Zinc-nickel plating carries the corrosion protection on a part; the passivate decides how much of that protection survives the first winter, the first wash line and the first handling cycle. TR-393 is the immersion stage that closes the gap — a trivalent chromium passivate formulated for zinc-nickel alloy deposits, forming a tight, uniform and transparent film in natural colour over the plated surface.
Because the film is clear, the part keeps the colour of the deposit underneath. It reads as a natural metal finish rather than a dyed or iridescent one, which suits work where the zinc-nickel layer is the finish the customer actually sees: fasteners, brackets, fittings and hardware that get handled, packed and shipped without a topcoat over them.
Running it takes a temperature-controlled immersion tank and a rinse after it, nothing more specialised than that. The working solution is long-lived and simple to maintain, with the parameters adjusted as the bath ages rather than fixed for the life of the tank. In a metal plating process, this is the stage that decides whether a part still looks and performs like new a year outdoors. Construction projects lean on anodized metal for both durability and appearance. Aluminium anodizing is popular for architectural work because it gives a clean finish that stands up to weathering, while alodine coating prepares surfaces for painting so the coating adheres better and lasts longer. Working with an experienced plating partner lets construction firms specify materials that are expected to meet project and building standards, which protects value and client trust over the life of the build.

| Parameter | Optimal condition | Operating range |
|---|---|---|
| Passivate concentration | 70 ml/L | 50–100 ml/L |
| pH | 3.5 | 3.5–4.0 |
| Immersion time | 40 seconds | 30–60 seconds |
| Bath temperature | 30 °C | 25–40 °C |
| Deposit | Zinc-nickel alloy | — |
| Working solution | Long service life, with parameters adjusted as the bath ages | — |
Trivalent chromium only. The passivate is built on trivalent chromium and contains no hexavalent chromium. That is the question a zinc nickel plating company is asked most often by its own customers, and here the answer sits in the chemistry: what goes into the tank is trivalent.
What it changes on the shop floor. Hexavalent passivation brings its own handling regime and its own waste-treatment route with it. Moving the passivation stage of the process of electroplating onto a trivalent product takes that hazard out of the daily running of the line, and the rinse water leaving the tank follows the acidic rinse route rather than a hexavalent reduction step. Have your EHS team confirm local discharge limits for the chemistry before the change-over — those limits are site-specific and cannot be set from a product sheet.
Handling the working solution. At a working pH around 3.5 the bath is acidic, so gloves, eye protection and ordinary acid-handling practice apply when making up, analysing and topping up. Ask your sales contact for the current safety data sheet for the batch you receive and keep it with the line documentation.
The rinse after the passivate. Because the chemistry is trivalent, that rinse carries trivalent chromium rather than hexavalent. If the plant still runs both chemistries, keep the two rinse streams apart so the waste routes stay the way your EHS team planned them.
Storage. Keep containers closed and upright in a cool, dry, ventilated place, out of direct sun and away from heat sources. Bunded storage is worth arranging wherever acidic plating solutions are kept on site.

| Term | What applies |
| Payment | 100% T/T in advance |
| Minimum order quantity | Varies by chemical; confirmed with our sales team per order |
| Lead time | 2 weeks |
| Packing | 10 kg/box; 25 kg or 50 kg/bag; 20 kg/25 kg/30 kg/200 kg/drum; 1000 kg/IBC drum |
| Shipping | Per the terms agreed in the current contract |
| Documents | Inspection certificate issued after delivery stating the batch number and warranty period |
| Quantity and pricing | Quoted per enquiry for the grade and pack size you need |
Colour comes from the deposit.
The film is clear and transparent, in a natural colour, with no dye and no iridescent tint of its own. The part therefore keeps the colour of the zinc-nickel plating underneath: a bright deposit reads bright, a matte or barrel-finished surface reads matte, and a batch that looks uneven is usually showing unevenness in the deposit and the gloss stage rather than in the passivate.
A heavy film reads slightly warmer.
Concentration, pH, immersion time and bath temperature decide how much film forms. Run heavy and the shade drifts a little warmer and yellower; run lean and it stays cooler and more silver. Both sit inside what buyers accept as natural colour, but once a shade has been approved, hold the bath at one point in the working window and check the first parts of every shift against the approved sample.
Thickness follows the reaction, not a dial.
The layer forms by converting the alloy surface rather than building up on top of it, so its thickness follows concentration, time and temperature instead of being set to a figure. Where a drawing or an end customer calls out a film weight or thickness, send that call-out with your enquiry: we will confirm what can be measured and reported for the batch you receive, rather than quote a number measured on someone else's part.
Sealing deepens the look.
Where a sealer follows the passivate it adds gloss and can deepen the shade a little. Judge colour after the full sequence — deposit, gloss dip, passivate, seal — because that combined finish is what the customer opens the box to.
