Bright zinc plating for lines that want cyanide out of the tank. This alkaline zinc plating solution is built for plating shops that run rack work and barrel work from the same order book and want one chemistry they can hold steady. Deposits come out bright across a wide cathode current density range, so a part sitting on the high-current edge of a jig and a part tucked into the low-current centre can leave the same tank looking alike. The zinc layer distributes evenly over uneven surface areas and holds on with especially good adhesion.
The process is organised around the things that decide whether an alkaline line stays stable: controlled agitation, continuous filtration, local exhaust ventilation, nickel-coated steel anodes and carbonate management. Every one of those requirements is written out below, so a shop can walk the line and check it before the first drum goes in. That check is usually the difference between a clean changeover and a week of chasing defects when a metal plating process is moved off cyanide in a hurry.
| Parameter | Specification |
|---|---|
| Product model | Bright Zinc ZN 50 |
| Product type | Alkaline non-cyanide zinc plating process |
| Plating method | Rack plating and barrel plating |
| Key properties | Excellent metal distribution, especially good zinc-layer adhesion, and a high cathode current density range |
| Anodes | Nickel-coated steel plates |
| Heating / cooling | Steel pipes for water heating, cooling plates or heat exchanger |
| Electrolyte agitation | 1–2 turnovers per hour |
| Part agitation | 2–4 m/min |
| Barrel rotation | 3–6 rpm |
| Filtration rate | Approximately 2 bath turnovers per hour |
| Filter media | Polypropylene precoat with alkali-resistant filter aid; cellulose-containing media must not be used |
| Zinc dissolving tank | Construction and dimensioning arranged with Fengfan field technicians |
| Carbonate control | Carbonate freezing unit required to reduce carbonate content in the electrolyte |
Alkaline zinc sits behind a lot of ordinary hardware: brackets, fasteners, hinges, welded tube frames, stamped sheet parts, and cast or forged components that need a corrosion-resistant finish before painting, powder coating or assembly. Shops with a mixed order book tend to settle on it because it is a metal plating process that carries a small turned pin in a barrel and a long welded frame on a jig without a chemistry change.
It suits plants moving off cyanide, and it suits plants that have been running acid zinc plating chemicals and now need better coverage on parts with recesses, blind holes or folded edges. Acid systems are efficient and bright on flat work; the alkaline route earns its place where the shape is awkward and the deposit has to reach inside it.
Typical users are job plating shops, captive finishing lines in hardware and automotive supply, and metal plating plants that run zinc alongside nickel, copper or passivation. Large parts and low volumes point to rack work; a drum of small parts supports the barrel.
Barrel plating is the volume end of the work. Screws, nuts, washers, small stampings, pins and clips are cheaper to tumble than to jig, and the same plating process that handles a welded frame on a rack handles a full drum of them. The load makes contact through the barrel's internal contacts, the barrel turns slowly enough to keep the parts tumbling and presenting fresh surfaces, and solution exchanges through the perforations on every revolution.
What barrel work rewards is judgement about the load, not a different chemistry. Overfill the barrel and the parts nest, contact turns erratic and the deposit varies from the front of the drum to the back; underfill it and the parts rub against each other instead of tumbling. Very large flat parts, heavy components that damage each other on impact, and parts whose faces have to stay unmarked are better off on a rack — the same rule that holds for any metal plating bath, and the reason many shops keep both routes running. If you have been buying acid zinc plating chemicals for barrel work and coverage inside the load is the recurring problem, this is the route to compare against.
The figures on this product come from laboratory work and production-line practice; treat them as a starting point rather than a fixed recipe. Actual values are adjusted to the material and geometry of the parts, the application the finish has to survive, and the conditions of the plating plant. Make-up concentrations, working temperature, cathode current density and plating time are set per bath, because a drum of small washers and a jig of welded tube do not want the same window.
Send us the tank volume, the base material, whether the work runs on racks or in a barrel, the zinc thickness you have to reach and where the goods are going, and our technicians will confirm the make-up and replenishment figures for your line. After that, replenishment follows bath analysis rather than a calendar, which is how a plating solution stays inside its window instead of drifting to one edge of it. The process of electroplating zinc from an alkaline electrolyte turns on how much zinc metal and brightener are in the tank at any moment, so the analysis schedule matters as much as the first charge.
| 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; 1,000 kg/IBC drum |
| Shipping | Per the terms agreed in the current contract |
| Documentation | Inspection certificate issued after delivery, stating the batch number and warranty period |
| Safety data sheet | Ask your sales contact for the SDS covering your lot and destination |
| Sample | Ask your sales contact about sample availability for a trial on your line |
| Storage | Keep drums closed and under cover; confirm the storage range for your lot on the SDS |
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.
It is an alkaline, non-cyanide zinc plating process for rack plating and barrel plating. The deposit stays bright over a wide cathode current density range, and the bath is managed through agitation, filtration, anode selection and carbonate control rather than through cyanide.
A bright zinc deposit with even metal distribution and especially good adhesion to the steel underneath. Brightness holds across a wide current density range, so high-current edges and low-current recesses on the same load come out close to each other. Final colour and corrosion performance come from the chromate or passivate applied afterwards.
Yes. The bright zinc layer can be chromated or passivated, and it is that step which sets the colour and the corrosion performance the part finally carries. The deposit takes the film readily, so the choice of passivate chemistry is about the result you need rather than about whether the zinc will accept it.
Continuous filtration at approximately two bath turnovers per hour, using a polypropylene precoat-type filter with an alkali-resistant filter aid. Filter media containing cellulose must not be used: cellulose breaks down in an alkaline bath and puts organic breakdown products into the plating solution. Filtration is part of the plating equipment, not something added after a roughness problem has already appeared.
Carbonate accumulates in an alkaline zinc electrolyte as the bath takes up carbon dioxide and as the brightener system breaks down. As the carbonate level climbs, the working window narrows and the bath becomes harder to hold on specification. The freezing unit is there to reduce the carbonate content in the electrolyte and keep the line inside its operating range.
It can, because there is no cyanide in the formulation. Plan the changeover with our technicians rather than draining one bath and charging the other: tank lining, ventilation, agitation, filtration, anode arrangement and waste treatment all need to line up with an alkaline non-cyanide system before the first production load goes in.
Acid zinc systems are efficient and give a very bright finish on flat, simple work. The alkaline route is the one to look at when parts have recesses, blind holes, folded edges or mixed surface areas, because metal distribution and coverage into low-current areas are better. Many shops keep both and route the work by shape, which is why the decision is usually about geometry rather than about brightness alone.
In an alkaline zinc bath the zinc is not supplied by dissolving zinc anodes; it is fed from a separate dissolving compartment, and the plates hanging in the plating tank are nickel-coated steel. That arrangement keeps the zinc metal content under control independently of the anode area. Have the compartment and baskets built and dimensioned with our field technicians so the geometry suits your tank.