Key takeaways
- Iron phosphate at 0.2–0.6 g/m² suits indoor enclosures in ISO 12944-2 category C2; zinc phosphate at 2–4 g/m² is the minimum for C3 and C4 outdoor service.
- Coating weight above about 6 g/m² on zinc phosphate is a defect, not extra protection: coarse crystals reduce powder adhesion and show as chipping at the edges.
- Final rinse conductivity above 30 µS/cm leaves salts in the crystal, and salts cause blistering under powder long before any salt spray test would.
- A salt spray hour figure without a test method, a creep criterion and a scribe pattern is not a specification; ISO 9227 sets the method and leaves duration and interpretation to the product standard.
A powder-coated genset canopy that shows rust at the panel edges after two monsoons has usually failed at the phosphate stage, not in the powder booth. The powder is the visible layer, but the conversion coating underneath decides how well it bonds and how far corrosion creeps once the film is damaged.
Phosphating and conversion coatings for steel are specified with a coating weight in grams per square metre, not with a colour name. Iron phosphate sits at 0.2–0.6 g/m² and zinc phosphate at 1.5–4 g/m². Below the range the surface is barely converted; above it the crystal grows coarse and the adhesion falls. Both failures look identical in a photograph and completely different under a microscope.
The surface treatment and coating hub covers the rest of the coating cluster, from degreasing chemistry to the failure modes that appear after curing.
What phosphating and conversion coatings for steel actually do
A conversion coating reacts with the steel surface and converts the top few micrometres into a phosphate crystal layer. That layer does three jobs. It provides a mechanical key for the powder or paint, it acts as a weak barrier that slows corrosion at a scribe or a damaged edge, and it passivates the surface so flash rust does not form between pretreatment and curing.
Iron phosphating, sometimes called alkali or amorphous phosphating, produces a thin, non-crystalline layer at a lower temperature. It is fast, produces little sludge and suits indoor parts. Zinc phosphating produces a crystalline hopeite layer, needs a titanium activation step before the bath, and gives the corrosion performance that outdoor equipment requires.
Tri-cation zinc phosphate, which adds nickel and manganese to the bath, produces a denser crystal with better paint adhesion on cold-rolled steel. The chemistry is a supplier decision, but the coating weight and crystal size are the customer's specification, and they need to be on the drawing because they drive both cost and performance.
Which phosphate for which environment
The service environment decides the system, and ISO 12944-2 is the vocabulary to use. It classifies atmospheric corrosivity into C1 to CX on the basis of measured mass or thickness loss, and its examples — heated offices, rural air, urban industry, coastal salinity — are a starting point that the standard itself says can mislead. For a canopy in a coastal plant, C4 is the honest assumption until a measured category exists.
| Environment | ISO 12944-2 category | Pretreatment | Coating weight | Ganesh limit or note |
|---|---|---|---|---|
| Heated indoor enclosure | C1–C2 | Iron phosphate | 0.2–0.6 g/m² | Seven-tank line, no activation stage needed |
| Unheated store or plant room | C2 | Iron phosphate or light zinc | 0.6–1.5 g/m² | Condensation is the risk, not pollution |
| Outdoor industrial or urban | C3 | Zinc phosphate | 1.5–3 g/m² | Activation stage is mandatory |
| Coastal or chemical plant | C4 | Zinc phosphate | 3–5 g/m² | Film build and powder type also change |
| Coastal with high salinity | C5 | Zinc phosphate plus primer | 3–5 g/m² | Duplex system; single-coat powder is not enough |
| Powder adhesion target | All | Activated zinc or iron | Crystal ≤ 10 µm | Cross-hatch test to the agreed method |
Above C5 the answer is not more phosphate. A duplex system — galvanising or zinc-rich primer under the powder — changes the substrate and the corrosion mechanism, and it has to be planned before the parts are cut rather than added at the coating stage.
The seven stages and the number each one controls
The line matters more than the chemical name. A seven-tank sequence gives each stage its own tank and its own rinse, which is what allows the bath to be controlled instead of contaminated by the previous step.
