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Anodising Process Operations SWMS

SWMS template for anodising process operations. Covers Aluminium anodising, sulfuric/chromic acid lines.. 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.

Anodising process operations involve immersing aluminium components into electrified sulfuric or chromic acid baths to grow a controlled oxide layer, with rinse, sealing and dye stages running in parallel. The work exposes operators to concentrated mineral acids, hexavalent chromium mist (Group 1 IARC carcinogen), hydrogen evolution at the cathode, and high-current DC rectifier circuits typically running at 12–24V but at hundreds of amps. Under WHS Regulation 2025 a SWMS is mandatory because the task constitutes High Risk Construction Work and High Risk Work under multiple section 291 categories, including work involving energised electrical installations, work where workers may inhale a hazardous chemical, and work near a substance under pressure or at extreme temperature. PCBUs operating anodising lines must document hazard identification, control selection against the hierarchy, and worker consultation before any tank charging, parts loading, or rectifier energisation occurs. This SWMS template provides the editable, jurisdiction-neutral framework required.

Hazards identified

7 hazards covered, sorted by priority.

Hexavalent chromium mist liberated from chromic acid anodising tanks during electrolysisHIGH

Carcinogenic inhalation exposure causing lung cancer, nasal septum perforation, occupational asthma and chronic dermatitis in operators

Concentrated sulfuric acid splash from tank charging, decanting or workpiece withdrawalHIGH

Full-thickness chemical burns to skin and eyes, corneal scarring, permanent disfigurement and potential respiratory tract injury

DC rectifier busbar contact at 150–600A while loading jigs onto energised cathode railsHIGH

Arc flash burns, cardiac arrhythmia from low-voltage high-current shock, and molten metal ejection causing severe thermal injury

Hydrogen gas accumulation above tank surface during high-current-density electrolysis cyclesHIGH

Flash fire or deflagration on ignition causing facial burns, tank rupture and pressure injury to nearby personnel

Caustic soda etch tank exposure during pre-treatment dipping at 50–60°CMEDIUM

Alkaline burns more insidious than acid burns, deep tissue saponification, and aerosol inhalation causing pulmonary oedema

Manual handling of loaded titanium jigs weighing 25–40kg above open acid tanksMEDIUM

Lumbar disc injury, shoulder rotator cuff tears, and consequential acid immersion injury if jig is dropped mid-transfer

Slip hazard from acid, rinse water and dye contamination on bund and walkway surfacesLOW

Falls onto chemical-wet floors causing fractures, lacerations and secondary chemical exposure through compromised PPE

Control measures

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

  1. 1Elimination — Eliminate chromic acid anodising where possible by substituting Type II sulfuric anodising or Type III hard anodising for non-aerospace specifications.
  2. 2Elimination — Remove manual jig transfer by installing automated hoist-and-rail systems that index parts between tanks without operator presence over the bath surface.
  3. 3Substitution — Replace hexavalent chromium sealing with trivalent chromium or nickel acetate sealants where corrosion specifications permit, eliminating IARC Group 1 carcinogen exposure.
  4. 4Engineering — Install lateral push-pull LEV on every acid and etch tank achieving 0.5 m/s capture velocity, ducted to a packed-bed scrubber per AS 1668.2 design criteria.
  5. 5Engineering — Fit rectifiers with insulated busbar covers, residual current devices, lockable isolators and interlocked guards preventing energisation while loading doors are open.
  6. 6Engineering — Install bunded flooring with 110% containment, acid-resistant grating, and continuous hydrogen gas monitoring with alarm at 10% LEL above each tank.
  7. 7Administrative — Implement permit-to-work for tank charging, dilution and decanting; restrict to trained operators with documented competency reviewed annually under AS/NZS 2865.
  8. 8Administrative — Conduct pre-start atmospheric monitoring for chromium VI per AS 3640 with results recorded and reviewed against the WES of 0.05 mg/m³ TWA.
  9. 9PPE — Provide acid-resistant PVC or neoprene gauntlets, chemical splash apron, full face shield over safety glasses, and acid-rated rubber boots compliant with AS/NZS 2210.
  10. 10PPE — Supply powered air-purifying respirators with combined acid-gas/HEPA cartridges for chromic acid line operators, fit-tested per AS/NZS 1715 and 1716.

Applicable Codes of Practice

AS/NZS 2865:2009 Confined spaces — applied to tank entry for maintenance, sludge removal and lining repair⚖ Legally binding · 1 Jul 2026

Triggers entry permit, atmospheric testing, standby person and rescue plan requirements before any worker enters a drained or partially drained anodising tank.

AS 1668.2:2024 The use of ventilation and air-conditioning in buildings — mechanical ventilation in buildings

Specifies minimum capture velocities and exhaust design for laboratory and process tanks emitting acid mists and chromium VI aerosols requiring local exhaust.

