Aluminium Anodising Knowledge App

Technical information for Type I chromic-acid anodising, Type II sulfuric-acid anodising and Type III hard anodising, including chemistry, electrochemistry, processing, compatible aluminium alloys, dimensional effects, sealing, dyeing, inspection, testing, process controls, failure modes and specification flow-down.

Specification
MIL-PRF-8625
Type I
Chromic-acid anodising
Type II
Sulfuric-acid anodising
Type III
Hard anodic coating

Process overview

Anodising is an electrolytic conversion process in which the aluminium component is made the anode in an acid electrolyte. Controlled oxidation grows an aluminium-oxide coating both into and above the original surface.

What anodising does

  • Improves corrosion resistance by creating a controlled aluminium-oxide layer.
  • Provides a porous surface that can absorb dyes and subsequently be sealed.
  • Improves paint and adhesive-bonding preparation when the specified system permits.
  • Provides electrical insulation except where the film is intentionally removed or penetrated.
  • Type III provides high hardness and improved abrasion and wear resistance.
  • Changes component dimensions because the coating grows partly inward and partly outward.
MIL-PRF-8625 defines six coating types and two classes. This app concentrates on Types I, II and III, but drawings may also call up Types IB, IC or IIB.

Type I — chromic-acid anodising

Type I is produced in a chromic-acid electrolyte. It generally forms a relatively thin, flexible, corrosion-resistant coating with less adverse effect on fatigue strength than thicker sulfuric-acid coatings. It is traditionally used on aerospace structures, complex assemblies and parts containing recesses where residual electrolyte control is important.

Chromic acid contains hexavalent chromium. Worker exposure, mist extraction, waste treatment and environmental controls are critical.

Type II — sulfuric-acid anodising

Type II is produced in a sulfuric-acid electrolyte. It is the most widely used conventional anodising process and provides good corrosion resistance, dyeability, paint adhesion and general engineering protection. The coating is normally thicker and more porous than Type I before sealing.

Type III — hard anodising

Type III uses a low-temperature, closely controlled acid electrolyte and high current density to form a thick, hard, wear-resistant oxide. It is used for sliding surfaces, pistons, cylinders, guides, gears and other components requiring abrasion resistance or electrical insulation.

Sealing improves corrosion resistance but can reduce hardness, abrasion resistance and dimensional accuracy. Type III sealing must be explicitly controlled by the drawing or purchase order.

Class 1 — non-dyed

Class 1 coatings are not intentionally dyed. Their natural appearance varies with alloy, pretreatment, thickness, electrolyte and sealing method.

Class 2 — dyed

Class 2 coatings are coloured using an approved dye or colouring process before sealing. Colour matching must account for alloy, coating thickness, surface finish, dye concentration, pH, temperature, time and sealing.

Chemistry, electrochemistry and coating structure

The anodic film is formed electrochemically from the aluminium substrate. The electrolyte supports current flow and simultaneously dissolves part of the newly formed oxide, producing the characteristic porous structure.

Fundamental anodic reactions

Anodic metal oxidation: 2Al → 2Al³⁺ + 6e⁻

Oxide formation: 2Al + 3H₂O → Al₂O₃ + 6H⁺ + 6e⁻

Cathodic hydrogen evolution: 6H⁺ + 6e⁻ → 3H₂↑

The coating consists mainly of aluminium oxide, commonly represented as Al₂O₃, but the as-formed film is hydrated, porous, contains electrolyte-derived species and is not a perfectly stoichiometric crystalline oxide.

The work is the anode. Poor electrical contact increases resistance and heat, causing thin coating, arcing, burning or complete loss of processing.

Type I representative chemistry

Chemical/speciesFormulaRole
Chromium trioxideCrO₃Forms chromic acid in water; principal electrolyte constituent.
Chromic acidH₂CrO₄Acidic Cr(VI) electrolyte species.
Hydrogen chromateHCrO₄⁻Cr(VI) species dependent on pH and concentration.
DichromateCr₂O₇²⁻Equilibrium Cr(VI) species in more acidic/concentrated conditions.
Aluminium ionsAl³⁺Accumulate through substrate dissolution and affect bath performance.

