We provide complete turnkey solutions for precious metal refining system.

Gold Refining Process

— Turnkey Gold Refining Process

The Gold Refining Process is a turnkey gold refinery line that carries crude gold, doré, karat scrap, anode slime and e-waste concentrate through granulation, nitric acid pre-treatment, aqua regia dissolution, selective reduction, anode casting, high-current-density electrolysis and vacuum ingot casting to Au99.99 (Grade I) gold ingots, or 99.999% by secondary electrolysis. Electrolysis runs at up to 1,000 A/m² — three times a conventional Wohlwill cell — on a 10–20 hour cycle, with refining loss below 0.02% and only 0.15 kg of gold locked up per litre of electrolyte, half a conventional circuit. A DC supply with superimposed AC breaks the silver chloride film that passivates the gold anode, so the anode dissolves completely and silver is recovered from the anode bag. Acid mist and NOₓ from dissolution and electrolysis are absorbed at 99.5% or better, taking an inlet above 30,000 mg/m³ below 150 mg/m³. 

Product Overview

A gold refining process is the sequence of chemical and electrochemical operations that takes gold which is impure but concentrated — a doré bar, a batch of 22K scrap, a filtered gold sponge, or the gold fraction of an anode slime — and raises it to a fineness that can be traded as investment-grade metal. In plant terms it is the refining half of a gold refinery plant: dissolution and reduction vessels, gold electrolysis equipment, the gold refining machine units that melt, granulate and cast the product, and the scrubber train that keeps the whole circuit legal. Specified as one supply, those units make up a single gold refining system engineered around one feed material and one required daily output. It is not smelting, and it is not melting. Smelting separates gold from ore and from gangue at temperatures above 1,000 °C and produces doré at roughly 90–95% gold; melting simply liquefies metal without changing its composition. Refining is the controlled part: gold is either dissolved into solution and chemically brought back as metal, or dissolved anodically and re-deposited cathodically in an electrolytic cell. The target is an internationally recognised fineness — for investment and central-bank trade this is 99.99% (Au99.99), and for premium or high-reliability industrial applications 99.999%.

The line described on this page is the complete refining circuit of a gold works, arranged in the order the chemistry demands. Feed arrives and is assayed and granulated, because a refining reaction runs at the speed of its surface area: a melt that has been poured into water to form shot dissolves in a few hours where the same weight of bar would take days. High-silver feed is then pre-treated with nitric acid, which removes silver and base metals ahead of the refining step instead of letting silver chloride form inside the dissolving vessel or the electrolytic cell. The prepared feed is attacked with aqua regia — one part concentrated nitric acid to three parts concentrated hydrochloric acid — which converts gold to chloroauric acid (HAuCl₄); the reaction is run hot, the vapour is condensed and returned, and the solution is cooled, filtered and clarified. Silver and any insoluble fraction stay behind as a chloride residue and are filtered off as a by-product. Gold is then brought back out of solution as metal by selective reduction with oxalic acid, sodium metabisulfite or ferrous sulfate at controlled temperature, pH and dosing rate, producing sponge gold or a fine gold powder that is washed, acid-scrubbed, washed again to neutral and dried.

Sponge gold is not yet 99.99%. The step that reaches investment grade is electrolysis. The dried gold is melted and cast into anode plates, which are suspended in an electrolyte of gold chloride in free hydrochloric acid at 60–70 °C against cathode starter sheets of pure titanium or fine gold. Under current, gold dissolves from the anode as Au³⁺ and plates out on the cathode as coarse crystalline gold of very high purity, while base metals stay in solution and insoluble impurities drop as anode slime into the anode bag. The two process problems that decide whether a gold electrolytic refinery performs are silver and copper. Silver above roughly 6% in the anode forms a silver chloride film that passivates the plate and stops the reaction; the line answers this with a DC supply with superimposed AC, which is an asymmetric pulsed current that breaks the silver chloride layer off the anode as it forms, so the plate dissolves evenly and completely and the silver is recovered from the anode bag. Copper above roughly 2% in the anode co-deposits at the cathode and contaminates the product, which is why copper is removed in pre-treatment and why the electrolyte is monitored, polished and periodically bled. The cathode gold is harvested, washed to remove occluded electrolyte, dried and melted and cast into ingots — under vacuum and inert gas where the customer requires porosity-free, ripple-free bars to an LBMA-approved trading specification.

The reason a gold refinery is bought as an engineered line rather than assembled from vessels is that dissolving gold generates the most aggressive off-gas in precious-metal processing. Aqua regia evolution, electrolysis at 60–70 °C and anode melting all release acid mist, chlorine, nitrosyl chloride and nitrogen oxides, and every one of those streams carries metal. Vapour above a dissolving reactor is therefore condensed and returned to the reactor, not vented; the enclosed hood keeps the operator out of the plume; the residual NOₓ is absorbed in a multi-stage train — two-stage bubble absorption, four-stage jet absorption and a final two-stage alkaline spray — at 99.5% or better absorption, which takes an inlet of 20,000 ppm down below 150 ppm and has been measured in service at 80 mg/m³ against a 100 mg/m³ regulatory limit; and the acid effluent is neutralised in an agitated PPH neutralisation tank before discharge or recycling, with washing water cross-reused inside the circuit so that the plant approaches closed-loop operation rather than merely compliant disposal.

What the operator ends up with is a compact, cyanide-free refining circuit — aqua regia, chloride, oxalic acid, sodium metabisulfite, hydrochloric acid and nitrite-free reduction chemistry, with no cyanide anywhere in the refining route — that runs on a 10–20 hour electrolysis cycle, locks up roughly 0.15 kg of gold per litre of electrolyte, consumes about 150 litres of hydrochloric acid per tonne of gold in the electrolytic step, and returns chemistry the operator can verify: Au99.99 (Grade I) on the Shanghai Gold Exchange standard, or 99.999% by a second pass through the same cell. Wetted parts are selected against the duty from high-performance polypropylene with anti-ageing additives, PPH structural framing, titanium, glass and titanium-clad copper; every vessel, filter, tank and duct can be built to the layout of an existing refinery building or supplied as a containerised line for a greenfield site.

Application Scenarios

A gold refining process line is specified wherever gold arrives in a form that is rich but not yet tradable, and where the operator wants to own the final step — the step that converts metal at a discount into metal at the market price — instead of paying a third-party refiner’s deduction. The following are the situations in which this line is installed.

