
A hard silver bath for contacts that have to keep working after thousands of mating cycles. The process is built on silver nitrate with three liquid components — the A and B additives and the Mu make-up — and it runs at an alkaline pH at ordinary room temperature, so an existing silver line needs no extra heating or cooling capacity to take it. What comes out is a bright to semi-bright deposit in the hard-silver hardness band, not the soft, smeary finish a decorative silver plating bath leaves behind.
We supply it to connector makers, switchgear plants and job shops that plate current-carrying parts, on rack or barrel equipment. The point of the bath is the combination: silver's conductivity and solderability with enough hardness that the contact does not gall. And because there is no free cyanide in it, the plating solution can be handled, rinsed and treated without the gas hazard and the hypochlorite detox stage that come with a cyanide silver line.
Replacing an old cyanide bath rather than installing a new one? The change is mostly cleaning: tanks, filters, pipework and racks must be free of cyanide residue before the first make-up. Anodes, rinses, anti-tarnish and drying all stay as they are.

| Parameter | Value |
|---|---|
| AgNO3 | 22–28 g/L |
| FF-7806A | 20–30 ml/L |
| FF-7806B | 15–20 ml/L |
| FF-7806Mu | 800 ml/L |
| pH | 9.0–10.0 |
| Temperature | 20–35 °C |
| Cathode current density | 0.3–1.0 A/dm² |
| Deposit hardness | 120–180 HV |
| Deposit appearance | Bright to semi-bright silver |
| Anode | Silver anodes |
| Underlayer | Silver strike or nickel barrier on diffusion-prone substrates |
| Bath analysis | Titration of silver metal and complexer concentration |
| Carbonate tolerance | Formulated to resist carbonate build-up |
Cyanide out of the building. A non-toxic organic complexer replaces the cyanide ion, which removes the gas hazard that hangs over any cyanide bath that gets acidified by mistake. Effluent treatment simplifies in the same move: rinse streams from this line carry no free cyanide, so there is no hypochlorite oxidation stage to run and no chlorinated by-product to manage.
The cost comparison is annual, not per litre. The concentrate costs more per litre than commodity cyanide salts, and that is the figure you see first. Overall running cost usually lands lower once cyanide waste treatment, the safety equipment and the regulatory fees attached to holding cyanide inventory are counted in — but your own effluent rules decide the balance, so run the comparison on your figures rather than ours.
Anodes that keep their shape. A stable complex holds the silver in solution instead of letting it immersion-plate onto the anode. Anodes last longer, the bath stays balanced, and anodes come out for inspection rather than for replacement.
Wear resistance that lets you plate thinner. Because the deposit resists abrasion, a thinner silver layer often meets the same mating-cycle target. On a precious-metal line, that is where the material saving shows up.
Tolerance to real contamination. The bath copes with the organic contamination that pushes fussier proprietary systems into repeated carbon treatment, so production hours go to production instead of to bath cleaning.
It drops into the line you already have. Rack or barrel, standard tanks, standard rectifiers. Compared with any other metal plating process you might be converting from, there is no new equipment to buy and no tank layout to redesign.
Copper and copper alloys need a diffusion barrier before the silver, because silver in direct contact with copper migrates and the joint weakens over time. Nickel plating is the usual answer: a nickel layer under the silver keeps the two metals apart and gives the silver something to bond to. Nickel substrates and nickel-plated parts only need clean activation.
Tanks are standard PP or PVC and the anodes are silver plate, so the plating solution does not call for a different tank, a new rectifier or a rebuilt busbar. Keep continuous filtration and light cathode movement running; they cost little and they even out the deposit across a mixed rack.
The compatibility point that catches people out runs the other way. If the same shop also runs cyanide chemistry, keep tanks, filters, racks and PPE separate, or clean and leach thoroughly between the two. Residues carried on a rack do more damage in a metal plating process than a bath that is slightly off specification.
Fengfan has been formulating plating chemistry in Wuhan since 1984 — more than forty years of bath development, additive synthesis and pilot plating before a product reaches a customer's tank. The silver plating chemicals we ship today are one part of a much wider range built for the same job: making a surface treatment line predictable, batch after batch.
That range covers most of a plating shop's process chain. Brightener for SZ-30B sulfate zinc plating and bright alkaline zinc for rack and barrel plating (ZN 50) sit alongside brightener for cyanide-free alkaline zinc plating ZN-500. For aluminium work there is the Phoenix EB 204A-204B divalent tin salt electrolytic colouring additive and the Phoenix Seal 149-L and 149-T middle temperature sealing agents. Copper, protection and purification are covered by FI-970 bright acid copper, FF-4219 nano-protective for wood, stone and concrete, Nickel Purify P3 for bright nickel baths, and FF-116 chrome mist inhibitor.