Chromic-acid anodising typically operates at higher voltage and lower current density than sulfuric anodising. The film is relatively thin and has a branched or less regularly porous morphology.

Type II representative chemistry

Chemical/speciesFormulaRole
Sulfuric acidH₂SO₄Primary electrolyte; provides conductivity and controlled oxide dissolution.
Hydrogen sulfateHSO₄⁻Principal acidic sulfate species.
SulfateSO₄²⁻Electrolyte-derived species incorporated to some extent in the porous film.
Aluminium sulfate speciesAl₂(SO₄)₃ / complexesForm as aluminium dissolves; excessive aluminium loading changes process behaviour.

Sulfuric acid attacks the outer oxide while the electric field grows new oxide at the metal/oxide interface. The balance between formation and dissolution creates ordered pores above a thin barrier layer.

Type III hard-anodising mechanism

Type III generally uses sulfuric-acid-based chemistry at low temperature, strong agitation and high current density. Cooling suppresses chemical dissolution so that a much thicker coating can grow.

  • Increasing voltage is normally required as the electrically resistive film thickens.
  • Local current concentration at edges and sharp features can cause burning.
  • High-silicon and high-copper alloys generate more heat and may limit achievable thickness.
  • Pulse, ramped-current or modified electrolytes may be used where permitted by the qualified process.

Barrier layer, pores and sealing chemistry

  • Barrier layer: dense oxide immediately above the aluminium substrate; thickness is broadly related to formation voltage.
  • Porous layer: columnar cells with central pores formed by field-assisted oxide growth and electrolyte dissolution.
  • Hot-water sealing: hydrates aluminium oxide toward boehmite-like aluminium oxyhydroxide, commonly represented as AlO(OH), swelling the pore walls and closing pores.
  • Nickel acetate sealing: combines hydration with precipitation of nickel-containing compounds in the pores.
  • Dichromate sealing: historically used where specified; introduces Cr(VI) hazards and may alter colour.
  • Cold sealing: commonly uses nickel fluoride chemistry; requires close control and may require an ageing or hot-water post-treatment.

Simplified hydration: Al₂O₃ + H₂O → 2AlO(OH)

Dimensional change and coating growth

Anodic oxide occupies more volume than the aluminium consumed. A commonly used engineering approximation is that approximately half the total Type II or Type III coating thickness penetrates the original surface and approximately half builds outward, but the actual ratio depends on alloy and process.

  • External dimensions increase by roughly the outward-growth component.
  • Hole diameters reduce by approximately twice the inward surface growth on opposing sides.
  • Threads, bearing fits, bores, sealing lands and electrical contact areas require allowance or masking.
  • Coating thickness is not the same as dimensional increase.

Typical process sequence

The approved processor must use a controlled and validated process appropriate to the alloy, geometry, coating type, class, thickness, dye, seal and end use.

1. Contract reviewConfirm specification revision, type, class, thickness, sealing, dye, alloy, masking and tests.
2. Tooling and maskingProvide secure electrical contact and protect threads, fits, bores and prohibited areas.
3. DegreaseRemove oil, coolant, polishing compound, silicone and temporary protectives.
4. Non-etch Alkaline cleanAchieve complete wetting. Avoid etch unless required by contract.
5. Rinse (1 minute min.)Use clean, well-agitated water and prevent drying or carry-over.
6. Etch / brightenUse only when required; controls appearance, roughness and material removal.
7. Deoxidise / desmutRemove alloying-element residues and activate the aluminium.
8. Rinse (1 minute min.)Remove acid and dissolved metals before anodising.
9. AnodiseControl electrolyte, temperature, current density, voltage ramp, time and agitation.
10. Rinse (1 minute min.)Remove electrolyte without damaging or contaminating the porous film.
11. Dye / post-treatApply approved colouring or lubricant impregnation where specified.
12. Seal, dry and inspectSeal where required, rinse, dry, inspect, test and protect from damage.

