What this is
What is a dust hazard assessment?
What is a dust hazard assessment?
A structured evaluation of whether a material can form combustible dust, whether it is accumulating somewhere it can be dispersed and ignited, and whether the ignition sources and explosion protection present are adequate for that risk.
What makes a dust combustible?
A material is treated as combustible dust if particles of it, at the size and concentration present in the process, can propagate a flame through a dust cloud. Milk powder, whey, flour, starch, spice and sugar are common examples; the finer the particle, the more readily it ignites.
Who should carry out a dust hazard assessment?
Someone competent in combustible dust hazards specifically, not general safety competence alone. The work depends on interpreting explosibility data, judging where dust genuinely accumulates, and knowing what protection is adequate for the figures involved.
Scope
When is a dust hazard assessment required?
This assessment establishes whether and where a combustible dust hazard exists. It is the analysis other, more specific controls and classifications depend on, not a substitute for them.
Use this template when
- A material handled or processed on site can form combustible dust at the particle sizes present
- A new dust-generating process, material or piece of equipment is being introduced
- An existing dust-generating process has changed materially in material, particle size, throughput or layout
- Housekeeping inspections or an incident suggest dust accumulation is heavier than assumed
- You are running the Chemical Safety and WHMIS programme and this is one of its steps
Do not use it for
- Explosive Atmosphere Zoning Record, which defines classified zones and equipment ratings once a dust hazard has been confirmed, not whether one exists.
- Chemical Risk Assessment, which assesses exposure risk from handling a specific substance in a task, not the process-wide explosion hazard.
- Safety Data Sheet Review, which confirms a data sheet is current and complete, not whether its explosibility data represents the material as processed.
- Chemical Substitution Assessment, which considers replacing a hazardous material with a safer one, rather than managing the hazard as currently used.
- The housekeeping cleaning schedule itself, which implements the frequency this assessment sets and belongs in a cleaning procedure, not the assessment.
Compliance mapping
Which NFPA 652 requirements does this satisfy?
Combustible dust has no dedicated OSHA standard, so the consensus standard, NFPA 652, functions as the benchmark enforcement and insurance both measure against. Defensibility rests on whether the assessment actually followed that method, not on a generic risk rating.
| Clause | Requirement | Where it lands |
|---|---|---|
| NFPA 652 sec.7.1.1 | Facility owner must complete and document a Dust Hazard Analysis for combustible-dust-forming materials | Dust characteristics |
| NFPA 652 sec.7.2.3 | DHA must determine explosibility characteristics, including Kst and Pmax, by testing or data representative of the material as processed | Dust characteristics |
| NFPA 654 sec.6.1 | Housekeeping programme must control combustible dust accumulation on floors, equipment, and elevated and concealed surfaces | Where dust accumulates |
| NFPA 654 sec.7.1 | Ignition sources including hot surfaces, static discharge and mechanical sparking must be identified and controlled where combustible dust is present | Ignition sources |
| NFPA 70 Article 500 / NFPA 499 | Electrical equipment in a classified dust location must carry a rating appropriate to that classification | Ignition sources |
| NFPA 68 | Deflagration venting must be sized and installed against the explosibility data for the material and equipment protected | Protection |
| NFPA 652 sec.7.3 | DHA must be reviewed and updated when process, material, or equipment conditions change | Result |
What it does not cover
- Explosive Atmosphere Zoning Record, which defines classified zones and equipment ratings once a dust hazard is confirmed, not whether one exists.
- Chemical Risk Assessment, which assesses handling exposure for a specific task and substance, not the process-wide explosion hazard.
- Safety Data Sheet Review, which confirms the referenced data sheet is current, not whether its data represents the material as processed.
- Chemical Substitution Assessment, which considers replacing a hazardous material rather than managing the hazard as currently used.
- The housekeeping cleaning schedule itself, which implements the frequency this assessment sets and lives in a cleaning procedure, not here.
Global
Dust Hazard Assessment requirements by country
The duty to evaluate combustible dust is close to universal wherever dust-generating processing occurs. What differs is whether a dust-specific standard is referenced directly, treated as guidance, or folded into a broader explosive atmosphere regime.
OSHA CPL 03-00-008; NFPA 652
No dedicated OSHA combustible dust standard exists. Enforcement runs through the General Duty Clause, with NFPA 652 as the recognised-hazard benchmark.
A DHA departing materially from NFPA 652's method leaves a General Duty Clause citation with little to rebut it, since the standard is what inspectors point to for what a competent employer should have done.
Dangerous Substances and Explosive Atmospheres Regulations 2002 (DSEAR)
Statutory duty to assess the risk of explosive atmospheres, including those from combustible dust, and to classify areas where they can occur.