We are a chemistry house, not a plating shop, so we do not compete with the silver plating service providers who run our baths. Our work is bath stability, deposit consistency and the process knowledge that goes with them — including support on the line after the order, when a defect needs a cause rather than a data sheet.
Thickness is decided by current density and time, not by the drum. The plating solution supplies the silver; the layer on the part is the product of how much current you apply and how long the part stays in the bath. The 0.3–1.0 A/dm² window, together with throwing power that reaches internal threads and blind holes, covers both a light functional layer on small terminals and a heavier one on a switch contact. Send us the thickness on the drawing along with the substrate and whether you run rack or barrel, and we will come back with the current/time combination and the loading that holds it — faster than finding the number by trial on production parts.
Appearance belongs in the acceptance criteria, not in an adjective. The deposit is bright to semi-bright and stays uniform across the whole current-density window, so parts from the top and the bottom of the same rack and parts from a barrel load come out matched. Agree with your customer what "good" means before the first production lot: uniform bright silver, no bare patches, no burning at the contact points, no colour drift between batches.
Hardness has to be quoted with its measuring conditions. 120–180 HV is the band, and where a drawing calls for a microhardness figure, settle the test load, the indentation depth against the layer thickness, and which laboratory measures it. A reading taken on a thin layer with a heavy load tells you more about the substrate than about the silver.
Adhesion problems are answered before plating starts. Blistering and peeling almost always begin in activation, or in a missing nickel plating barrier on copper alloys. A bend test or a thermal cycle on a coupon that went through the same pre-treatment as production is the useful check, and it costs a fraction of a rejected lot.
Corrosion and porosity: fix the method first. Silver does not fail the way a zinc layer fails; what causes trouble is tarnish and porosity reaching down to the underplate. If a salt spray, nitric acid vapour or gel electrography clause applies, name the standard, the layer thickness and the substrate before the panels are plated, because two laboratories can disagree on the same part when the method differs. Salt-spray hours for a specific coating stack are answered against your clause by our technical team rather than published as one figure for the bath.
What you hand to your own customer. Every delivery is accompanied by an inspection certificate stating the batch number and the warranty period. If your customer's specification also names a test standard, a thickness record or a coupon result, raise it at the enquiry stage so the paperwork is arranged alongside the plating schedule instead of after the parts have shipped.
| If the job is | Choose | Reason |
| Contacts that mate, slide or vibrate in service | FF-7806 | Hard silver plating in the 120–180 HV band, so spring terminals, switchgear and slip rings resist galling and fretting where soft silver smears. |
| A non-reflective, matte silver surface | FF-7800 | Matte silver process where bath stability and easy maintenance matter more than wear resistance. |
| General bright functional silver across mixed industries | FF-7805 | Bright silver with wide coverage of appliances, instrumentation, high-voltage gear and aerospace parts. |
| Lead frames and parts carrying photoresist | FI-7802 | Weakly acidic bath with fast deposition that does not attack the resist layer. |
| A drawing that specifies soft, highly ductile silver | A soft silver bath | The hardened deposit here trades some ductility for wear resistance; do not force it onto a forming or deep-draw part. |
| Coming off a cyanide silver line | FF-7806, or the matte and bright variants above | None of these processes contains free cyanide; the changeover is a cleaning job on tank, filter, pipework and racks, not a new line. |
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. Standard PP or PVC tanks, silver anodes, your usual rectifiers and the existing rack or barrel equipment all stay as they are — there is no new equipment setup to install. The one extra job is tank preparation: a tank that previously held a cyanide silver solution has to be cleaned and leached before make-up, otherwise the first bath will not behave and nothing else you change will fix it.
This is a hard silver, not a decorative one: the deposit measures 120–180 HV depending on current density and bath condition, against the much softer finish a conventional bright silver bath gives. In practice that is what lets a terminal survive thousands of mating cycles without galling, and it is why a thinner layer often meets the same wear target — which is where the saving on a precious-metal line comes from.
On copper and copper alloys, yes. A nickel plating barrier or a compatible copper strike goes on first to stop copper migrating into the silver, then the part is activated and struck before the main bath. On nickel and nickel-plated substrates, clean activation is enough — a full barrier layer is not required.
Job shops are a good fit. The operating window is wide enough to plate mixed work — large busbars on a rack, small fasteners in a barrel — and the bath tolerates the organic contamination that varied jobs bring in better than a fussier proprietary system. Running a silver plating service also stops being a liability question, because there is no cyanide inventory to hold, secure or report.
Deposit thickness is set by current density and plating time rather than by the bath, so tell us the target thickness, the substrate and the finish your customer specifies and we will come back with the running conditions and the current data for that combination. If a salt-spray or porosity clause applies, send it over — agreeing the test method before the first panel is far cheaper than arguing about it afterwards.