  • In-house refineries for jewellery manufacturers and goldsmiths — refine workshop scrap, sprues, filings, polishing dust, sweeps and old gold taken in part-exchange, and put the metal straight back into production as certified fine gold. Output: Au99.99 ingots, granules or granulate for alloying.
  • Karat gold and old-jewellery processors — take 18K, 22K, dental gold, watch cases and mixed karat scrap through pre-treatment, dissolution and electrolysis in one line rather than in separate chemical batches. Output: Au99.99 with the silver fraction recovered as silver chloride.
  • Precious-metal recyclers and urban-mining operators — finish the gold fraction produced by e-waste, PCB and plating-sludge recovery circuits into saleable fine gold on the same site. Output: Au99.99 ingots plus gold granules.
  • Gold mines, doré smelters and mine-site refineries — refine gravity concentrate, doré bullion and electrowinning cathode from cyanidation or gravity circuits into market metal, shortening the chain from mine to bank. Output: Au99.99 bars to a trading specification.
  • Copper and nickel electrorefineries — treat the gold fraction of anode slime, where gold arrives as a rich but contaminated residue after silver removal. Output: fine gold ingots with the silver and PGM fractions routed onward.
  • E-waste and PCB recycling plants — refine the gold-bearing concentrate, gold powder or gold alloy produced by mechanical and hydrometallurgical front ends. Output: Au99.99 in a cyanide-free refining circuit.
  • Mints, assay houses and trading houses — convert returned, off-spec, contaminated or mixed gold material back to assay-certified metal with full batch traceability. Output: certified ingots with a Certificate of Analysis per batch.
  • Banks, pawn networks and bullion dealers — bring melting and refining in-house so that bought-in scrap is settled against a documented assay rather than an external refinery’s deduction. Output: standard-weight fine gold bars.
  • Industrial and electronics manufacturers — recover gold from rejected plating lines, sputtering targets, bond wire, contact scrap and process residue, and close the loop back into the plating bath. Output: fine gold for anode or target manufacture.
  • Dental laboratories and medical device makers — refine crown, bridge and alloy scrap, crucible residue and bench sweeps in-house. Output: high-fineness gold for alloy make-up.
  • Hydrometallurgical plants and precious-metal works — add a dedicated gold finishing circuit behind a leaching, solvent-extraction or ion-exchange train. Output: fine gold plus a bleed stream routed to the PGM circuit.
  • Greenfield refinery projects and national precious-metal programmes — build domestic refining capacity with a single supplier for dissolution, electrolysis, casting and emissions control. Output: a standalone gold refinery with auditable metal balance.
  • Pilot, laboratory and teaching facilities — small-batch refining and process development on the same flow sheet as a production refinery. Output: analytical-grade fine gold for development work.

Applicable Raw Materials

Feed selection is set by the chemistry, and the first question on any gold refining project is which route a given material belongs to. Material assaying roughly 75% gold or above with silver below about 8% can go straight through aqua regia dissolution and chemical reduction; material assaying roughly 90–95% gold or above, with silver below about 6% and copper below about 2%, can be cast into anodes and taken to 99.99% by electrolysis in a single pass; anything leaner, dirtier or richer in silver is given a pre-treatment or a first-pass chemical upgrade on the same line. In every case the feed is assayed, granulated and blended first, because the process runs on surface area and on a representative sample. Each raw material below is listed with the treatment it receives and the product it yields.

  • Crude gold and doré bars — the doré bullion produced by mine smelting, at roughly 80–95% gold with silver, copper and iron as the balance; melted, granulated and, where the silver content is low enough, cast directly into anodes for electrolysis. Output: Au99.99 ingots, with silver chloride recovered from the anode bag.
  • Karat gold scrap and alloy jewellery — 18K, 22K and dental gold alloys with silver, copper, nickel and zinc as the alloying elements; granulated, pre-treated with nitric acid to strip silver and base metals, then dissolved in aqua regia. Output: Au99.99 fine gold plus a silver by-product.
  • Gold-bearing polishing dust, sweeps and filings — bench sweeps, floor residue, filter bags and jar dust from jewellery manufacture; incinerated or roasted to burn off organics, milled, blended and assayed before dissolution. Output: fine gold with the ash residue assayed for recovery losses.
  • Aqua regia gold sponge and reduced gold powder — the intermediate gold produced by a chemical refining stage elsewhere or in the first pass of this line; dried, melted and cast into anodes for the electrolytic step. Output: electrolytic gold at 99.99% or, on a second pass, 99.999%.
  • Silver- and gold-bearing anode slime — copper, nickel, lead and zinc electrorefinery slime after the silver and base metals have been removed; melted with flux and oxidising agents to remove the remaining base metals and cast into anodes. Output: fine gold ingots with a PGM-bearing residue routed onward.
  • Gold concentrate and precipitate from e-waste and PCB circuits — gold powder, cemented gold, gold-bearing resin eluate residue and the gold alloy recovered by mechanical or hydrometallurgical front ends; dissolved, reduced and then electrolysed. Output: Au99.99 in a cyanide-free refining circuit.
  • Cyanidation gold precipitate and zinc-box sludge — gold precipitated on zinc from a leach circuit, and the cleaned-up slimes from a cyanide plant, where the gold content supports an economic refining pass. Output: fine gold ingots, with the cyanide-bearing wash effluent neutralised on site.
  • Spent gold plating, stripping and drag-out solutions — gold-bearing electroplating baths, strip liquors, spent ion-exchange resin and gold-loaded activated carbon; eluted, reduced and refined on the same line. Output: fine gold recovered from low-concentration liquors.
  • Gold-bearing electronic and industrial scrap fractions — connector and contact scrap, bond wire, rejected targets, printed-circuit fractions and components too rich to be sold as mixed scrap; pre-processed to a gold concentrate and then refined. Output: Au99.99 and a separately routed palladium and silver fraction.
  • Gold residues, slags, crucible scale and refractory waste — melting-scale residue, crucible and mould scale, floor sweepings from melting rooms and refractory material that has absorbed gold; milled, upgraded by melting with flux and oxidant, then refined. Output: recovered fine gold from material usually written off as waste.
  • High-silver gold alloys and mixed gold-silver bullion — alloy above the silver tolerance for direct electrolysis; taken through nitric acid pre-treatment, or routed first to a silver electrolytic circuit where the silver content is the larger value. Output: fine gold plus silver at 99.95% or better.
  • Gold-bearing effluent, filter cake and neutralisation sludge — sludges and cakes from effluent treatment and scrubber blowdown in precious-metal works; milled, blended and assayed as a secondary feed. Output: fine gold with the barren residue assayed and disposed of against local limits.

Output Products

Every consignment leaves the line against a Certificate of Analysis produced by fire assay with ICP-OES confirmation, and each product is packed in the form its buyer wants — ingot, granule, granulate or powder. Fineness is reported as parts per thousand against an internationally recognised standard.