Cleaning and pretreatment

  • Water-break-free surface after cleaning.
  • Controlled cleaner concentration, temperature, time and contamination.
  • Etching changes dimensions, surface roughness and appearance.
  • Nitric-acid-based or proprietary deoxidisers remove copper, silicon and other smut.
  • Mixed assemblies, inserts and trapped solution require special review.

Racking and electrical contact

  • Contact must carry the required current without overheating.
  • Contact marks must be located in permitted areas.
  • Racks must resist the electrolyte and remain mechanically secure.
  • Air pockets prevent coating; gas pockets and poor orientation cause defects.
  • Contact pressure must account for oxide formation around the contact point.

Dyeing

  • Control coating thickness and pore condition before dyeing.
  • Control dye identity, concentration, pH, temperature, time and contamination.
  • Use colour standards and defined lighting where colour matching is required.
  • Rinse thoroughly before sealing to prevent bleed, staining and seal contamination.
  • UV exposure, heat and chemicals can fade some dyes.

Sealing

  • Control seal chemistry, pH, temperature, time, water quality and loading.
  • Under-sealing leaves excessive porosity and poor corrosion resistance.
  • Over-sealing may produce bloom, smut, loss of colour or dimensional change.
  • Hardcoat should remain unsealed where wear is primary unless sealing is explicitly required.

Compatible aluminium alloys and design considerations

Most wrought and cast aluminium alloys can be anodised, but alloying elements strongly influence colour, coating quality, electrical efficiency, corrosion performance and achievable thickness.

FamilyTypical behaviourImportant risks and controls
1xxxHigh-purity aluminium; generally forms clear, uniform and highly corrosion-resistant coatings.Soft substrate limits wear performance despite good oxide quality.
2xxx Al-CuCopper reduces anodising efficiency and can give yellow, grey or mottled films.Higher risk of burning, pitting and reduced corrosion performance; pretreatment and current ramp are critical.
3xxx Al-MnGenerally anodises satisfactorily; manganese may darken the natural colour.Appearance variation with temper, fabrication and surface condition.
4xxx Al-SiSilicon remains partly undissolved and produces grey to dark coatings.High silicon can give nonuniform appearance, lower conductivity during processing and limited hardcoat thickness.
5xxx Al-MgUsually provides good corrosion resistance and decorative response.High-magnesium alloys can develop grey tones; avoid alkaline etching.
6xxx Al-Mg-SiWidely anodised with generally good colour and coating quality.Extrusion die lines, welds and local microstructure can remain visible.
7xxx Al-Zn-Mg-CuHigh-strength aerospace alloys can be anodised but are sensitive to heat and aggressive processing.Burning, pitting, intermetallic attack and fatigue effects require close control.
Cast aluminiumResponse depends strongly on silicon, copper, porosity and casting quality.Dark appearance, smut, retained solution, gas entrapment, pitting and nonuniform thickness are common risks.

Welds, brazed joints and mixed metallurgy

Weld metal and heat-affected zones may anodise to a different colour and thickness. Copper-bearing filler, silicon-rich filler and brazing residues can produce severe colour differences or local attack. Assemblies that trap acid require drainage and rinsing provisions.

Mechanical-property effects

Anodising does not normally create the classic steel hydrogen-embrittlement mechanism, but surface attack, residual stress, thick brittle oxide and sealing temperature can affect fatigue performance. Highly stressed parts, sharp radii and high-strength alloys need design-authority review.

Equipment and facilities

Anodising requires controlled chemical processing equipment plus substantial electrical power, cooling, ventilation, measurement and wastewater-treatment capability.

Process line equipment

  • Compatible cleaning, etching (if required), deoxidising, anodising, dye, seal and rinse tanks.
  • Rectifier with controlled current, voltage, ramp and recording capability.
  • Cathodes correctly sized and positioned for uniform current distribution.
  • Refrigeration and heat exchangers, especially for Type III.
  • Air agitation or solution circulation designed to avoid local heating.
  • Racks, clamps, masking plugs, tapes and stop-off materials.
  • Hoists, timers, drainage stations and clean drying equipment.

