ZN-265 is a concentrated brightener for cyanide-free alkaline zinc plating, built from a blend of polyamine compounds rather than a single salt. Dosed into a zincate bath, it produces a smooth, bright, fine-grained zinc layer on steel parts, and it is designed to take the place of a conventional cyanide zinc system outright rather than to top one up.
The concentrate carries no free cyanide. That changes what the line has to manage day to day: the bath stays alkaline throughout, waste treatment is no longer built around cyanide destruction, and the chemistry behaves predictably across a broad zinc metal span — an important quality when the same tank plates a different workload every week.
We supply it as three liquids: a brightener, an additive and a purifier. Splitting the system that way lets a bath be corrected one variable at a time instead of through a single blended product. It sits in our range of electroplating chemicals for lines that zinc plate steel parts in alkaline media, and it is worked on both rack and barrel equipment.
The sections below set out the working ranges, how a bath is charged and kept in condition, where the product earns its place on a line, and how it behaves when a tank is dirty or when parts go on to passivation and sealing.
| Parameter | Working range |
|---|---|
| ZnO (g/L) | 10~20 (optimum 15 g/L) |
| NaOH (g/L) | 100~140 (optimum 130 g/L) |
| ZN-265A brightener (mL/L) | 10–14 |
| ZN-265B additive (mL/L) | 0.5–2 |
| ZN-265C purifier (mL/L) | 2–4 |
| ZN-265A brightener consumption (mL/KAH) | 80~180 |
| ZN-265B additive consumption (mL/KAH) | 30~80 |
| ZN-265C purifier addition | Usually not required; add when impurity content is high or when sodium hydroxide is added |
| Zinc metal content (g/L) | 5.5~18.5 |
| Bath temperature | 5~52 °C |
| Anode | 0# zinc plate |
| Anode to cathode area ratio | 1:1.5~2 |
| Cathode current density, rack and barrel (A/dm²) | 0.5~8 |
The bath chemistry does not change between a rack line and a barrel line; what changes is the way the parts meet the solution.
On a rack, cathode movement of 8 to 12 cycles per minute keeps fresh solution at the part face and evens out the boundary layer. Without that movement the low-current side of a complex part can lose brightness even when the analysis is perfect. Jig contact deserves as much attention as the chemistry: one weak contact point will show as a dull patch that no brightener addition will fix, so check the rack before touching the bath.
In a barrel, rotation of 6 to 8 revolutions per minute is the working range. Overfilled barrels plate slowly and unevenly, because parts shield one another and the solution cannot exchange inside the mass. Load within the barrel's normal working volume and leave small parts enough room to tumble past the contacts.
The current density window runs from 0.5 to 8 A/dm², which covers light decorative work and heavier functional deposits on the same bath. If you are working towards the top of that window for thickness, confirm the dwell with us first — long holds at high current build a coarser layer that brightener cannot smooth afterwards.
Keep the bath filtered and the anode bags clean. Sludge on the anode alters current distribution long before it shows up in the analysis, and it is one of the commonest reasons an electroplating line blames the brightener for a problem that sits in the tank. Because the chemistry is unchanged between the two setups, a job can move from rack to barrel without rebuilding the plating process around it.
Alkaline zinc baths accumulate contaminants: calcium and magnesium carried in with the work and the water, iron from parts that were not fully pickled, lead, cadmium and chromium from scrap or from upstream operations. In industrial electroplating that build-up is normal; what matters is how the brightener behaves once it happens. This one keeps producing a bright, coherent layer past the point where a less tolerant product starts to grey out, and the deposit still takes a passivation film.
Watch for the usual signals: a bath that turns hazy, brightness that drops first in the low-current areas, a passivation film that comes out dark or patchy, or fine spots on barrel work. Those are impurity symptoms rather than brightener symptoms, and adding more brightener makes them worse and costs more.
The purifier is the answer to that, and it is deliberately the component you reach for least. It is normally left out of a new bath; dose it when incoming work is known to be dirty or after a sodium hydroxide addition, which is when contaminant levels tend to step up. Because it is a separate liquid, the bath can be treated without touching the brightener or additive levels.
Passivation is where a good zinc layer proves itself. The deposit accepts the common post-treatments — blue-white, colour and the rest — and holds an even appearance through them, so a line does not have to choose between a bright as-plated finish and a passivation that actually performs. Where parts are sealed after passivation, the film sits on a coherent zinc layer rather than a patchy one, and that is where corrosion performance is won or lost.
| Term | Details |
| 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 |
| Batch documentation and warranty | Inspection certificate issued after delivery stating the batch number and warranty period |
Ductility is decided at the bend, not in the tank. A bracket bent to fit after plating, a terminal crimped onto a cable, a fastener staked into a housing, a tube end flared — each of those pulls the zinc layer across a fold, and a stressed deposit opens up there as fine crazing or flakes away along the line of the bend. Nothing shows in the plating record; the reject surfaces at assembly.
