The concentration of zinc sulfate is directly proportional to the amount of weak zinc hydroxide sulfuric acid. Cementitious sediment is identified. A 3 gram-mol zinc sulfate compound is detected.
The concentration of zinc sulfate is directly proportional to the amount of weak zinc hydroxide sulfuric acid. Cementitious sediment is identified. A 3 gram-mol zinc sulfate compound is detected.
ZnSO4·3Zn(OH)2+4H2O
The solution undergoes the following chemical reaction during the cementation process.
Me SO4+2Zno+H2O=MeO+H2+ZnSO4+Zn(OH)2
View of potential energies between electrodes:
Zn+2H2O=Zn(OH)2+2H+2e Eo=-0,439v
2Sb+3H2O=Sb2O3+6H++6e E0=+0,152v
Cu+H2O=CuO+2H+2e E0=+0,57v
Description of the technological process.
Preparation of solutions and dehydration.
Technical zinc sulfate is produced by evaporating a solution of zinc sulfate in a fluidized bed furnace (BL).
The solution after cementitious purifications from cadmium in the cadmium production is fed to the filter press for filtering. The filtered solution is sent to a filler with a capacity of 70 m3. From the collection container, the gravity solution is periodically poured periodically as necessary into a 20 m3 supply tank. The tank is equipped with a level gauge for measuring the amount of solution. From the supply tank, the olution is pumped to the nozzles and sprayed into the furnace.
containers or paper bags for.
containers or paper bags for.
Start of the BL furnace.
The start of the furnace begins with checking the technical condition of the furnace, the presence of the initial solution, testing all the mechanisms in operation.
The sequence of operations for starting the furnace:
- the furnace is sealed;
- the smoke exhauster is included in the operation and a vacuum is created in the furnace 5-8 mm water column;
- the supercharger is put into operation according to the instructions;
- a gas burner is ignited while supplying primary air. Ignition of a gas burner is carried out in accordance with the operating instructions for the furnace of the furnace to "BL".
- the furnace is heated to a temperature of 600-6500 C;
- secondary air is supplied to create blast elasticity under the hearth, while the air flow is brought up to 6000-9000 m3 / h;
- the temperature under the hearth rises to 780-8000 C;
- a layer is loaded, granular zinc sulfate with a granule size of 3-4 mm in an amount of 2-3 tons is used as a material;
- air consumption increases until the blast elasticity is established under the hearth 800-900 mm and amounts to 10000-12500 m3 / h;
-the temperature in the layer rises to 190-2600 C;
- the pump for supplying the solution to the nozzles starts up.
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