  • Au99.99 (Grade I) gold ingots — electrolytic cathode gold melted and cast to the Shanghai Gold Exchange Au99.99 (Grade I) standard gold ingot specification, in weights and dimensions agreed with the buyer. Output: 99.99% gold ingots, assay-certified per batch.
  • 99.999% fine gold — where the buyer’s end use requires five-nines metal, the cathode gold is recast and passed a second time through the same electrolytic cell. Output: 99.999% gold ingots or granules.
  • LBMA-specification cast bars — vacuum and inert-gas casting to any LBMA-approved trading specification the customer requires, delivered without porosity, shrinkage cavities or surface ripple. Output: cast bars to a nominated trading specification.
  • Investment-grade gold granules and granulate — gold melted and granulated rather than cast where the buyer needs a free-flowing, easily weighed and easily redissolved form. Output: gold granules of controlled size distribution for alloying or plating.
  • Gold in sponge and powder form — the reduced gold intermediate, washed to neutral and dried, supplied where the customer routes it to powder metallurgy, catalyst preparation or a plating bath rather than to a bar. Output: sponge gold and fine gold powder at 99.9% and above.
  • Silver chloride and recovered silver — the silver chloride recovered from the anode bag and from nitric acid pre-treatment, reduced and melted to silver metal; where a silver electrolytic circuit is added, refined further. Output: silver metal at 99.95% and above, or silver chloride for onward sale.
  • PGM-bearing anode slime and residue — the insoluble fraction of the anode and the electrolyte bleed, which concentrates platinum, palladium and rhodium. Output: a PGM-bearing residue routed to a platinum-group-metal refining circuit.
  • Spent electrolyte and recovered gold from electrolyte bleed — electrolyte removed from the circuit when impurity levels rise, with the contained gold recovered by reduction before the liquor goes to effluent treatment. Output: recovered gold plus a treated chloride liquor.
  • Treated off-gas and neutralised effluent — acid fume and nitrogen oxides absorbed in the scrubber train and the acid effluent neutralised, so that both streams leave the plant within local emission and discharge limits. Output: compliant stack emission and neutralised effluent for discharge or reuse.
  • Batch documentation and metal balance — an assay certificate, a batch record of feed weight, product weight, residues and losses, and a full parameter log from the PLC. Output: an auditable batch file for every refining lot.

Gold Refining Process Flow

The gold refining process runs in ten stages, arranged in the order the chemistry requires: the feed is characterised and given surface area, silver and base metals are taken out ahead of the refining step, gold is dissolved and brought back as metal, that metal is cast into anodes and electrolysed to investment grade, and the gas, effluent and residue streams produced along the way are treated in the same package. Steps 1 to 4 form the chemical route, which is the flexible half of the line and accepts the widest range of feed; steps 5 to 8 form the electrolytic route, which is the half that delivers 99.99% and, on a second pass, 99.999%. Steps 9 and 10 recover the value that would otherwise leave as slime, bleed liquor or stack emission.

Gold Refining Process
Gold Refining Process Flow

Steps 1 — Feed Assay and Granulation. Feed is weighed, sampled and assayed by fire assay with ICP-OES confirmation so that the route, the reagent charge and the expected recovery are set before any gold is dissolved rather than after. The batch is then granulated — melted and poured into water to form shot, or granulated directly from the melting furnace — because dissolution rate is governed by surface area, and a granulated batch dissolves in hours where the same weight of solid bar would take days. The assayed, homogenised and granulated lot is the unit of production for everything that follows. Output: an assayed, granulated feed lot with a recorded starting weight and fineness.

Steps 2 — Nitric Acid Pre-Treatment and Silver Removal. Silver is the impurity that decides whether a gold refining process runs smoothly, because it forms insoluble silver chloride that coats both the dissolving gold and the anode plate. High-silver feed is therefore pre-treated with nitric acid, which dissolves silver, copper, nickel, zinc and other base metals and leaves the gold as a residue; the silver is recovered from the nitrate solution, and the gold residue is washed to neutral before the next stage. The same pre-treatment removes the copper that would otherwise co-deposit at the cathode, and it lowers the silver content of the anode to the level at which electrolysis is stable. Output: desilvered, decoppered gold feed plus a silver-bearing nitrate solution for recovery.

Steps 3 — Aqua Regia Dissolution and Off-Gas Condensation. The prepared feed is charged to a titanium or PP/PPH reaction vessel and dissolved in aqua regia — one part concentrated nitric acid to three parts concentrated hydrochloric acid, added in portions at a controlled rate and temperature — converting metallic gold to chloroauric acid (HAuCl₄). The reactor head is sealed and the vapour is drawn through a condenser and gas–liquid separator so that evaporated electrolyte and entrained metal-bearing mist condense and return to the vessel instead of leaving as loss. The solution is then cooled, diluted, filtered and clarified, and the insoluble fraction — silver chloride, refractory oxide and any unleached residue — is separated and washed. Output: clarified chloroauric acid liquor plus a filtered silver chloride and residue cake.

Steps 4 — Selective Reduction to Sponge Gold. Gold is brought back out of solution as metal by adding a selective reducing agent — oxalic acid, sodium metabisulfite or ferrous sulfate — at controlled temperature, acidity and dosing rate, so that gold reduces while base metals stay in solution. Reduction is run hot and under agitation to completion, judged by the disappearance of the yellow chloroaurate colour and then confirmed by testing the liquor for residual gold. The gold powder is settled, decanted, washed, scrubbed with dilute acid to remove occluded base-metal salts, washed again to neutral with deionised water, and dried. Output: sponge gold and fine gold powder, washed, dried and ready to be cast into anodes.

Steps 5 — Anode Melting and Plate Casting. The dried gold is melted in an induction furnace under a borax or soda-ash flux cover and cast into anode plates of a size and thickness matched to the cell, using graphite or steel anode moulds that have been preheated to prevent surface defects. The anode is the working electrode of the electrolytic step, so its weight, geometry, surface condition and silver and copper content are all controlled and recorded; anode weights and the anode-to-cathode spacing are set so the plate dissolves evenly and completely over the electrolysis cycle. Output: cast gold anode plates with recorded weight and assay.

Steps 6 — High-Current-Density Gold Electrolysis. The anodes are suspended in the electrolytic cell in an electrolyte of gold chloride in free hydrochloric acid, held at 60–70 °C, against cathode starter sheets of pure titanium or fine gold. Current is applied at a cathode current density of up to 1,000 A/m², and gold dissolves from the anode as Au³⁺ and deposits on the cathode as high-purity crystalline gold; base metals remain in solution and insoluble material falls as anode slime into the anode bag. The supply is a DC rectifier with superimposed AC, producing an asymmetric pulsed current that continuously breaks the silver chloride film off the anode, so the plate does not passivate and the silver is collected in the bag as a saleable by-product. Output: high-purity cathode gold, silver chloride in the anode bag, and anode slime.

Steps 7 — Cathode Washing, Electrolyte Polishing and Drying. Cathode gold is lifted from the cell, drained and washed with hot deionised water to remove occluded electrolyte, then washed and dried; washing water is routed back so that the gold it carries is not lost. In parallel, the electrolyte is kept at its working gold concentration of about 120–150 g/L, its temperature is held automatically at 60–70 °C, and the circulation and filtration loop removes suspended slime and keeps flow even past every cathode. The electrolyte is sampled, assayed and, when the impurity load rises, bled and replaced, with the gold in the bleed liquor recovered before the liquor leaves the circuit. Output: washed and dried high-purity gold, plus a monitored and polished electrolyte circuit.

Steps 8 — Final Melting and Vacuum Ingot Casting. The high-purity gold is melted once more and cast into bars, or granulated where a free-flowing form is wanted. For buyers who require a fully dense, ripple-free product, casting is carried out in a vacuum ingot casting machine under nitrogen or argon, where the combination of vacuum and inert-gas pressure eliminates porosity, shrinkage cavities and surface ripple and produces bars to any LBMA-approved trading specification. Each ingot or granulation lot is drilled or sampled for assay, marked with weight and fineness, and released with a Certificate of Analysis. Output: Au99.99 ingots, cast bars, granules or granulate released against an assay certificate.

