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Hot-Dip Galvanising Plant SWMS

SWMS template for hot-dip galvanising plant. Covers Pre-treatment, kettle, post-treatment.. 8-state AU coverage, CIH-reviewed editable DOCX, available as an instant download.

⚖️WHS Regulation 2025 & Codes of Practice — legally binding from 1 July 2026 (s26A)
👷Reviewed by certified occupational health and safety professionals
🗺️State-specific variants for all 8 Australian jurisdictions
$99 AUD✓ Instant Download Available

SWMS variants reference your state’s WHS legislation. Instant download after payment.

Hot-dip galvanising operations involve immersing fabricated steel into a kettle of molten zinc at approximately 450°C, preceded by acid pickling and fluxing pre-treatment and followed by quenching, passivation and inspection. The work exposes operators to severe thermal hazards, hexavalent chromium and zinc oxide fume, concentrated sulphuric and hydrochloric acid baths, overhead crane loads, and elevated platforms above the kettle and dip tanks. Under WHS Regulation 2011 r291 and the harmonised WHS Regulation 2025, this constitutes High Risk Construction Work because it involves work at heights above 2m over open process tanks, exposure to substances hazardous to health, and the risk of molten metal explosion from moisture ingress. A documented Safe Work Method Statement is mandatory before any galvanising shift commences and must be reviewed whenever the process, jig design, or workforce changes. This template enables PCBUs to demonstrate consultation, hazard identification and control verification across the full pre-treatment, kettle and post-treatment workflow.

Hazards identified

7 hazards covered, sorted by priority.

Molten zinc explosion from moisture trapped in sealed or hollow sections during dippingHIGH

Catastrophic ejection of molten metal causing fatal full-thickness burns, blindness and structural damage to plant

Zinc oxide and hexavalent chromium fume inhalation at kettle edge and passivation tankHIGH

Acute metal fume fever, occupational asthma, and Group 1 carcinogen exposure leading to lung and nasal cancers

Falls from kettle-side jig loading platforms and overhead walkways above acid tanksHIGH

Fatal immersion in molten zinc or concentrated acid, multiple fractures and chemical burns from height impact

Concentrated sulphuric and hydrochloric acid splash during pickling tank loading and decantingHIGH

Full-thickness chemical burns, corneal destruction, respiratory tract injury and permanent disfigurement

Overhead crane jib failure or load swing while transferring jigged workpieces between tanksHIGH

Crush fatalities, tank rupture causing molten zinc release, and secondary fire from hydraulic fluid ignition

Radiant heat stress and dehydration during sustained kettle-side operation above 40°C ambientMEDIUM

Heat exhaustion, heat stroke, syncope leading to falls into adjacent tanks, and cardiac arrhythmia

Manual handling of heavy jigs, chains and ash-skimming tools at awkward postures over the kettleMEDIUM

Lumbar disc injury, rotator cuff tears, hernia and chronic musculoskeletal disorders with long lost-time periods

Control measures

Hierarchy-of-controls order: elimination → substitution → isolation → engineering → administrative → PPE.

  1. 1Elimination — Reject any fabricated article with sealed hollow sections; require vent and drain holes minimum 25% cross-sectional area per AS/NZS 4680 before dipping to eliminate explosion risk.
  2. 2Elimination — Remove personnel from kettle-side during automated dip cycles by installing remote jig lowering controls operated from a shielded pulpit station.
  3. 3Substitution — Replace hexavalent chromium passivation with trivalent chromium or chromium-free polymer post-treatment systems to remove Group 1 carcinogen exposure pathway.
  4. 4Substitution — Use inhibited hydrochloric acid pickling formulations in place of higher-fuming sulphuric blends to reduce airborne acid mist generation.
  5. 5Engineering — Install lateral-draught and push-pull local exhaust ventilation over kettle and passivation tanks designed to AS 1668.2 capture velocities, with quarterly extraction performance testing.
  6. 6Engineering — Provide engineered guardrails, kettle-edge fall arrest anchor points and grated walkways above all tanks, certified to AS/NZS 1657 for platforms and AS/NZS 1891 for fall systems.
  7. 7Engineering — Pre-heat all loads in a dedicated drying oven to above 100°C and verify with infrared thermometer before kettle immersion to eliminate trapped moisture.
  8. 8Administrative — Mandate pre-start SWMS sign-on, jig inspection checklist, vent hole verification and crane pre-operational checks per WHS Regulation r291 and Managing Risks of Plant CoP.
  9. 9Administrative — Schedule kettle-side rotation limiting continuous exposure to 20 minutes with mandated hydration breaks, supported by heat stress monitoring per the Managing Heat at Work CoP.
  10. 10PPE — Issue aluminised proximity suits, chrome leather spats, face shields over P3 respirators, acid-resistant gauntlets and AS/NZS 2210.3 metatarsal safety boots, with health monitoring per WHS Reg Schedule 14.

Applicable Codes of Practice

AS/NZS 4680:2006 Hot-dip galvanized (zinc) coatings on fabricated ferrous articles

Specifies venting, drainage and surface preparation requirements that directly eliminate the molten zinc explosion hazard during immersion.

AS 1668.2:2012 The use of ventilation and airconditioning in buildings — Mechanical ventilation in buildings⚖ Legally binding · 1 Jul 2026

Defines capture velocities and extraction design for kettle and pickling tank LEV systems controlling zinc oxide and acid mist.

Model Code of Practice: Managing Risks of Hazardous Chemicals in the Workplace (Safe Work Australia)⚖ Legally binding · 1 Jul 2026

Triggers SDS register, manifest, placarding and air monitoring duties for sulphuric acid, HCl, zinc ammonium chloride flux and chromates.