Which deposits it accepts.
TR-393 is formulated for zinc-nickel alloy deposits from both alkaline and acid zinc-nickel baths. Plain zinc is a different substrate and the range holds separate products for it. If you are not certain what your line lays down — the nickel share in particular — send a plated sample with the enquiry and the fit can be confirmed before a tank is made up.
| What the figure must state | Why it changes the answer |
| Test method and conditions | Hours mean little without a named method. Neutral salt spray to ASTM B117 — 5% sodium chloride fog at 35 °C — is the usual reference; a result run to a different standard is a different test. |
| Zinc-nickel thickness beneath the film | A passivate slows attack on the deposit; it cannot outlast the deposit it sits on. Any figure is only transferable when the thickness is quoted alongside it. |
| Sealed or unsealed | Sealing is a separate stage and moves time to first corrosion considerably. Sealed and unsealed results are not interchangeable, so the figure has to say which one it is. |
| Time to white rust | The first visible corrosion product is white and comes from the zinc-nickel layer itself. Most acceptance criteria on passivated work are written against this point. |
| Time to red rust | Base-steel corrosion, the end of the protection. In a metal plating process both points are recorded, never compressed into one number. |
| Part, position and finish | Edges, thread roots and cut faces corrode first, so a flat test panel will always outlast a real bracket. Ask which part the figure refers to and test against that part where the specification allows. |
| The report handed over | Batch number, test date, conditions and result. Ask for the report matching the batch you receive and file it alongside the documents supplied for the batch, so plating solutions supplied later can be checked against the same baseline. |
Fengfan's zinc nickel plating is built for parts that have to keep working in demanding conditions. The coating resists corrosion and wear, which makes it a practical choice for industries that cannot afford early failures. Electroless nickel plating adds a uniform layer across complex geometry, so recessed areas and edges receive the same protection as flat surfaces. That consistency extends the working life of components, reduces maintenance costs and gives buyers confidence in long-term performance.
Innovation at Fengfan centres on how the plating process is controlled, not just on the metal being deposited. Electroplating techniques and alodine coating are tuned to improve surface finish and durability, while anodizing aluminum and aluminium anodizing are used where a harder, more uniform oxide layer is needed. Each process is matched to the part's base material and its end use, so the finish supports the job it has to do. Share your drawing, base material and required finish with our team so the right process and tolerance can be confirmed before production.
Choosing the right match is where most sourcing decisions stall. As a trading supplier, we keep one point of contact from first enquiry to after-sales: tell us what you are making and the conditions you work under, and we shortlist the closest matches from our supplier network, compare specifications and arrange samples before you commit to a bulk order. If something does not behave as expected, we work with the supplying partner on the cause and a practical fix, and stay with the case until it is settled. Email, WeChat or WhatsApp enquiries get a reply within 24 hours.
No. It is built for deposits produced by zinc nickel plating, and a plain zinc layer reacts differently in the bath — running zinc parts through it will not give the film the product is specified for. If you run both lines, tell us what your zinc line produces and we will point you to the grade that matches it, rather than have you test the wrong one.
The aluminium product is a trivalent chromium passivate for aluminium alloys, used before coating or for corrosion protection on aluminium parts. This one works on electroplated zinc-nickel over steel. They are not interchangeable and no amount of parameter tuning will make one do the other's job, because the substrate decides which chemistry works. The range holds different plating solutions for exactly that reason: tell us the base material first and the finish second.
In practice it is nearly always one of four things: concentration or pH has drifted outside the working window, the rinse before the passivate is carrying plating bath in, parts are touching in the barrel so the solution cannot reach every surface, or the dwell is too short for the geometry. Work through them in that order — bath figures, then rinse, then loading — and the cause usually reproduces on the same parts, which makes it easy to confirm before you change anything.
Yes — the cold end of the window is a working condition, not a tolerance. Running cool generally means allowing a little more immersion time to build the same film, and it suits plants that cannot heat a tank or that lose heat overnight. What you should avoid is running cold and short at the same time; that combination is how thin, uneven films happen. Once you settle on a combination, keep it fixed and write it into the shift log.
No — sealing and passivation do different jobs. The passivate converts the zinc-nickel surface; a sealer closes what is left of it and is where a good part of the corrosion performance comes from on parts that face real weather. Whether you need one depends on the environment and on the test your customer specifies. If you do seal, choose the sealer with the passivate in mind rather than adding whatever is already on the shelf.
For shells, cans, housings and frames the film does its job without changing how the part assembles. Where the drawing sets a contact-resistance or solderability figure, send that call-out with your enquiry: the passivate stage itself does not change, but the acceptance test you sign off on does — and that is better agreed before the first batch than argued about after it.