IDEAL OPERATIONAL PARAMETERS OF TIN SMELTING FURNACES - J1 FACTOR
L. R. Jaccard
ANTECEDENTS
We verified that the C3 equations ( I = C3 . P2/3 and V = P1/3 / C3 ), commonly used to define the submerged arc ideal parameters, are wrong.
Based on theoretical principles, confirmed by experiences made in cassiterite reduction furnaces, we concluded that, for a determined electrode spacing, the voltage that promotes the electrode ideal position is a function of the electrodes diameter and the active power: V = J0 . D / P1/4, where D is the electrode diameter, P is the active power and J0 is a factor dependent of the processed material and electrode space.
It was also suggested that, inside a certain range, the ideal voltage is proportional to the electrode spacing square root: V = J1 . D . S1/2 / P1/4, in which S is the electrode spacing and J1 is a factor proportional to the resistivity of the processed material ( J1 = V . P1/4 / D . S1/2 ).
APPLICATION OF FACTOR J1 TO TIN SMELTING ( CASSITERITE ) FURNACES
During 2005 and 2006 we conducted tests in tin smelting furnaces, varying the active powers between the limits of 400 kW and 1000 kW, changing electrode diameters and sizes. For each operational set of parameters it was verified the energy consumption and the productivity. Also, the factors C3, J0 and J1 were calculated. The experiences showed that the factor C3 equations did not match with reality.
We concluded that for cassiterite reduction furnaces the factor J1 is equal to 0,607, using the following unities:
V ( Volts )
P ( 1 phase, Watts )
D ( cm )
S ( cm )
Practical application of J1 for cassiterite furnaces
For the case of a furnace with certain electrode diameter and space, assuming operation with certain active power:
The ideal voltage between electrode and hearth is: V = 0,607 . D . S1/2 / P1/4
The ideal current is: I = P / V
The unload voltage V0 at the transformer secondary is: V0 = V / cos phi.
Cos phi can be calculated knowing the circuit reactance X and the load resistance R, being tan phi = X / R.
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