Stage 1 and 2: degrease and rinse
Alkaline degreasing at 55–60 °C removes drawing oil, and the rinse that follows must not return oil to the surface. A part with a 2 µm oil film will phosphate patchily, and the patches appear as a mottled finish under a thin powder coat even when the salt spray result passes.
Degreasing is also where the shape of the part matters. A box section with a folded seam traps oil, and a 30 s spray does not reach the inside of the seam. The degreasing guide for mild steel covers the geometry that causes it.
Stage 3: activation
A titanium-based conditioner deposits a fine nuclei layer on the steel so the phosphate crystals grow small and dense. Skip it, or let the bath age out, and the same phosphate bath produces a coarse crystal at the same coating weight. Crystal size is not on the coating weight certificate, which is why two parts can both read 3 g/m² and behave completely differently.
Stage 4: phosphating
Zinc phosphate runs at 40–55 °C with 15–20 minutes of immersion for a medium coating weight. Free acid, total acid and iron content are the three bath parameters that move during a shift, and the ratio between free and total acid controls both the coating weight and the crystal structure.
Iron phosphate runs cooler and faster, typically 35–45 °C, and produces 0.2–0.6 g/m² in a few minutes. It is more forgiving of the bath but less protective at a scribe.
Stage 5 and 6: rinse and demineralised rinse
The first rinse stops the reaction. The second uses demineralised water with conductivity below 30 µS/cm, because any salt left in the crystal becomes a blister under powder after curing. This is the cheapest stage to control and the one most often skipped when a line is busy.
Stage 7: passivation and dry-off
A final passivating rinse, chrome-free on most modern lines, closes the pore structure and delays flash rust. Dry-off has to remove water from seams and hems without over-drying the crystal, because a crystal heated too hard before powder application becomes brittle and dusts off in the booth.
Where phosphating goes wrong, and what it looks like
Four failure modes account for most coating complaints, and each has a distinct appearance.
Smut is a dark, loosely adherent residue on the surface after phosphating. It comes from a degrease stage that did not remove the oil, or from a bath with too much iron. Powder applied over smut adheres to the smut rather than to the crystal, and the coating lifts in sheets.
Coarse crystal looks like a grey, sandy surface. It comes from low titanium in the activation stage, low free acid, or a bath running too hot. Coating weight can be inside the range and adhesion still fails, because the powder bridges the gaps between large crystals instead of keying into them.
White spots after curing are usually salts from the final rinse or water trapped in a hem. They appear as small blisters, often in a line along a fold, and they grow after a humidity test rather than appearing immediately.
Edge rust on laser-cut or sheared edges is a coverage problem as much as a pretreatment problem. A sharp edge holds less phosphate and less powder, so the film thins exactly where corrosion starts. Deburring before pretreatment, or specifying a heavier film build at the edges, does more than adding another 100 hours to the salt spray callout.
Two finish checks separate a good batch from a plausible one. The first is film build, read with a magnetic gauge at the same points every time. A 35 µm reading on a folded flange can sit beside a 75 µm reading on the flat face of the same part, and only one of them is inside a nominal 60–80 µm specification. The second is adhesion, by cross-hatch on a coated panel from the same batch, not on a coupon coated separately.
Cure is the third variable and the one that gets blamed last. An under-cured powder looks correct, passes a thumbnail test and then fails adhesion after a week in service. The oven profile should be recorded per batch, and the part temperature, not the oven air temperature, is the number that matters. Heavy sections and parts with a folded hem take longer to reach cure temperature than a flat panel, so a mixed rack needs its own profile rather than a single setpoint.
The Ganesh coating route
Ganesh operates a seven-tank pretreatment line, a 16 ft × 16 ft shot blast chamber, an 18 ft × 14 ft electrostatic powder booth, a wet paint booth and a curing oven. Coating thickness is checked with a DFT gauge and adhesion with a cross-hatch test, so the two numbers that decide acceptance are measured on the finished part rather than assumed from the settings.
The shot blast chamber matters for heavier fabrications, where mill scale or weld oxide would otherwise sit under the phosphate and fail adhesion at the weld toe. For sheet metal, the laser cut edge is clean enough that blasting is usually unnecessary, and the pretreatment process explanation sets out the sequence stage by stage.