Steps 9 — Anode Slime and Spent Electrolyte Recovery. Nothing that has touched the bath is discarded. Anode slime and bag contents are washed, dried and either melted with flux for recovery on site or bagged and assayed as a platinum-group-metal-bearing residue; spent electrolyte is treated to recover its gold content before the chloride liquor goes for neutralisation; filter cake, floor residue and clean-up material are returned to Steps 1 and 2 as a secondary feed. Each of these streams is weighed and assayed so that the batch metal balance closes and the actual refining loss can be reported rather than assumed. Output: recovered gold, a PGM-bearing residue, and a closed batch metal balance.

Steps 10 — NOx Scrubbing and Effluent Neutralization. Acid mist, chlorine, nitrosyl chloride and nitrogen oxides released from dissolution, from the electrolytic cell at 60–70 °C and from melting pass through an enclosed hood and ductwork into a multi-stage absorption train — two-stage bubble absorption, four-stage jet absorption and a final two-stage alkaline spray — with the absorption solution circulated and dosed automatically. Absorption efficiency is 99.5% or better, taking an inlet load of about 20,000 ppm down below 150 ppm, and the same train holds stack nitrogen oxides below the local limit; the acid effluent is neutralised in an agitated PPH neutralisation tank to a controlled pH before discharge or reuse, with washing water cross-reused in the circuit. Output: compliant stack emission and neutralised, recyclable effluent.

Product Structure (Main Equipment)

The line is delivered as a set of function-matched units rather than a list of tanks — a gold refinery machine bought as a single vessel will not reach 99.99% on its own, because fineness is produced by the sequence, not by any one unit. Each unit below is sized to the feed assay and the required daily output, is built in the material the duty demands, and is connected to the same PLC, the same ductwork and the same effluent circuit.

  • Reaction and dissolution unit — titanium dissolution vessel and PP/PPH reaction tank with sealed head, sight glass and inspection port, fed from the granulation stage and dosed with acid under controlled rate and temperature. Function: dissolve prepared gold feed into chloroauric acid without loss of vapour or entrained metal.
  • Condenser and gas–liquid separator — glass or PP condenser with circulation cooling water and a separator that returns condensate and captured mist to the reaction vessel. Function: recover evaporated electrolyte and entrained metal-bearing mist instead of losing them to the exhaust.
  • Reduction and precipitation unit — jacketed agitated vessel with reagent dosing, temperature control and pH measurement, served by a tilting or bottom-discharge arrangement. Function: reduce gold selectively to sponge gold under reproducible temperature, acidity and dosing conditions.
  • Filtration and washing unit — vacuum filter plate, filter press and wheel filter with diaphragm pumps, plus deionised-water washing and a conductivity endpoint check. Function: separate solution from solids and wash occluded salts out of the gold powder and the silver chloride cake.
  • Storage and dosing tanks — glass elevated storage tanks and PP solution tanks for aqua regia, chloroauric acid, reductant, hydrochloric acid and electrolyte make-up, with vacuum transfer rather than pouring. Function: hold and meter process liquors so that no solution is handled by hand and no gold is left on tank walls.
  • High-current-density gold electrolysis cell — PPH cell body with high-performance polypropylene and anti-ageing additive, transparent enclosed fume hood, anode bars, anode bags, and cathode starter sheets in pure titanium or fine gold. Function: dissolve gold anodically and deposit it cathodically at up to 1,000 A/m² to reach investment fineness.
  • Rectifier with superimposed AC power supply — DC rectifier with an AC component superimposed to create an asymmetric pulsed current, individually enclosed and isolated from workshop acid vapour. Function: suppress the silver chloride film that passivates the gold anode and keep the plate dissolving evenly and completely.
  • Electrolyte circulation, temperature control and automatic dosing — magnetic-drive fluorine-lined circulation pump, filtration loop, heater and heat exchanger, level and make-up control. Function: hold the electrolyte at 60–70 °C and 120–150 g/L gold with even flow past every cathode.
  • PLC control system with touchscreen HMI — control of rectifier start-stop, current and voltage setting, heating and circulation, plus monitoring of cell voltage, cell current and busbar temperature with a direct interlock that shuts the rectifier down on an abnormal parameter, and storage and recall of every parameter of every batch. Function: run the cell reproducibly, protect the equipment, and leave a traceable parameter record for each refining lot.
  • Melting furnace — induction melting furnace with a working range up to about 1,600 °C, thermocouple temperature monitoring and a tilting pour; a heat can be taken in as little as about two minutes at small batch size. Function: melt feed, sponge gold, cathode gold and anode scrap under a flux cover with rapid, repeatable heats.
  • Granulation machine — gravity granulator with solid-state IGBT power supply rated for continuous 24-hour duty and low-voltage induction coil protection. Function: convert melted gold into shot and granules for fast dissolution or for sale as granulate.
  • Anode casting and ingot moulds — preheatable anode moulds for plate casting plus ingot moulds for standard bar sizes. Function: produce electrodes of the exact geometry the cell needs and bars of the exact weight the buyer needs.
  • Vacuum ingot casting machine — closed casting chamber under vacuum with nitrogen or argon pressure, induction heating, high-seal casting cylinder and one-button automatic cycle; approximately 15 minutes for a cast, at 4 × 1 kg or 1 × 12.5 kg per cycle, with a 63 m³/h vacuum pump. Function: cast fully dense bars free of porosity, shrinkage and surface ripple to an LBMA-approved specification.
  • Multi-stage NOx and acid fume scrubber train — two-stage bubble absorption tank, four-stage jet absorption tower, two-stage alkaline spray section, demister, circulation tank, automatic chemical dosing, centrifugal fan and exhaust stack. Function: hold nitrogen oxides and acid mist at the stack below the local emission limit at 99.5% or better absorption efficiency.
  • Effluent neutralisation unit — agitated PPH neutralisation tank covering roughly 0.05 to 5 m³ of working volume, rated for atmospheric to −0.1 MPa gauge and −10 °C to 80 °C, with pH control and transfer pumps. Function: neutralise acid effluent to a controlled pH before discharge or reuse.
  • Off-gas and effluent monitoring with interlocks — continuous measurement of nitrogen oxides in the stack, pH and conductivity in the effluent circuit, and level and temperature in the scrubber circulation tank, all wired to alarm and to automatic dosing and shutdown. Function: prove compliance continuously and stop the process automatically if a limit is approached.

Product Features

Each feature below is a design decision taken because of a specific problem in gold refining, not a general claim. They are listed in the order a buyer evaluates them: what the line produces, how fast, how much gold it holds, how much it loses, and how it behaves in a real refinery building.