Laboratory and measurement equipment

  • Acid titration and dissolved-aluminium analysis equipment.
  • Calibrated temperature probes, pH meters and conductivity meters.
  • Coating-thickness instruments and metallographic sectioning facilities where required.
  • Analytical balance for coating-weight tests.
  • Seal-quality, dye-bleed and spot-test equipment.
  • Salt-spray cabinet, abrasion tester and dielectric test equipment.
  • Calibrated current and voltage measurement independent of display indicators where required.

Safety and environmental controls

  • Local exhaust ventilation for acid mist and chromic-acid operations.
  • Interlocked rectifier and safe rack-handling arrangements.
  • Acid-resistant PPE, eyewash, emergency shower and spill response.
  • Segregated storage for acids, alkalis, oxidisers, dyes and seal chemicals.
  • Wastewater treatment for acidity, aluminium, chromium, nickel, fluoride and dye contaminants as applicable.
  • Formal control of hexavalent chromium exposure for Type I and dichromate sealing.

Process controls and validation

Operating limits must come from the approved processor specification and qualified chemistry. The values below identify what must normally be controlled, not universal set points.

Stage / variableTypical controlsRisk when uncontrolled
CleanerConcentration, temperature, time, oil loading, dissolved aluminium, water-break test.Bare areas, fingerprints, pitting, adhesion failure.
Etch / deoxidiserAcidity/alkalinity, inhibitor, dissolved metals, fluoride, temperature, time and alloy compatibility.Over-etch, dimensional loss, smut, pitting, mottling.
Anodising electrolyteAcid concentration, aluminium content, contaminants, temperature, agitation and tank uniformity.Thin film, soft film, burning, poor colour, corrosion failure.
Electrical cycleCurrent density, voltage, ramp rate, time, contact resistance, load calculation and waveform.Arcing, burning, nonuniform thickness, low hardness.
DyeIdentity, concentration, pH, temperature, time, contamination and colour standard.Wrong shade, fading, bleed, uneven colour.
SealSeal type, concentration, pH, temperature, time, water quality, loading and ageing.Corrosion failure, dye bleed, bloom, softening, wear loss.
RinsesConductivity, pH, flow, agitation, chloride, hardness and carry-over.Staining, contamination, pitting, poor seal or colour.
RecordsPart/lot, alloy, rack, bath, load, current-time profile, analyses, operator, tests and concessions.Loss of traceability and inability to demonstrate validated processing.

Type III special controls

  • Accurate surface-area calculation and current-density control.
  • Controlled current ramp to avoid thermal shock and edge burning.
  • High-capacity refrigeration and continuous temperature monitoring.
  • Strong, uniform agitation around recessed and massive sections.
  • Thickness checks at representative low- and high-current-density areas.
  • Defined sealing status and allowance for final grinding or honing if permitted.

Bath maintenance

  • Scheduled analysis and statistical review of trends.
  • Control dissolved aluminium by decant, regeneration, ion exchange or bath replacement as applicable.
  • Inspect cathodes, busbars, contacts, cooling coils and agitation.
  • Prevent chloride, copper, iron, cleaner and dye cross-contamination.
  • Process representative test panels after major adjustment or maintenance.

Inspection and testing

The applicable drawing, contract and specification determine the required sampling and acceptance tests. Visual inspection alone cannot confirm coating performance.

Visual inspection

  • Complete coverage except at permitted contact and masked areas.
  • No burns, arcing, powder, pitting, corrosion, stains, scratches or handling damage.
  • Uniformity appropriate to alloy and part geometry.
  • Class 2 colour compared against the specified standard under controlled lighting.
  • Contact marks located only where permitted.

Coating thickness

Thickness may be measured by eddy-current instruments, microscopic cross-section or other approved methods. Curvature, roughness, substrate conductivity, alloy, edge effects and calibration standards influence results.

