A kind of recycling method of electrode foil corrosion waste sulfuric acid
A waste sulfuric acid and electrode foil technology, which is applied to aluminum sulfate, chemical instruments and methods, sulfur trioxide/sulfuric acid, etc., can solve the problems of resource waste, high cost, and environmental pollution, and achieve improved recovery efficiency, long equipment life, No secondary pollution effect
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Embodiment 1
[0031] The recycling method of electrode foil corrosion waste sulfuric acid of the present invention, concrete steps are as follows: its technological process is as follows figure 1 Shown:
[0032] (1) Preheating: the electrode foil corrosion waste acid from the waste sulfuric acid storage tank is pumped into the preheater for preheating, in which the uncondensed steam and concentrated high temperature produced by the two-effect three-stage Acid is the heat source for preheating;
[0033] (2), evaporation:
[0034] One-effect evaporation: the waste acid enters the first-effect evaporation tower, uses the heat provided by the steam pipe network, controls the evaporation temperature between 90-100°C, and controls the pressure at 70-100KPa for evaporation, and the evaporated steam is used as secondary steam to the second effect heat supply, and the remaining materials enter the second-effect evaporation tower;
[0035] Two-effect evaporation: Use the heat generated by the firs...
Embodiment 2
[0047] The recycling method of electrode foil corrosion waste sulfuric acid of the present invention, concrete steps are as follows: its technological process is as follows figure 1 Shown:
[0048] (1) Preheating: the electrode foil corrosion waste acid from the waste sulfuric acid storage tank is pumped into the preheater for preheating, in which the uncondensed steam and concentrated high temperature produced by the two-effect three-stage Acid is the heat source for preheating;
[0049] (2), evaporation:
[0050] One-effect evaporation: the waste acid enters the first-effect evaporation tower, uses the heat provided by the steam pipe network, controls the evaporation temperature between 90-100°C, and controls the pressure at 70-100KPa for evaporation, and the evaporated steam is used as secondary steam to the second effect heat supply, and the remaining materials enter the second-effect evaporation tower;
[0051] Two-effect evaporation: Use the heat of the first-effect e...
Embodiment 3
[0063] The recycling method of electrode foil corrosion waste sulfuric acid of the present invention, concrete steps are as follows: its technological process is as follows figure 1 Shown:
[0064] (1) Preheating: the electrode foil corrosion waste acid from the waste sulfuric acid storage tank is pumped into the preheater for preheating, in which the uncondensed steam and concentrated high temperature produced by the two-effect three-stage Acid is the heat source for preheating;
[0065] (2), evaporation:
[0066] One-effect evaporation: the waste acid enters the first-effect evaporation tower, uses the heat provided by the steam pipe network, controls the evaporation temperature between 90-100°C, and controls the pressure at 70-100KPa for evaporation, and the evaporated steam is used as secondary steam to the second effect heat supply, and the remaining materials enter the second-effect evaporation tower;
[0067] Two-effect evaporation: Use the heat of the first-effect e...
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