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    Refining Plant With Static Glass

    • Supply TypeManufacturer, Exporter, Supplier, Retailer
    • Preferred Buyer Location All over the world

    Principle of operation Through a combination of acids and the subsequent use of chemical compounds it is possible to refine gold containing alloys. The aqua regia is a mixture of hydrochloric acid....
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    • calendar Member Since 16 Years
    • building Nature of Business Retailer
    • Year of Establishment 1938

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    Principle of operation

    Through a combination of acids and the subsequent use of chemical compounds it is possible to refine gold containing alloys.
    The aqua regia is a mixture of hydrochloric acid (HCl) and nitric acid (HNO 3 ).

    The refining process can be summarized in several operations:

    • Analysis of the alloy to be refined title
    • Production of grit or fine gold foils
    • Refining by aqua regia
    • Separation and storage of silver chloride (AgCl)
    • gold precipitation
    • Recovery and filtering of the precipitated gold powder
    • Analysis of the security of this gold
    • Gold Fusion in its final form

    Key benefits:

    • Compact system
    • Easy to transport and assemble
    • Low purchase costs
    • No harmful smoke released
    • No loss of gold in the process
    • Automatic loading of acids

    Refining by aqua regia

    The minimum recommended title for the gold alloys to be refined must be at least 600/1000.
    Lower Titles significantly reduce productivity by increasing the processing time.
    The percentage of silver present in the alloy should not exceed 10-12%. Higher values can reduce the productivity of the process as well as adding the times.

    The gold will be melted and reduced to fine grit (through a melting furnace and a container for the production of grits) or small plates. These latter make it possible to maximize the effect of dissociation due to their high external surface when they are immersed in aqua regia solution.
    The grit, due to a lower outer surface and more irregular shape, it needs a longer time for its complete dissociation, sometimes leaving residues in the reactor
    is, however, easier to get gold in the form of grit.

    The plant consists of:

    • Bath PPL with panels, which accommodate the two containers for HCL and HNO3.
    • Extractor in PPL with the intake manifold, to be connected to our tower suction and fumes neutralization, type TLF. The above is constructed so as to collect any leaks of acids.
    • An electric heater with power regulator
    • Reactor with condenser, pyrex glass.
    • Transfer HCl and HNO 3 as containers sized containers by means of vacuum.
    • Polyethylene container, with lid and suction for AgCl decantation.
    • Flask pyrex glass for the gold cementation, porcelain Buchner funnel and its lid for the transfer and filtration of solutions by means of vacuum.
    • Antacid diaphragm pump, powered by compressed air, for the transfer of solutions.
    • polyethylene containers for the containment of the mother liquors.
    • Metering pumps for the transfer of HCL and HNO3 in the reactors.
    • Pyrex glass capacitors.

    The described plant can undergo customizations on the customer's request, photos posted are just one example of the many possible system solutions.
    Based on the needs of the customer it is possible to create tailor-made systems, with suitable characteristics to the machining process required.



     

    TECHNICAL DATAIAO10IAO20IAO20-20IAO50-10IAO50-20IAO50-50
    SupplySingle phaseThree PhaseThree PhaseThree PhaseThree PhaseThree Phase
    Power1 kW2.5 kW7 kW5.3 kW7 kW8 kW
    Quantity daily
    maximum affinabile * (kg / 9h)
    3 Kg6 Kg12 Kg20 Kg22 Kg32 Kg
    Overall Dimensions (mm)Lung:1100
    Prof:700
    Alt:2000
    Lung:1300
    Prof:2400
    Alt:2545
    Lung:1300
    Prof:2400
    Alt:2545
    Lung:1300
    Prof:3450
    Alt:2550
    Lung:5000
    Prof:3300
    Alt:2550
    Lung:5000
    Prof:3300
    Alt:2550
    Weight85 Kg290 Kg550 Kg450 Kg500 Kg500 Kg













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