AS/NZS 1891.4:2009 Industrial fall-arrest systems and devices — Selection, use and maintenance⚖ Legally binding · 1 Jul 2026

Governs anchor point selection and rescue planning for work on elevated kettle platforms and tank-side walkways above 2 metres.

Who this is for

  • Galvanising plant operators and kettle supervisors
  • Surface coating PCBUs and production managers
  • WHS managers in structural steel fabrication facilities
  • Industrial hygienists auditing metal finishing sites

What you receive

  • Editable DOCX template — Microsoft Word compatible
  • State-specific WHS legislation schedule (NSW/VIC/QLD/SA/WA/TAS/NT/ACT)
  • Hazard register with risk ratings + hierarchy-of-control mapping
  • Worker sign-on register, pre-start checklist, and incident escalation flow

Worked example

At a regional structural steel galvanising facility, the morning shift supervisor convenes a pre-start brief at the kettle pulpit with two operators, a crane driver and a quality inspector. The SWMS is projected on the toolbox screen and each worker walks through the hazard register, confirming today's job — dipping a batch of fabricated handrail assemblies — has been vent-hole inspected and pre-heated to 110°C in the drying oven. The crew identifies that one assembly has a sealed end cap; the supervisor halts that item and returns it to the fabrication bay, citing the elimination control in the SWMS. Operators sign on electronically, confirming they have aluminised PPE, P3 respirators and that the LEV draught gauge reads within the green band per the engineering control entry. Mid-shift, ambient temperature climbs to 42°C and the heat stress monitor triggers; the supervisor invokes the administrative rotation control, swapping kettle-side personnel every 15 minutes and increasing electrolyte break frequency. When a load swing incident occurs with the overhead crane, work stops, the SWMS is reviewed against the crane operations clause, the anchor inspection is repeated, and a dynamic risk note is added before resumption. The signed document is filed to the site WHS register that evening for the two-year retention period.

Related legislation

  • WHS Act 2011 (model)
  • WHS Regulation 2025
  • Managing the Risk of Falls at Workplaces CoP

Frequently asked questions

Does a galvanising plant need a SWMS under section 299?

Not for routine plant operation. A galvanising kettle line is fixed plant and production work in a facility is not construction work, so the s291 high risk construction work categories and the s299 SWMS duty are not what compels the document. The real obligation is a documented safe system of work under the general duties, backed by specific duties for hazardous chemicals, atmospheric monitoring, plant and fall protection. Where galvanising work is carried out as part of a construction project, or a contractor works at height over the tanks during a shutdown and meets an s291 category, a SWMS is then required before that work starts.

How does this prevent a molten zinc explosion?

By elimination at the fabrication gate, not by PPE at the kettle. Any article with sealed hollow sections is rejected, and vent and drain holes to AS/NZS 4680 are verified before the item goes anywhere near the zinc. Loads are then pre-heated in a dedicated drying oven above 100 degrees and confirmed with an infrared thermometer, so trapped moisture has already flashed off before immersion. Moisture entering a kettle at roughly 450 degrees ejects molten metal violently enough to kill. The worked example has a supervisor pulling a single handrail assembly with a sealed end cap out of the batch and returning it to the fabrication bay.

What controls the zinc fume and chromate exposure?

Lateral-draught and push-pull local exhaust over the kettle and passivation tanks, designed to AS 1668.2 capture velocities with quarterly extraction performance testing, and a draught gauge reading verified in the green band at pre-start. Above that sits substitution: replacing hexavalent chromium passivation with trivalent chromium or a chromium-free polymer post-treatment removes a Group 1 carcinogen pathway outright. Zinc oxide fume causes acute metal fume fever and the acid mists carry their own respiratory injury, so P3 respiratory protection under a face shield is specified at kettle edge with scheduled health monitoring for exposed workers.

How is heat stress managed at the kettle?

With a rotation limit rather than a general instruction to take care. Continuous kettle-side exposure is capped at 20 minutes with mandated hydration breaks and heat stress monitoring, and the SWMS expects that limit to tighten as ambient climbs. In the worked example the plant hits 42 degrees, the heat stress monitor triggers, and the supervisor cuts rotation to 15 minutes and increases break frequency. The reason it is treated as a high consequence hazard rather than a comfort issue is the geography: syncope at kettle edge means falling toward molten zinc at 450 degrees or into an open acid tank.

Does it cover the acid pickling and crane work as well as the dip?

Yes — the document runs the full workflow: pre-treatment pickling and fluxing, the kettle, then quenching, passivation and inspection. Concentrated sulphuric and hydrochloric splash during tank loading and decanting has its own hazard line, with inhibited hydrochloric formulations substituted for higher-fuming blends. Overhead crane transfer between tanks is covered for jib failure and load swing, with guardrails, kettle-edge anchor points and grated walkways to AS/NZS 1657 and fall systems to AS/NZS 1891.4. You receive it as an editable Microsoft Word DOCX bought once, adapted to your kettle, jigs and tank layout.

What's in this SWMS

Document details

Regulation
WHS Regulation 2011 r291 — High Risk Construction Work; applicable state WHS Regulations and Codes of Practice.
HRCW Category
Molten zinc, heights, fume
Hazards Identified
7 hazards with controls
Format
Editable DOCX (Microsoft Word)
Author
Certified Industrial Hygienist (CIH)
Delivery
Instant download after payment
CIH-reviewed SWMS · from $99 · instant download

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