  • One line, both routes — chemical dissolution and reduction and electrolytic refining are engineered as one flow sheet on one frame, so the line accepts both high-grade feed that can go straight to anodes and lean, dirty or high-silver feed that has to be dissolved and reduced first. Function: one feed gate for the whole range of gold-bearing material a refinery sees.
  • Cathode current density up to 1,000 A/m² — roughly three times the loading of a conventional Wohlwill cell on the same cathode area, achieved by electrolyte circulation, temperature control and anode geometry rather than by simply raising the current. Function: the same daily output from a smaller, cheaper cell and a much shorter cycle.
  • 10–20 hour electrolysis cycle — a batch completes in a working day or overnight instead of the one to two days a conventional gold electrolytic refinery requires. Function: faster turnaround of high-value metal and lower in-process inventory.
  • DC with superimposed AC — an asymmetric pulsed current continuously breaks the silver chloride film off the anode as it forms. Function: no anode passivation, complete anode dissolution, and silver recovered as a saleable chloride instead of blocking the cell.
  • Electrolyte gold lock-up cut to about half — the circuit holds approximately 0.15 kg of gold per litre of electrolyte, so a 12-litre cell locks up roughly 1.8 kg of gold rather than the 4 kg or more a conventional gold electrolytic circuit holds for the same duty. Function: less working capital tied up in the bath and less exposure to gold price movement.
  • Refining loss below 0.02% — measured as loss of gold from the batch, with wash water, electrolyte bleed, anode slime, filter cake and floor residue all returned or recovered. Function: the difference between a refining loss and a refining business.
  • Flue-gas condenser returns electrolyte to the cell — the electrolytic cell runs at 60–70 °C and the dissolving reactor runs hot, so vapour is condensed and returned rather than vented. Function: gold is not carried out of the plant in the exhaust.
  • Enclosed transparent hood — a closed, transparent enclosure over the cell and the dissolving vessel, sealed at the extraction points. Function: the operator can see the process without standing in the acid plume, and the extraction system captures the plume at source.
  • PLC control with real interlocks — touchscreen control of rectifier start-stop, current and voltage setting, heating and circulation, with monitoring of cell voltage, cell current and busbar temperature and a direct interlock to the rectifier when a parameter goes abnormal. Function: reproducible batches, protection of the equipment, and safe default behaviour without an operator decision.
  • Batch parameter logging and recall — every parameter of every electrolysis batch is stored and can be recalled. Function: process problems can be diagnosed from data, and a batch record can be produced for a customer or an auditor.
  • Anti-corrosion materials chosen per duty — high-performance polypropylene with anti-ageing additives, PPH structural framing, titanium for the dissolution vessel and cathode plates, titanium-clad copper for conductive bars, glass for the condenser and elevated tanks, and enamel-lined steel where the duty demands it. Function: equipment life measured in years in an atmosphere that destroys ordinary steel in months.
  • Rectifier isolated from acid vapour — the power supply is independently enclosed and physically separated from the workshop atmosphere. Function: the electronics survive a chloride-and-acid environment.
  • Vacuum and inert-gas ingot casting — casting under vacuum with nitrogen or argon pressure, with a high-seal casting cylinder and no open flame. Function: dense, ripple-free bars with no porosity or shrinkage cavities, cast to an LBMA-approved trading specification.
  • Integrated emissions control — the reactor, the cell, the melting furnace and the casting station all vent into one multi-stage absorption train that is part of the delivered package rather than a separate purchase. Function: the plant is commissioned as a compliant plant, not as a plant waiting for a permit.
  • Quantified environmental performance — 99.5% or better nitrogen-oxide absorption, outlet below 150 ppm from an inlet above 20,000 ppm, and a measured in-service result of 80 mg/m³ against a 100 mg/m³ limit. Function: the operator can demonstrate compliance with numbers, not with adjectives.
  • Cross-reused washing water and neutralised effluent — cathode washing water, filter wash liquor and scrubber blowdown are routed back into the circuit wherever the chemistry allows, and the balance is neutralised in an agitated PPH tank. Function: lower fresh-water demand and a smaller effluent load.
  • Cyanide-free refining route — the refining circuit uses aqua regia, chloride electrolyte, hydrochloric and nitric acid, oxalic acid and metabisulfite; no cyanide is used anywhere in refining. Function: a simpler permit, a safer workplace and no cyanide-bearing effluent stream.
  • Modular, expandable, relocatable — the line is built as function-matched skids and single units that can be laid out into an existing refinery building or containerised for a greenfield or remote site, and extended later with additional cells. Function: capacity grows with the business instead of in one capital step.
  • Single-supplier interface — dissolution, reduction, filtration, electrolysis, casting, granulation, scrubbing and effluent neutralisation come from one supplier with one control philosophy and one commissioning team. Function: no argument between vendors when a stream underperforms.

Technical Parameters & Specifications

The table below states the engineering parameters of the gold refining process line — the parameters that are validated in commissioning and recorded per batch. Capacities, installed power, footprint, clear height and utility loads are engineered to the customer’s feed assay and required daily output and are therefore confirmed in the technical proposal rather than fixed here; the process parameters — current density, temperature, cycle time, gold concentration, absorption efficiency, fineness, loss and emission limits — are fixed values that the line is guaranteed to hold.

Parameter Specification
Applicable feed grade Granulated crude gold, doré and gold alloy feed from about 75% Au for the aqua regia and reduction route, and from about 90–95% Au and above for direct anode casting and electrolysis
Feed impurity tolerance Silver below 6% and copper below 2% in the anode for stable direct electrolysis; higher-silver or higher-copper feed is routed through nitric acid pre-treatment first
Product fineness 99.99% (Au99.99, Grade I) as standard; 99.999% by a second electrolytic pass
Product form Cast ingots and bars to a nominated LBMA-approved trading specification, granules, granulate, sponge gold and fine gold powder
Cathode current density Up to 1,000 A/m²
Power supply DC rectifier with superimposed AC, producing an asymmetric pulsed current
Electrolyte composition Gold chloride in free hydrochloric acid
Electrolyte gold concentration 120–150 g/L Au
Electrolyte temperature 60–70 °C, automatically controlled
Electrolyte gold lock-up Approximately 0.15 kg of gold per litre of electrolyte
Electrolysis cycle time 10–20 hours per batch
Electrolysis efficiency Approximately 3–4 times the throughput of a conventional gold electrolytic cell at the same cathode area
Dissolution and reduction conditions Aqua regia added in portions under controlled heating; gold reduced at approximately 70 °C with pH adjusted to approximately 1.5
Refining loss Below 0.02% of the gold contained in the batch
Overall recovery 99% and above, with gold in wash water, electrolyte bleed, anode slime, filter cake and floor residue returned to the circuit
Hydrochloric acid consumption Approximately 150 litres per tonne of gold in the electrolytic step
Nominal capacity Configured to your feed assay and required daily gold output, from a bench unit to a multi-hundred-kilogram-per-day refinery
Installed power Configured to capacity, cell count and local supply voltage
Footprint and clear height Configured to throughput and laid out into your existing refinery building or a containerised plant
Utilities Configured to assay, throughput and site conditions: cooling water, deionised water, compressed air, extraction air volume and reagent storage
Extraction and scrubber air volume Configured to the number of reactors and cells in service, with the absorption train sized on the peak simultaneous load
Nitrogen oxide inlet load Above 30,000 mg/m³ at the reactor outlet, equivalent to approximately 20,000 ppm
Nitrogen oxide outlet concentration Below 150 ppm, with a measured in-service result of 80 mg/m³ against a 100 mg/m³ local emission limit
Absorption efficiency 99.5% and above
Effluent neutralisation Agitated PPH tank, atmospheric to −0.1 MPa gauge, −10 °C to 80 °C, working volume approximately 0.05–5 m³, pH controlled and monitored
Wetted materials High-performance polypropylene with anti-ageing additive and PPH structural framing, titanium, titanium-clad copper, glass and enamel-lined steel as the duty requires
Cathode material Pure titanium plate or fine gold starter sheet
Conductive bars Titanium-clad copper
Melting and casting Induction melting up to approximately 1,600 °C; vacuum inert-gas ingot casting at approximately 15 minutes per cast, 4 × 1 kg or 1 × 12.5 kg, under nitrogen or argon
Control system PLC with touchscreen HMI, cell voltage, current and busbar temperature monitoring, rectifier interlock, and storage and recall of every batch parameter
Product verification Fire assay with ICP-OES confirmation for every batch, released with a Certificate of Analysis
Batch metal balance Feed weight, product weight, residue weight and reported refining loss recorded and reported for every lot