Model Code of Practice: Managing Risks of Hazardous Chemicals in the Workplace (Safe Work Australia, 2024)⚖ Legally binding · 1 Jul 2026

Mandates SDS register, manifest, placarding, health monitoring for chromium and acid mist exposed workers, and emergency plan for major spill scenarios.

AS/NZS 3000:2018 Electrical installations (Wiring Rules) — Section 7 special locations including wet electrolytic process areas⚖ Legally binding · 1 Jul 2026

Governs rectifier installation, earthing, IP rating of fittings near tanks, and RCD protection requirements for the high-current DC electrolysis circuit.

Who this is for

  • Anodising plant operators and line supervisors
  • Surface finishing PCBUs in aerospace and architectural sectors
  • WHS managers overseeing electroplating facilities
  • Maintenance contractors servicing acid tank lines

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 mid-sized architectural aluminium anodising facility, the day-shift leading hand opens the pre-start brief at 6:45am beside the sulfuric line. Three operators are scheduled to run a 2,400-piece extrusion batch through degrease, etch, desmut, anodise and dye stages. The leading hand walks the team through this SWMS section by section. Under hazard identification, the team flags that today's batch includes a small chromic seal run scheduled for 2pm — triggering the PAPR requirement and additional LEV check. Controls are confirmed live: the hydrogen LEL sensor above Tank 4 reads 0%, LEV manometer shows design pressure, and the rectifier RCD test button is pressed and reset. Each operator signs onto the SWMS register, with the new third-year apprentice signing under direct-supervision endorsement only. Mid-shift, an operator reports the etch tank temperature has drifted to 64°C, above the 60°C control limit specified in the SWMS. Work pauses, the SWMS dynamic-review section is consulted, and the team agrees to reduce dwell time and notify maintenance — the variation is initialled on the live document before resuming. At handover, the signed SWMS is filed against the batch traveller as required under the company's chromium health monitoring program.

Related legislation

  • WHS Act 2011 (model)
  • WHS Regulation 2025
  • AS/NZS 3000 — Electrical installations

Frequently asked questions

Is anodising high risk construction work under section 291?

Not as routine production. An anodising line runs in a fixed plant, and factory process work is not construction work, so the s291 categories and the s299 SWMS duty do not attach to a normal production shift. What does apply is the general duty to have a documented safe system of work, supported by specific duties for hazardous chemicals, confined spaces and electrical work. The picture changes when anodising work forms part of a construction project, or when a drained tank is entered for relining or sludge removal — that entry is confined space work under AS/NZS 2865 with a permit, atmospheric testing, a standby person and a rescue plan.

Does this cover chromic acid anodising as well as sulfuric?

Yes, and it treats chromic separately because the exposure is different in kind. Chromic acid tanks liberate hexavalent chromium mist during electrolysis, an IARC Group 1 carcinogen linked to lung cancer, nasal septum perforation and occupational asthma. The document sets pre-start atmospheric monitoring for chromium VI with results reviewed against the workplace exposure standard of 0.05 mg per cubic metre as an eight-hour average, and requires powered air-purifying respirators with combined acid-gas and HEPA cartridges on the chromic line. It also puts elimination first: specifying Type II sulfuric or Type III hard anodising where the finish specification does not demand chromic.

What ventilation does the SWMS require on the tanks?

Lateral or push-pull local exhaust on every acid and etch tank achieving a capture velocity of 0.5 m per second, ducted to a packed-bed scrubber and designed to AS 1668.2. The extraction is verified, not assumed — the pre-start check includes reading the LEV manometer against design pressure, and the worked example has the leading hand doing exactly that before a chromic seal run. Alongside it sits continuous hydrogen gas monitoring with an alarm at 10 percent LEL above each tank, because high current density electrolysis evolves hydrogen at the cathode and a flash above a tank surface is a real event, not a theoretical one.

How does it handle the rectifier and busbar risk?

As a live electrical hazard at low voltage and very high current. Anodising rectifiers typically run at 12 to 24 volts but at hundreds of amps, and operators contact cathode contact rails when loading and unloading jigs. Controls are insulated busbar covers, residual current devices, lockable isolators and interlocked guards that prevent energisation while loading doors are open, with installation and earthing to AS/NZS 3000 including the special-locations provisions for wet electrolytic areas. The monthly press-to-test on the rectifier RCD is part of the pre-start record, so the protection is proven rather than presumed.

How do I use this on a real shift?

You receive an editable Microsoft Word DOCX, bought once, that you populate with your own tanks, chemistry, rectifier ratings and crew. Brief the team on it before charging tanks, loading parts or energising the rectifier, and have every operator sign on — apprentices under a direct-supervision endorsement. Then keep it live. In the worked example an etch tank drifts to 64 degrees against a 60 degree control limit, work pauses, the dwell time is cut, maintenance is notified and the variation is initialled on the document before the line restarts. That amendment trail is what makes it evidence rather than paperwork.

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
Acid baths, electrical, 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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