What the chemistry contributes
ZN-265 is built on polyamine compounds and lays down a smooth, bright, fine-grained and flexible zinc layer in the alkaline bath. That ductility belongs to the deposit itself rather than to a film applied over it, so it carries through the forming step as long as the layer has been run inside its working window. It is one reason this brightener suits industrial electroplating work on parts that are still going to be shaped after they leave the line.
Keeping the deposit ductile
- Do not chase gloss by over-dosing. Brightness comes from holding ZN-265A within its 10–14 mL/L charge and topping up against the 80~180 mL/KAH consumption figure. Extra brightener pushed in to lift a dull bath builds internal stress into the deposit, and a stressed layer is exactly what cracks at a fold. - Watch thickness and current density together. The 0.5–8 A/dm² window covers decorative and functional work, but long dwells near the top of it build a coarser, harder layer. Where a part needs a heavy deposit and is formed afterwards, confirm the dwell with us before the run. - Hold the bath inside its temperature range. Brightness is retained up to 48 °C and the bath runs to 52 °C, but a tank that drifts warm while the brightener is also being pushed is where ductility is most often lost. - Treat contamination early. Iron, lead and calcium raise deposit stress and dull the finish at the same time. The purifier is the corrective, dosed when the analysis or a run of dirty work calls for it, and correcting early costs far less than correcting after a batch of bent parts has failed.
Telling a ductility problem from an adhesion problem
Both look like flaking and they are fixed in different places. If the layer peels back cleanly to bare steel in sheets, the fault is usually pretreatment — oil, scale or a smut film left on the part — and no change in the brightener will help. If the coating crazes into a network of fine cracks across the bend while staying bonded, the deposit itself is too stressed, and the bath rather than the cleaning line is where to look. Plate a coupon, bend it and inspect the fold before committing a production load.
Forming before or after passivation
Where the sequence allows it, form the part before passivation. A trivalent passivation film is thin and does not stretch with the zinc beneath it, so bending a passivated part cracks the film on the outside of the bend and leaves that strip unprotected in salt spray even though the zinc itself is sound. If the order cannot be changed, keep the bend radius generous and consider a sealant from the same plating chemicals range to close the film again.
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.
Yes — it is formulated as a full replacement rather than a partial substitute. The bath runs alkaline with no free cyanide to add or destroy, and it still produces the bright zinc layer with the throwing power that cyanide systems were valued for. In most shops the tank, rectifier, jigs and passivation sequence stay exactly as they are; what changes is the bath chemistry and the waste treatment behind it.
The bath is built on zinc oxide and sodium hydroxide, with the brightener, the additive and the purifier added on top. The specification table above gives every working range, the consumption rates and the temperature window. In practice the three components are charged separately and topped up against ampere-hour consumption rather than by eye — the habit that keeps electroplating chemicals in a bath balanced over months instead of days.
Yes. A rack line runs with cathode movement, a barrel line with rotation, and the brightener delivers the same brightness and coverage across both. The chemistry is identical on the two; only the way the parts are held changes, so a job can move between them without rebuilding the plating process. Watch the low-current areas when you switch a part from one to the other, and plate a panel on the new setup before releasing a production load.
The brightener tolerates the contaminants an alkaline zinc bath normally collects — calcium, magnesium, iron, lead, cadmium and chromium — and keeps its brightness further into a dirty bath than a narrow-spectrum product would. When contamination does start to show, the purifier is the correction, and it can be dosed without disturbing the brightener level. On the finish side, the deposit accepts the usual passivation treatments and holds an even appearance through them, so parts can carry a decorative top coat as well as the corrosion protection.
Smooth, bright and fine-grained, with a sheen rather than a mirror polish before passivation. Colour is not present at this stage; the final colour comes from the passivation step, which is why as-plated brightness matters: a uniform base is what makes a blue-white or colour film come out even.
It is built for standard alkaline zinc equipment: a lined steel tank, a 0# zinc anode, filtration and either cathode movement or barrel rotation. Nothing exotic needs installing. Send us the tank volume, the anode arrangement and the parts you plate, and we will confirm the charge figures and flag anything in the setup that would limit the result — anode area ratio is the usual one, and it matters across industrial metal plating regardless of whose brightener is in the tank. Most industrial electroplating lines keep their rectifier, jigs and passivation sequence untouched.
The brightener does the main work of brightness and throwing power and is the component you top up most often. The additive is charged at a much smaller volume and is the fine adjustment. The purifier is corrective only: it normally stays out of the bath and goes in when contamination is high or right after a sodium hydroxide addition. Keeping the three as separate plating chemicals is what makes a metal plating process diagnosable — when something changes, you know which lever you pulled.