A DSEAR risk assessment is the legal equivalent of a DHA in Great Britain; HSE inspectors expect area classification and equipment selection to follow directly from it.
NFPA 652; IEC 60079 series for equipment in dust atmospheres
NFPA 652 is widely used outside the US as the reference method, but equipment approval schemes differ: IECEx and ATEX ratings aren't interchangeable with NFPA or UL ratings for Class II locations.
A multi-site operation cannot assume a DHA written to NFPA 652 justifies the equipment ratings another regulator requires; the local approval scheme has to be mapped against the findings.
How to complete it
How to complete a dust hazard assessment, step by step
Most fields can be filled from a walkthrough. What decides whether the result is defensible is a small number of judgement calls the fields don't force by themselves.
Kst and minimum ignition energy change with particle size and moisture, often sharply. Literature figures for a coarser or drier version understate the hazard of the finer dust milling or conveying actually generates on site, and testing the real material is the only way to know the gap.
The accumulation causing a secondary explosion is almost never the layer visible on a normal walkthrough. Ceiling voids, duct interiors, cable trays and equipment tops need to be part of the inspection scope on a defined schedule, not treated as inaccessible and skipped.
Static discharge, friction sparking and hot surfaces are transient conditions a single walkthrough can miss entirely. Recording what was checked and how, rather than a bare no, lets a reviewer tell a genuinely controlled area from one that simply wasn't sparking that day.
Venting, suppression and isolation are only valid for the Kst and Pmax figures used to design them. A process change altering particle size, moisture or throughput can invalidate installed protection while it still looks correctly fitted, with nothing about the equipment showing the numbers have moved.
What auditors find
Most common dust hazard assessment findings
Findings here usually trace back to where the assessor looked, not to a missing signature or an incomplete field.
| Finding | Clause | What fixes it |
|---|---|---|
| Explosibility data taken from generic literature rather than tested for the material and particle size as processed. | NFPA 652 sec.7.2.3 | Commission Kst and Pmax testing for the material as milled or conveyed where particle size or moisture differs from the literature source. |
| Dust accumulation above head height, inside ductwork, or behind enclosures excluded from the inspection scope. | NFPA 654 sec.6.1 | Extend the housekeeping inspection to overhead surfaces, duct interiors and concealed spaces on a defined schedule. |
| Cleaning carried out with compressed air, raising dust into suspension rather than removing it safely. | NFPA 654 sec.6.1 | Restrict cleaning to vacuum or wet methods rated for combustible dust; remove compressed air from the procedure. |
| Electrical equipment in a dust-affected area not rated for the classification of that location. | NFPA 70 Article 500 | Verify equipment ratings against the area's dust classification before installation, move, or reuse. |
| Explosion venting or suppression sized to explosibility data that no longer matches current process conditions. | NFPA 68 | Re-size protection whenever Kst or Pmax figures change, and record the design basis alongside the equipment. |
| Assessment not reviewed after a change to process, material, particle size or equipment. | NFPA 652 sec.7.3 | Link the assessment to management of change so a process or material change raises the review automatically. |
Case in point
Case in point: the powder that got finer and the ceiling nobody opened
A dairy blending plant's dust hazard analysis, written for a coarse milk powder, rated the packing area medium risk using literature explosibility figures for that grade. Housekeeping covered floors and working-height surfaces, found them clean, and was signed off for several cycles. A new line later introduced a finer, atomised powder for solubility, and nobody re-tested explosibility, since the change was managed as formulation, not process safety.
A static discharge from an ungrounded transfer hose ignited a small primary event inside a mixer. The pressure wave lofted fine powder accumulating, undetected, above the packing hall's suspended ceiling for months, and the resulting secondary explosion travelled the hall's length. The finer powder had a markedly lower ignition energy and higher Pmax than the coarse-grade figures relied on, and the ceiling void had never been part of any inspection scope the site had run since it was built.
The template
The template, field by field
The form exactly as it installs. Every field, option, score and conditional rule is editable, and the links to other templates come with it.
7 sections
- Reference
- SAF-090
- Archetype
- Assessment
- Record ID
- RSK-2026-000
- Scoring
- Risk band
- Direction
- High is bad
- Singleton
- No
- Basis
- NFPA 652, OSHA CPL 03-00-008
- Links
- Links Substance, Asset
- Tags
- Chemical, Fire, Process safety
- Sections
- 7
- Fields
- 46
- Follow up fields
- 3
- Repeating sections
- 0
- Links out
- 4
Header
9 fieldsAssessment ID*
Auto sequence. Format RSK-2026-00000.
The record's own ID. Other templates point at this value.
Status*
Drives who this goes to next.
- Planned2 pts
- In progress2 pts
- Complete3 pts
- Deferred0 pts
- Open0 pts
- Closed3 pts
- Overdue0 pts
Date and Time*
Completed By*
Site*
Site ID*
Format SITE-000.