Typical coated work includes genset canopies and base frames for Mahindra Powerol, elevator components for TKE and Eros Elevators, and rack and enclosure parts. The plant runs inside ISO 9001:2015 and ISO 14001:2015, with an effluent treatment plant handling the rinse water from the line.
The paint shop capability lists the equipment and the finishes; the powder coating cost estimator shows how film build, part size and rack density change the piece cost.
What to put on the drawing
- Substrate: CRCA to IS 513, hot-rolled, or a coated grade, with the grade designation.
- Pretreatment type and coating weight range, in g/m², not a colour or a trade name.
- Powder or paint system, with the resin family where the environment demands it.
- Film build range in µm, and the points on the part where it is measured.
- Colour to a RAL or customer standard, and the gloss level.
- Adhesion test method and acceptance, agreed before the first batch.
- Salt spray hours, test method, scribe condition and pass criterion.
- Masking: threads, earth points, mating faces, and any surface that must be bare metal.
- Handling and packing, because a coated panel that rubs in transit fails the same inspection as a badly pretreated one.
The canopy specification sheet is a working example of how those fields fit together for an outdoor enclosure.
When phosphating is not the answer
Stainless steel does not need a conversion coating for appearance or corrosion, and phosphating it is a waste of a process step. Aluminium and galvanised steel need their own conversion chemistry, and running them through a ferrous phosphate bath contaminates it for every part that follows. If a drawing mixes substrates in one assembly, split the coating route before quotation.
A conversion coating is also the wrong answer where the environment calls for a barrier rather than a key. Immersion service, chemical exposure and salt-laden coastal air at C5 need a duplex system, and no coating weight on a phosphate certificate will substitute for it.
Send the drawing with the substrate, the service environment and the test method you want. The engineering team will confirm the pretreatment, the film build and the acceptance checks before the first panel reaches the line.
Frequently asked questions
Do I need zinc phosphate or is iron phosphate enough?
For an indoor enclosure in a heated building, iron phosphate at 0.2–0.6 g/m² with a polyester powder is adequate. For outdoor equipment in industrial or coastal air, use zinc phosphate at 2–4 g/m² and expect the salt spray result to improve by several hundred hours.
What coating weight should I specify on the drawing?
Specify a range, not a single number: 0.2–0.6 g/m² for iron phosphate and 1.5–4 g/m² for zinc phosphate on steel sheet. ISO 3892 gives the gravimetric method for measuring it, and a strip sample per batch is more reliable than guessing from colour.
Why does powder coating peel from a phosphated part?
Usually because the phosphate crystal is too coarse or the final rinse left salts behind. Both reduce the bond between the conversion layer and the powder, and both show up as adhesion loss at the edges after a cross-hatch test rather than as a visible defect.
Can phosphating replace a primer on outdoor steel?
No. A conversion coating is a pretreatment that improves adhesion and slows under-film corrosion; it is not a barrier coating. Outdoor steel in C3 or C4 still needs a powder or paint system with adequate film build over the phosphate.
Does phosphating work on galvanised or aluminium parts?
Not with a steel phosphate bath. Zinc and aluminium surfaces need their own conversion chemistry, and running them through a ferrous line contaminates the bath. Declare the substrate at enquiry so the pretreatment route is planned before the parts are cut.
Sources
- ISO 9717:2024 — Metallic and other inorganic coatings — Phosphate conversion coating of metals · 3 Nov 2026
- ISO 3892:2000 — Conversion coatings on metallic materials — Determination of coating mass per unit area — Gravimetric methods · 3 Nov 2026
- ISO 9227:2022 — Corrosion tests in artificial atmospheres — Salt spray tests · 3 Nov 2026
- ISO 12944-2:2017 — Corrosion protection of steel structures by protective paint systems — Classification of environments · 3 Nov 2026
Need a coating system specified for outdoor service?
Send the drawing, the service environment and the substrate. We will propose the pretreatment, the film build and the test method before the first panel is coated.
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