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Refining Plant
Working Principle
The system for a correct dust laying is made by a special scrubber tower where the noxious vapours are channelled into a tower with their consequential speed reduction. From the dome tower, a drainage system homogeneously spread a neutraliser agent specific for each kind of vapour.
- Refinery is a procedure used to extract pure metal from an alloy. This is an ancient process,but still used for its simple operation, cheap, too!
- By our compact refining plants, it is possible to achieve a purity of the treated metal close to 99,99%.
- With our plants the purity obtained is very high, never less than 99,95%.
- Refinery is made by the dissolution of the entire alloy mass into Aqua Regia by the pure gold precipitat ion in powder form to be consequently washed.
- With this process it is possible to recover the silver as insoluble silver chloride. Then, by the right procedure, it will be possible to reduce the metallic silver.
- Thanks to the right vapour speed modulation and to the intensity of the reactor drainage, the scrubber neutralise the fumes until the 99%.
- With our systems is possible to normalise and optimise the concentration of the agent by the PH-metre and a dosing pump.
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| Big Gold Refining Plant | Big Silver Refining Plant |
Technical Features
- The installation is complete of: Tower sizes: Height mm 3500, Diameter mm 600
- Bed of Rashing rings made in PP
- Sprinkled by sprayers made in PVC
- Recycling pump with impeller and dipping part made in PP
- Drops separator
- Well dimensioned aspirator in PVC which has PP impeller on the tower outlet;
- Piping in PVC
- Tank for solution holding, equipped of vertical pump made in PP for liquid recycling
- Inspection window for rings charge and discharge
- Automatic dosing pump
- pH-meter to control the purity of the rinsing water
- Capacity: 1500 m3/h
- Overall dimensions : 700 x 1500 x 3500h mm
Small Gold Refining Plants

| Example Models |
ORS TR8 |
ORS 50/100 |
ORS 100/200 |
ORS 100D/200 |
ORS 200D/200 |
| Average of refined alloy per normal working shift |
over 12 Kg. |
over 30 Kg. |
over 60 Kg. |
over 120 Kg. |
over 240 kg. |
| Numbers of working glass reactors |
02 |
02 |
02 |
03 |
03 |
| Heating system: |
Electric |
Diathermy oil bath |
Diathermy oil bath |
Diathermy oil bath |
Diathermy oil bath |
| Power consumption |
Kw 3,5 |
Kw 5,0 |
Kw 7,5 |
Kw 13,0 |
Kw 15,0 |
| Overall size |
160x130x220H cm. |
360x150x240H cm. |
360x150x240H cm. |
520x150x240H cm. |
520x150x240H cm. |
Small Silver Refining Plants
| Example Models |
ORS PEAG12 |
ORS EAG1 |
ORS EAG2 |
ORS EAG3 |
ORS EAG5 |
| Refined alloy per day |
till 12 Kg. |
over 30 Kg. |
over 60 Kg. |
over 90 Kg. |
over 150 kg. |
| Numbers of working cells |
01 |
01 |
02 |
03 |
05 |
| Movement system: |
Compressed air |
Compressed air |
Compressed air |
Compressed air |
Compressed air |
| Up gradable |
NO |
YES till 150 Kg. |
YES till 150 Kg. |
YES till 150 Kg. |
NO |
| Overall size |
150x80x160H cm. |
200x95x130H cm. |
300x95x130H cm. |
400x95x130H cm. |
600x95x130H cm. |
Gold Potassium Cyanide Production Plants

| Example Models |
Production capacity per day |
Working cells |
Heating system |
Over all dimensions |
| ORS CyAu3 |
around 03 Kg. |
30 liters glass |
Static heater |
240x85x246H cm. |
| ORS CyAu5 |
around 05 Kg. |
50 liters glass |
Static heater |
240x85x246H cm. |
Electrolytic Gold Refining Plant
Working Principle
Electrolysis is a technological process that utilizes the electric energy generated from a current rectifier and from the technical features of acid solution. The metal to be deposited (in this case Au) is melted by a liquid solution called gold chloride.
The metal to be refined is generally composed of almost pure gold (min. 995,0‰), previously melted and poured in a special mould called ANODE which will be placed to the positive pole.
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The cathode, a very thin plate of pure gold (999,9‰) will be placed to the negative pole. By means of a proper electromotive force and for the electrolytic bath characteristics , the metal anodes will gradually dissolve; at the same time, through the natural pole attraction between electrodes, gold migrates towards the cathode under metallic sponge form, in the plunged cathode surface. |
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Once the operation is over, the initial cathode and the total gold sponge deposited , are properly washed , melted and prepared for the following working phases. Being a selective process for noble metals, when the operation ends, the cathode will carry only an elevated fineness gold deposit: 999,9‰.ALWAYS GUARANTEE.
Productivity is to be considered in 24 h. cycle and taking into consideration the number of anodes used in the cells, following from the morning these operations:
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- Cathodes recovery / washing and melting
- Recovery of anodes pieces / washing
- Melting of new anodes
- Bath maintenance (acidity and gold analysis)
- Bath filtering / parameter correction
- New cathodes positioning / pre-heating
- New anodes positioning
- Initial current setting
- Gradual current increasing up to proper parameter achievement
- Control of baths and adding systems levels
Model: ORS Eau20
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- Refined capacity: per day over 20 Kg.
- Working cells: 02
- Heating system: PTFE wire
- Power consumption Kw: 4,5
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Model: ORS Eau30
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- Refined capacity: per day over 30 Kg.
- Working cells: 01
- Heating system: PTFE wire
- Power consumption Kw: 5,0
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