Technical Advantages

Gold refining equipment is easy to describe and hard to verify. Almost every supplier of a gold refining machine or a gold electrolytic refining cell in this market quotes 99.99% purity and “no loss”; very few publish the current density, the cycle time, the electrolyte concentration, the gold held in the bath, the acid consumption or the stack concentration that make those numbers possible. The advantages below are stated as values that a buyer can test in a factory acceptance or a commissioning trial, and they are the reason this line performs differently from a conventional gold electrolytic refinery at the same capacity.

  • Up to 1,000 A/m² cathode current density against roughly 300–400 A/m² conventional — high current density is the single biggest lever on gold refining throughput, because output per cell is proportional to current. Reaching it requires the electrolyte to be circulated evenly past every cathode, the temperature held within a narrow band at 60–70 °C and the anode geometry controlled; raising the current without those three conditions produces rough, dendritic and impure cathode gold. This line is engineered as a system for that reason, not simply fitted with a larger rectifier. Advantage: the same daily output from far fewer cells and a far smaller building.
  • 10–20 hour cycle instead of one to two days — a conventional gold electrolytic refinery needs one to two days per batch, and the metal in that batch is unavailable throughout. At current gold prices the carrying cost of a slow batch is a real cost. Advantage: roughly three to four times the effective throughput per cell, and metal released back to sale a day earlier.
  • Electrolyte gold lock-up around half the conventional figure — a conventional gold electrolytic circuit holds on the order of 4 kg of gold in solution for a 10 kg/day duty; this line holds approximately 0.15 kg per litre, so a 12-litre circuit holds about 1.8 kg. Advantage: lower working capital, lower price-movement exposure and a smaller insurance sum on the bath.
  • Asymmetric pulsed current eliminates anode passivation — silver in the anode forms silver chloride that coats the plate and stops dissolution; conventional practice tolerates this by limiting anode silver or by manual intervention. The DC supply with superimposed AC breaks the film off continuously. Advantage: complete anode dissolution, no unreacted plates returned to melt, and silver recovered as a saleable chloride from the anode bag.
  • Refining loss below 0.02% — a conventional electrolytic gold circuit accepts losses an order of magnitude larger, because electrolyte is lost as vapour, entrained in off-gas, retained on tank walls and discarded in bleed liquor. Every one of those paths is closed on this line: vapour is condensed and returned, solution is moved by vacuum transfer rather than pouring, glass tanks are used where residual hold-up matters, and bleed liquor is treated for gold before it leaves the circuit. Advantage: at 100 kg/month throughput, 0.02% is 20 g per month recovered rather than lost — and it is measurable.
  • Condenser-based vapour recovery instead of exhaust loss — the cell runs hot by design, and heating electrolyte is exactly how a gold refinery loses gold up the stack. The condenser returns it. Advantage: the high operating temperature stops being a loss mechanism.
  • Emissions performance that can be quoted as a number — 99.5% or better absorption, an inlet above 20,000 ppm brought below 150 ppm, and a documented in-service result of 80 mg/m³ measured against a 100 mg/m³ local limit. Multi-stage absorption — two-stage bubble, four-stage jet and two-stage alkaline spray — is delivered as one train with automatic dosing. Advantage: permit applications, audits and local inspections are answered with measured data rather than with a specification sheet.
  • Vacuum inert-gas casting produces bars, not castings — porosity, shrinkage cavities and surface ripple are what separate a bar that a bank will accept from a bar that gets discounted. Vacuum casting under nitrogen or argon with a high-seal chamber and no open flame eliminates all three. Advantage: bars to an LBMA-approved trading specification, and no argument about the product.
  • Verification built into the process rather than claimed — every batch is released against fire assay with ICP-OES confirmation; the fineness target is the Shanghai Gold Exchange Au99.99 (Grade I) standard gold ingot specification; and the melting point loss, the anode weight, the cathode weight and the residue weight are recorded so the metal balance closes. Advantage: a buyer can audit the refining loss instead of taking it on trust.
  • Cyanide-free refining chemistry — no cyanide is used in the refining route; the reagents are aqua regia, hydrochloric acid, nitric acid, oxalic acid, metabisulfite and alkaline scrubber liquor. Advantage: simpler permitting, safer working conditions and no cyanide-bearing effluent.
  • Materials selected against the actual duty, not against a price list — polypropylene with anti-ageing additive for the cell body and ductwork, PPH for structural framing and hence for the whole support structure, titanium for the dissolution vessel and cathode plates, titanium-clad copper for current-carrying bars, glass for the condenser and elevated tanks. Advantage: a chloride-and-acid plant built from materials that a chloride-and-acid plant needs.
  • Rectifier isolated from the acid atmosphere — power electronics fail long before mechanical equipment in a refinery, and they fail faster in a chloride atmosphere. The rectifier is independently enclosed and physically separated. Advantage: longer equipment life and fewer unplanned stops.
  • Batch data, not batch memory — cell voltage, current, busbar temperature and every setpoint are logged and recallable per batch, with an interlock that shuts the rectifier down if a parameter goes abnormal. Advantage: problems are diagnosed from records, operator error is contained, and a customer or auditor can be shown a batch file.
  • One supplier for the whole train — dissolution, reduction, filtration, electrolysis, casting, granulation, scrubbing, effluent neutralisation and control come from one engineering team with one control philosophy. Advantage: single point of accountability at commissioning and afterwards.

Service Process

The line is delivered as an engineered plant, so the service process is a project process: the feed is tested before the flowsheet is fixed, the flowsheet is designed around the customer’s building and permit, the equipment is proved in a factory acceptance test before dispatch, and the plant is commissioned to a performance test rather than simply switched on.

Steps 1 — Raw Material Testing and Route Selection. A representative sample of the customer’s feed is received, weighed, milled and assayed in the laboratory — fire assay with ICP-OES confirmation, plus silver and copper determination, because those two set the route and the anode specification. Dissolution and reduction trials establish reagent consumption, expected recovery and the achievable fineness for that specific material, and the customer receives a test report stating the recommended route before any equipment is specified. Output: a laboratory test report with assay, recovery, reagent consumption and route recommendation.