Links to FDN-001 Site ID
Area*
The area within the site.
Exact Location
Drop a pin for anything hard to find.
Combustible Dust In Food Plants
Milk powder, whey, flour, starch, spice and sugar are all combustible. A primary explosion shakes settled dust into the air and causes a far larger secondary explosion. Housekeeping is the control that matters most.
Dust characteristics
6 fieldsDust Type*
- Milk powder0 pts
- Whey powder0 pts
- Flour0 pts
- Starch0 pts
- Sugar0 pts
- Spice0 pts
- Non combustible4 pts
Explosibility Data Available*
- Yes, tested3 pts
- From literature2 pts
- No0 pts
Kst Value
Minimum Ignition Energy Known
- Yes3 pts
- No0 pts
Particle Size Below 500 Micron*
- No3 pts
- Yes0 pts
Moisture Content
Where dust accumulates
7 fieldsAsset
Asset ID
Format AST-0000.
Links to FDN-002 Asset ID
Accumulation On Horizontal Surfaces*
- None visible3 pts
- Light layer1 pt
- Heavy layer0 pts
Accumulation Above Head Height*
Overhead accumulation causes the secondary explosion. It is the layer nobody cleans.
- None3 pts
- Light1 pt
- Heavy0 pts
Layer Depth Millimetres
Hidden Accumulation Checked*
Above ceilings, behind panels, inside ducting and on cable trays.
- Yes2 pts
- No0 pts
- N/Aexcluded from denominator
Percent Of Surfaces Covered
Ignition sources
6 fieldsHot Surfaces Present*
- No3 pts
- Some1 pt
- Yes0 pts
Electrical Equipment Rated For Dust*
- Pass2 pts
- Partial1 pt
- Fail0 pts
- N/Aexcluded from denominator
Static Bonding And Earthing*
- Pass2 pts
- Partial1 pt
- Fail0 pts
- N/Aexcluded from denominator
Mechanical Sparks Possible*
- No3 pts
- Yes, controlled1 pt
- Yes, uncontrolled0 pts
Hot Work Controls Adequate*
- Pass2 pts
- Partial1 pt
- Fail0 pts
- N/Aexcluded from denominator
Tramp Metal Removal In Place*
- Yes2 pts
- No0 pts
- N/Aexcluded from denominator
Protection
6 fieldsExplosion Venting Fitted*
- Pass2 pts
- Partial1 pt
- Fail0 pts
- N/Aexcluded from denominator
Isolation Between Vessels*
- Yes3 pts
- Partly1 pt
- No0 pts
Suppression System Fitted
- Pass2 pts
- Partial1 pt
- Fail0 pts
- N/Aexcluded from denominator
Dust Extraction Adequate*
- Pass2 pts
- Partial1 pt
- Fail0 pts
- N/Aexcluded from denominator
Wet Or Vacuum Cleaning Only*
Compressed air raises a dust cloud and creates the explosive atmosphere.
- Yes3 pts
- Mostly1 pt
- No, compressed air used0 pts
Cleaning Frequency Defined*
- Pass2 pts
- Partial1 pt
- Fail0 pts
- N/Aexcluded from denominator
Related records
1 fieldChemical Assessment ID
The assessment covering the dust source.
Links to SAF-086 Assessment ID
Result
11 fieldsDust Hazard Analysis Complete*
- Pass2 pts
- Partial1 pt
- Fail0 pts
- N/Aexcluded from denominator
Residual Band*
- Low, 1 to 45 pts
- Medium, 5 to 94 pts
- High, 10 to 142 pts
- Very high, 15 to 191 pt
- Extreme, 20 to 250 pts
Action Required*
Raise the action record, then enter its reference here.
- No2 pts
- Yes0 pts
Priority
- High0 pts
- Medium1 pt
- Low3 pts
CAPA ID
Format CAPA-2026-00000.
Links to FDN-014 CAPA ID
Action Owner
Next Review Due*
Assessor*
Signature*
Site Manager*
Second Signature*
SAF-090 · record IDs look like RSK-2026-000 · Links Substance, Asset
Open in KnowellaRun it with agents
From a document you fill in to a programme that runs itself
The assessment identifies the hazard. What prevents the incident is whether a formulation or process change reaches the people who maintain the explosibility data and the protection sized against it.
Holds the assessment library against the asset and material registers, flags assessments whose subject has changed, and routes review to a competent assessor.

Watches formulation and process change records for events that should invalidate an assessment's explosibility data, raising review rather than waiting for the interval.
Ties electrical equipment and explosion protection ratings to the asset record, so a replacement part is checked against the area's classification first.
Connects the housekeeping and hot work controls this assessment depends on to the training record that should already cover them.
