Deep processing: what happens after the module has been dismantled
Dismantling produces fractions. Deep processing turns those fractions into products — or into a cost. This section covers the four routes that matter
Silver in a crystalline-silicon module is not a separate component you can pick out. It is printed as a paste onto the front and rear of each cell to collect current, and it also appears in the interconnection ribbons. Fraunhofer ISE's published module composition data for a conventional module lists the silver-bearing cell fractions at around 0.03–0.05% of module mass. Everything else — the glass, the frame, the encapsulant — contains essentially none.
Two consequences follow, and they govern the whole business case. First, a whole-module feed is far too dilute for any chemical route to be economic. Second, the value is only accessible if the upstream line can produce a separated cell concentrate. If your dismantling line mixes cells into a general fines stream, that silver is gone.
The crushed cell material is contacted with an acid or alkali leach. Silver enters solution while the bulk of the silicon and glass does not.
The insoluble fraction is removed. This step decides the cleanliness of everything downstream — carry-over of solids becomes contamination in the final metal.
Silver is brought out of solution as a powder, by replacement or reduction.
The powder is filtered and washed to remove entrained impurities and residual liquor.
The washed powder is dissolved into an electrolyte and electrolysed; silver deposits on the cathode at high purity.
The refined silver is dried, melted in a crucible and cast into ingots.
Cells are separated from the rest of the dismantled material and crushed to a working particle size for the leach.
Dilute HNO₃ removes surface impurities such as silicon, aluminium and organic residue, and dissolves the silver into solution.
Sodium chloride or hydrochloric acid is added; silver comes out of solution as silver chloride (AgCl).
Iron powder is added and displaces the silver from the chloride, producing metallic silver.
The silver powder is dissolved into an electrolyte and electrolysed, depositing high-purity silver on the cathode.
The electrolytic silver is melted in a crucible, poured into moulds, cooled and taken out as ingots.
Our process documentation states a design target of silver ingots at 99.99% purity or better. That is a design specification for the process, not a measured result for your feedstock.
Achieved purity depends on the feed composition, the control of the leach and precipitation steps, the cleanliness of the separation, the quality of the electrolyte and the discipline of the operators. Any buyer relying commercially on a purity figure should require an independent assay of the actual product, and should ask what the process does with the effluent and the spent electrolyte. We say this plainly because a purity number quoted from one project is routinely repeated as though it were universal, and it is not.
Silver recovery from old modules faces a structural headwind: the industry is deliberately using less silver. Multi-busbar designs, busbar-less cells and the substitution of silver by copper or aluminium are all established reduction strategies, documented in Fraunhofer ISE's analysis of module material consumption.
The practical implication for a plant being planned today is that the modules you will process in ten years will contain less silver per watt than the ones you process now, while the modules you process now were made when loadings were higher. That argues for treating silver recovery as a route that suits the high-silver feedstock of the 2010s and for planning the plant so the silver stage can be scaled or deferred rather than assuming its economics hold forever. Our silver recovery economics page works through what has to be true for the route to pay.
That answer decides whether silver recovery is on the table at all. Tell us what your line produces and we will say plainly whether this route is worth pursuing.
Published composition data for conventional crystalline-silicon modules puts the silver-bearing cell fractions at roughly 0.03 to 0.05% of module mass — a few grams per module. It is the most valuable element by weight, but the mass is very small.
Not economically. The concentration is too low for a chemical route to work on a whole-module feed. Recovery requires a separated cell concentrate produced by the upstream dismantling and separation stages.
Our process documentation states a design target of 99.99% or better for the cast ingot. That is a design specification, not a measured result for a given feedstock. Independent assay of the actual product is the only figure worth relying on commercially.
No — it depends on it. The dismantling line is what produces the separated cell fraction the chemistry needs. Without that concentration step there is no viable feed, which is why we describe deep processing as a concentration problem before a chemistry problem.
In most jurisdictions it is effluent treatment and permitting, not the reaction equipment. Reagent handling, effluent neutralisation and the assay programme should be costed before an equipment decision is taken.
Tell us what arrives at your gate and what has to leave. The engineering team replies with the station configuration, the scope boundary and the information still missing before drawings start.
Prefer to talk first? WhatsApp +86 182 0399 3035 or email [email protected].
Three details are enough to start: what modules you receive, how fast you need to process them, and what output you have to produce.