Steps 2 — Flowsheet and Plant Layout Design. The flowsheet is drawn for the tested feed and the required daily output, with equipment sized on the peak simultaneous load rather than the average, and the layout is drawn into the customer’s actual building — clear height, floor loading, chemical storage, extraction routing, effluent route and operator access all resolved on the drawing. Where the site is new or remote, a containerised or skid-mounted arrangement is developed instead. The deliverable is a technical proposal with an equipment list, a utility schedule, a footprint drawing and the process guarantees the line will be commissioned against. Output: a technical proposal with flowsheet, layout, equipment list, utility schedule and process guarantees.

Steps 3 — Equipment Manufacturing and Factory Acceptance Test. Equipment is manufactured to the released drawings, wetted parts are verified against the duty materials, and the electrolysis cell, rectifier and control system are assembled and wired as a set. Before dispatch the customer is invited to witness a factory acceptance test that includes a hydrostatic and leak test on the wetted assemblies, a functional test of the PLC, rectifier, dosing, temperature control and interlocks, and where feed is available a trial batch confirming dissolution and reduction behaviour. Output: a factory acceptance test report and released equipment.

Steps 4 — Shipment, Installation and Commissioning. Equipment is packed for sea or land freight — cells, tanks and frames on cradles in plywood cases, fragile items crated separately, with a packing list keyed to the installation drawings — and our engineers attend site to supervise installation, align the cell and busbar arrangement, connect the extraction and effluent circuits and commission the plant. Commissioning runs on the customer’s own material wherever possible and closes with a performance test on fineness, recovery, cycle time, reagent consumption and stack emission. Output: an installed and commissioned line with a signed performance test record.

Steps 5 — Operator Training and Production Handover. The customer’s operators and supervisors are trained on the delivered plant rather than on a generic manual: feed preparation and granulation, acid handling and dosing, dissolution and reduction, anode casting, cell loading and unloading, cathode washing and drying, melt and cast, scrubber operation and dosing, effluent neutralisation, and what to do when a parameter goes out of range. Training combines classroom sessions on the chemistry and the schematic with hands-on operation of each unit, and covers the PLC screens, alarm handling and batch record keeping. Handover is not complete until the customer’s team can run a full batch unaided. Output: trained operating and supervisory staff, and a documented handover.

Steps 6 — Warranty, Spare Parts and Preventive Maintenance. A bill of wearing and critical spares is agreed at the contracting stage and can be shipped with the plant, so that consumables, seals, filter media, pump parts, electrodes, bags, packing media and dosing components are on site before they are needed. A preventive maintenance schedule is issued covering the cell, busbar and electrode inspection intervals, electrolyte sampling and analysis, scrubber dosing and packing checks, condenser and duct cleaning, pump and seal inspection, and calibration of the pH, conductivity, temperature and NOx instruments. Output: an installed spare-parts package and a scheduled preventive maintenance programme.

Steps 7 — Remote Diagnostics and Continuous Process Improvement. Process parameters logged by the control system can be shared with our engineers for review, so that a drift in cathode quality, a rise in cell voltage, a fall in absorption efficiency or an increase in reagent consumption can be identified from data before it becomes a batch problem. Batch records are reviewed against the original test report, and where feed or product requirements change — a new supplier of scrap, a higher fineness target, a larger daily output — the route, the reagent charge and the electrolyte management are revised, and additional cells or units are added to the existing frame. Output: data-based process support, with an upgrade path as the customer’s business changes.

Warranty & After-Sales Service

The warranty applies to equipment designed, manufactured and supplied by YuSai Machinery, covers defects in design, materials and workmanship under normal operating conditions, and is honoured through the same engineering team that commissioned the line. Warranty terms, the covered scope, the excluded items and the response times are fixed in the contract so that both parties know what is included before the plant is shipped.

  • Warranty period — the standard warranty runs from the date of successful commissioning, with the exact duration fixed in the contract; extended warranty is available on request. Function: a defined window in which supplier responsibility is unambiguous.
  • What is covered — design, materials and workmanship of the supplied equipment, including the reaction and dissolution vessel, reduction unit, filtration and washing unit, storage and dosing tanks, electrolysis cell and hood, rectifier and control system, melting and granulation equipment, vacuum ingot casting machine, scrubber train and effluent neutralisation tank, together with the PLC programme and the control logic as supplied. Function: the customer is not left to argue about which vendor owns a fault.
  • What is not covered — consumable and wearing items such as filter media, packing, seals, gaskets, anode bags, electrodes and cathode starter sheets; damage from operation outside the agreed parameters, from feed outside the agreed specification, from failure to follow the maintenance schedule, from unauthorised modification, or from reagents and utilities outside specification; and freight, import duties and site civil works. Function: a clear boundary so that both sides can plan.
  • Response and attendance — a service engineer responds to a reported fault within an agreed time from notification, with telephone and remote diagnosis first and site attendance where the issue requires it; the response and attendance times are set out in the contract for the customer’s region. Function: a fault is answered within a known interval rather than whenever an engineer becomes available.
  • Remote support — remote review of PLC logs, batch records, cell voltage and current history, busbar temperatures and scrubber readings allows most process questions to be answered without a site visit. Function: faster resolution and fewer unnecessary trips.
  • Spare parts — a recommended wearing and critical spares list is issued with the plant and can be supplied as an initial stock; ongoing spares are supplied against the equipment list with the parts identified by drawing and position. Function: the plant can be maintained without reverse-engineering parts.
  • Consumables and reagents specification — the specification of reagents, filter media, packing and electrodes is documented so that local sourcing does not compromise fineness, cycle time or emission performance. Function: local supply without a drop in performance.
  • Training and refresher support — operator training is delivered at commissioning and can be repeated when staff change or when the line is expanded; refresher and advanced training on electrolyte management, anode casting and emission control is available. Function: operating standards hold after the commissioning team leaves.
  • Process support on new feed — when the customer brings a new feed material, our laboratory can test it and confirm whether the existing route, reagent charge and anode specification remain valid or need revision. Function: the refinery keeps its fineness guarantee as its feed range widens.
  • Documentation — the plant is handed over with an operation and maintenance manual, an electrical and instrument schematic, a spare parts list, a commissioning and performance test record and the equipment drawings. Function: a plant that can be operated, maintained and audited without the supplier present.

Frequently Asked Questions

Q1. What is the gold refining process in simple terms?
The gold refining process turns impure but concentrated gold — doré bullion, karat scrap, gold sponge or anode slime — into tradeable fine gold by dissolving the gold and bringing it back as metal. Feed is assayed and granulated, silver and base metals are removed with nitric acid, the gold is dissolved in aqua regia to form chloroauric acid, a selective reducing agent brings it back as sponge gold, the sponge is melted and cast into anode plates, and electrolysis in gold chloride electrolyte deposits 99.99% gold on the cathode, which is then washed, dried and cast into ingots.

Q2. What is the difference between the Miller process, the Wohlwill process and aqua regia refining?
The Miller process blows chlorine gas through molten gold; impurities and silver form chlorides that float as slag, giving roughly 99.5% gold quickly and simply. The Wohlwill process is electrolytic: an impure gold anode dissolves in gold chloride and hydrochloric acid and pure gold plates onto the cathode, reaching 99.99% or better. Aqua regia refining dissolves gold chemically and reduces it back as powder, which is the practical route for low-grade, mixed or high-silver material that cannot be cast into a stable anode. This line combines aqua regia refining and Wohlwill-type electrolysis in one flow sheet, so it accepts the full range of feed.

