intervals, spare-parts needs, and operator training.

Common reason systems disappoint

The collector was sized, but the source enclosure, branch balance, dust discharge, makeup air, or operating controls were not designed with equal care. Dedusting performance belongs to the whole system.

Sources and engineering boundary

Authoritative regulatory context includes the EU worker-protection requirements for explosive atmospheres in Directive 1999/92/EC, equipment requirements in Directive 2014/34/EU, and Germany’s TRGS 560 for relevant recirculation duties. Current local law, harmonized standards, substance-specific rules, permits, and insurer requirements must be checked for each project.

This article is original preliminary guidance. It does not specify transport velocities, filtration rates, exposure limits, emission limits, explosion relief areas, equipment categories, or safety distances for a particular installation. Final design requires verified process data, applicable standards, vendor performance data, hazard assessment, and competent specialist review.