This template lives in KnowSafe — safety and compliance. Incidents, hazards, permits, inspections and the critical controls behind them.
Meet KnowSafe→Glossary
Dust Hazard Assessment definitions and key terms
- Combustible dust
- A finely divided material that, at the particle size and concentration present in a process, can propagate a flame through a dust cloud.
- Kst value
- A measure of a dust's explosion severity, derived from testing, used to size venting, suppression and isolation.
- Minimum ignition energy (MIE)
- The smallest energy, such as a static discharge, capable of igniting a dust cloud of a given material at a given concentration.
- Deflagration venting
- A protection method releasing the pressure of an internal dust explosion through a designed panel or duct, sized to the material's data.
- Secondary explosion
- A larger explosion caused when a primary event's pressure wave disturbs settled dust elsewhere, dispersing it into a cloud that then ignites.
FAQ
Frequently asked questions about dust hazard assessment
What actually counts as combustible dust?+
Any finely divided material that can propagate a flame through a cloud of its own particles in air, at the particle size and concentration the process generates. Milk powder, whey, flour, starch, spice and sugar are common examples; the same material at a much coarser grind may not qualify.
Why does particle size matter so much for the Kst value?+
Finer particles have more surface area relative to mass, igniting more readily and burning faster once airborne. A Kst figure measured for a coarse grade understates the hazard of a finer version of the same material, sometimes significantly.
Is a written dust hazard analysis legally required?+
NFPA 652 requires one for facilities handling materials capable of forming combustible dust, and in the US it is the benchmark OSHA cites via the General Duty Clause absent a dedicated standard. In Great Britain the equivalent duty sits in DSEAR.
What is the difference between a primary and a secondary explosion?+
A primary explosion is the initial ignition, often small, inside equipment or a confined space. A secondary explosion happens when that event's pressure wave disturbs dust settled elsewhere, dispersing it into a cloud that then ignites and is typically far more destructive.
How often should a dust hazard assessment be reviewed?+
Whenever process, material, particle size, throughput or equipment changes, and at a stated interval as a backstop. A review date alone won't catch a formulation change managed outside safety, exactly the change most likely to invalidate the data relied on.
If dust extraction is already installed, do we still need explosion venting?+
Extraction reduces dust available to ignite but doesn't eliminate accumulation, and doesn't address a primary event inside the equipment itself. Whether venting is also needed depends on the explosibility data and equipment configuration, not on extraction being present.
Keep going
Related templates and programmes
Industries this is written for
Programmes this belongs to
Used together in Chemical Safety and WHMIS
Spill Report
Records a release of chemical, fuel, oil or wastewater
Spill Response Record
Records what was done to contain, clean up and dispose of a spill
Chemical Substitution Assessment
Assesses whether a hazardous substance can be replaced by something safer, and what the substitute brings with it
Restricted Substance Compliance Record
Records compliance with restricted substance obligations covering ozone depleting gases, persistent chemicals and packaging materials
Explosive Atmosphere Zoning Record
Records the zoning of areas where flammable dust or vapour can form an explosive atmosphere, and the equipment permitted there
Chemical and Substance Register
Lists every chemical and hazardous substance held on site, with quantity, location and hazard class
More in Chemicals
Chemical Inventory Record
Records what chemicals are held where, in what quantity and in what container
Safety Data Sheet Review
Checks each safety data sheet is current, complete and available to the people who use the product
Chemical Risk Assessment
Assesses the risk of using a chemical for a specific task, covering exposure route, quantity, ventilation and PPE
Chemical Storage Compatibility Check
Checks that stored chemicals are separated correctly so incompatible products cannot mix
Spill Kit Inspection
Checks spill kits are stocked, sealed, accessible and suited to the chemicals nearby
Chemical Decanting Checklist
Steps through transferring a chemical from one container to another safely, including labelling the new container

Written and reviewed by
Siddarth Singh
Founder & Chief Executive Officer, Knowella
Certified Safety Professional and industrial and systems engineer with more than a decade inside food supply chain, freight and manufacturing operations. This page was written against the current text of the standards it cites, not against secondary summaries of them.
- Certified Safety Professional (CSP), Board of Certified Safety Professionals
- MBA, University of Chicago Booth School of Business
- MS and BS, The Ohio State University, Industrial and Systems Engineering
- Six Sigma Black Belt
Sources and last review. Reviewed 16 August 2026 against:
- NFPA 652 — Standard on the Fundamentals of Combustible Dust
- NFPA 654 — Standard for the Prevention of Fire and Dust Explosions
- OSHA CPL 03-00-008 — Combustible Dust National Emphasis Program
- NFPA 68 — Standard on Explosion Protection by Deflagration Venting
This page is general guidance, not legal advice. Confirm requirements with your jurisdiction’s regulator.