Q3. Why does the process need electrolysis if chemical reduction already reaches 99.9%?
Chemical reduction reliably reaches around 99.9% and is limited by the purity of the reducing agent, the completeness of the wash and the behaviour of the liquor. It also struggles to deliver a consistent five-nines product. Electrolysis separates gold from the remaining impurities electrochemically: base metals stay in solution and insoluble material drops as anode slime, so the deposit on the cathode is purer than anything the chemical step can produce, and repeatability is set by current, temperature and electrolyte concentration rather than by operator judgement.

Q4. Can the line refine karat gold and jewellery scrap, or only doré bars?
It refines both. Karat gold and jewellery scrap go through granulation, nitric acid pre-treatment to strip the alloying silver and copper, aqua regia dissolution and reduction, and then to anodes and electrolysis. Because karat scrap already carries a high gold content, it does not need enrichment before refining — it needs the alloying metals taken out, which is exactly what pre-treatment does.

Q5. How much gold is locked up inside the equipment at any time?
The electrolytic circuit holds approximately 0.15 kg of gold per litre of electrolyte, so a 12-litre cell locks up about 1.8 kg of gold in solution, against roughly 4 kg or more for a conventional gold electrolytic circuit of the same duty. Anode plates in the cell add the working load, and sponge, powder and solution in the chemical half of the line add their own inventory. The figure is calculated for each project from the cell volume and the batch size, and is stated in the technical proposal because it is a direct working-capital number at today’s gold price.

Q6. What is the refining loss, and how is it verified?
Refining loss on this line is below 0.02% of the gold in the batch. It is verified by closing a metal balance for every lot: feed weight and assay in, product weight and assay out, plus the weighed and assayed residues — anode slime, filter cake, bag contents, bleed-liquor recovered gold and clean-up material. The difference is the reported loss. Nothing is estimated, and the batch record is available to the customer.

Q7. How is the purity of the finished gold confirmed?
Purity is confirmed by fire assay with inductively coupled plasma optical emission spectrometry confirmation on a sample taken from the finished ingot or granulation lot. Fire assay is the reference method for gold because it is not a surface measurement. X-ray fluorescence should not be relied on as the release method for a bar, because it reads only the top few microns and its error on gold alloys can reach a few percent; a bar must be sampled from the melted, homogenised metal to be assayed properly.

Q8. What fineness can the line guarantee, and against which standard?
The standard product is 99.99% gold, cast to the Shanghai Gold Exchange Au99.99 (Grade I) standard gold ingot specification, and cast bars can be produced to any LBMA-approved trading specification the buyer nominates. Where a five-nines product is required, the cathode gold is recast and passed a second time through the same electrolytic cell to reach 99.999%.

Q9. What silver and copper content can the feed contain?
For stable direct electrolysis, silver in the anode should stay below about 6% and copper below about 2%. Silver above that level forms silver chloride that passivates the anode plate, and copper above that level co-deposits at the cathode and reduces product purity. Feed that exceeds either limit is not rejected — it is routed through nitric acid pre-treatment, which removes silver and base metals first, so high-silver and high-copper material is handled rather than turned away.

Q10. How long does a batch take, and how many batches per day?
The electrolytic step runs 10–20 hours per batch, so a cell completes one batch per working day or overnight. The dissolution and reduction stages ahead of it run in hours; a granulated batch dissolves far faster than a solid bar of the same weight because the reaction is surface-controlled. The number of batches per day is set by the number of cells, which is why capacity is configured to the required daily output rather than fixed by a single model.

Q11. Why does the line use a DC supply with superimposed AC?
Because silver in the anode forms a silver chloride film that coats the plate and stops it dissolving. A DC supply with an AC component superimposed creates an asymmetric pulsed current that breaks the film off continuously as it forms. The anode therefore dissolves evenly and completely, unreacted plates do not have to be returned for remelting, and the silver reports to the anode bag as recoverable silver chloride instead of blocking the cell.

Q12. Do I need cyanide to refine gold with this line?
No. The refining circuit uses aqua regia, gold chloride electrolyte, hydrochloric acid, nitric acid, oxalic acid and metabisulfite, and alkaline scrubber liquor. Cyanide has no role in refining this feed range; it belongs to ore leaching, not to refining. Removing cyanide from the refining circuit simplifies permitting, removes a cyanide-bearing effluent stream and reduces the hazard the operator is exposed to.

Q13. What does the plant do with the acid mist and nitrogen oxides it produces?
Dissolution and electrolysis are vented at source into a multi-stage absorption train — two-stage bubble absorption, four-stage jet absorption and a final two-stage alkaline spray — with automatic chemical dosing and a demister. Absorption efficiency is 99.5% or better, taking an inlet above 20,000 ppm down below 150 ppm, and the same train has been measured in service at 80 mg/m³ against a local limit of 100 mg/m³. Scrubber liquor, filter wash water and cathode washing water are cross-reused in the circuit, and the acid effluent balance is neutralised to a controlled pH in an agitated PPH neutralisation tank.

Q14. What space, power and utilities does the line need?
Footprint, clear height, installed power and utility loads are all configured to the feed assay, the required daily output and the customer’s building, and are stated in the technical proposal rather than fixed here. The process parameters are not configured — current density up to 1,000 A/m², electrolyte at 60–70 °C and 120–150 g/L gold, a 10–20 hour cycle and 99.5% or better absorption are the values the line is guaranteed to hold. The line is built as function-matched units and can be laid out into an existing refinery or containerised for a new or remote site.

Q15. What is included with the plant, and what is not?
Included: the reaction and dissolution vessel, condenser and gas–liquid separator, reduction and precipitation unit, filtration and washing unit, storage and dosing tanks, electrolysis cell with hood, anode bags and cathode starter sheets, rectifier with superimposed AC supply, electrolyte circulation and temperature control, PLC control system with touchscreen, melting furnace, granulation machine, anode and ingot moulds, vacuum ingot casting machine, multi-stage scrubber train, effluent neutralisation tank, monitoring and interlocks, and the documentation, training and commissioning that go with them. Not included unless separately agreed: site civil works and foundations, building and extraction ductwork outside the equipment battery limit, chemical storage buildings and bunding, electrical supply to the plant terminal, reagents, and local permits and approvals.

Q16. How long does delivery and commissioning take, and what does the warranty cover?
Delivery time and commissioning duration are quoted per project because they depend on the number of cells, the degree of containerisation and the destination. The service process is fixed: laboratory testing of the feed, flowsheet and layout design, manufacture with a factory acceptance test, shipment and site installation, commissioning against a performance test on fineness, recovery, cycle time and emission, operator training and handover. The warranty covers defects in design, materials and workmanship of the supplied equipment, runs from successful commissioning for a period fixed in the contract, excludes consumable and wearing items and damage from operation outside the agreed parameters, and is supported by a recommended spare-parts list and remote diagnostics on the batch data.

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