Corrosion resistance

Neutral salt-spray testing is commonly used for process-control or qualification. Test panels, alloy, coating type, class, seal, edge preparation, exposure and acceptance criteria must match the governing requirement.

Seal quality

Seal quality may be evaluated by acid-dissolution, dye-stain, admittance, mass-loss or other specified methods. A visually acceptable sealed coating can still have excessive residual porosity.

Abrasion and hardness

Type III performance is often verified by abrasion resistance rather than indentation hardness alone. Alloy, thickness, seal, test wheel, load, cycles and conditioning significantly affect results.

Electrical and dielectric properties

Anodic oxide is electrically insulating. Breakdown voltage depends on thickness, porosity, defects, sealing, humidity and test geometry. Do not rely on anodising for safety-critical insulation without a defined and validated requirement.

Failure modes and troubleshooting

Select an observed symptom to review likely causes, effects and corrective actions.

Drawing and purchase-order information

Type, class, thickness, sealing and dimensional requirements must be unambiguous. “Anodise to MIL-PRF-8625” alone is usually insufficient.

Recommended drawing information

  • MIL-PRF-8625 and required revision.
  • Type I, II or III and Class 1 or 2.
  • Required coating thickness or permitted range.
  • Areas to anodise, mask, plug or leave conductive.
  • Final dimensional limits and whether dimensions apply before or after coating.
  • Seal type or explicit “unsealed” requirement, particularly for Type III.
  • Dye colour, colour standard, gloss and colour-matching requirements.
  • Contact-mark locations and touch-up permissions.
  • Post-anodise grinding, lapping, honing, impregnation or lubricant.
  • Special corrosion, abrasion, dielectric, adhesion or fatigue requirements.

Recommended purchase-order information

  • Part number, drawing and revision.
  • Alloy, temper, casting or forging condition.
  • Specification, revision, type, class, thickness and sealing.
  • Approved processor and customer-specific process specification.
  • Required certification, test reports, retained panels and traceability.
  • Sampling plan and lot definition.
  • Packaging requirements to prevent scratching, fretting and moisture staining.
  • Notification or approval before chemistry, source, seal or process changes.

Example callouts

GENERAL PURPOSE: ANODISE TO MIL-PRF-8625, TYPE II, CLASS 1, COATING THICKNESS [DEFINE], SEALED [DEFINE SEAL IF REQUIRED]. DIMENSIONS APPLY AFTER FINISH.

DYED: ANODISE TO MIL-PRF-8625, TYPE II, CLASS 2, BLACK, COLOUR TO APPROVED STANDARD, SEALED.

HARDCOAT: HARD ANODISE TO MIL-PRF-8625, TYPE III, CLASS 1, THICKNESS [DEFINE]. DO NOT SEAL / SEAL [SELECT ONE]. MASK IDENTIFIED BEARING, THREAD AND ELECTRICAL CONTACT AREAS.

These examples are guidance only. The design authority must define the technically and contractually correct requirement.

Further information and web links

Verify current revision, contractual applicability and access before use. Supplier operating parameters remain proprietary and process-specific.

ReferenceUseLink
MIL-PRF-8625Performance requirements for anodic coatings on aluminium and aluminium alloys.DLA Quick Search
NASA PRC-5006Detailed NASA process specification for anodising aluminium alloys, including Type I, II and III practices.NASA PDF
ASTM B244Measurement of anodic-coating thickness by eddy-current instruments.ASTM
ASTM B117Salt-spray apparatus and operating practice.ASTM
SAE AMS2469Hard anodic coating of aluminium and aluminium alloys.SAE Standards
SAE AMS2470 / AMS2471 / AMS2472Chromic- and sulfuric-acid anodising requirements for aluminium alloys.SAE Standards
OSHA Hexavalent ChromiumWorker-exposure information relevant to chromic-acid anodising and dichromate sealing.OSHA

External links are for research and revision verification. Purchase may be required for copyrighted standards.