Production technology for preparing polyferric chloride coagulant from seamless steel pipe acid-washing waste liquid
A ferric chloride-based, pickling waste liquid technology, applied in the direction of ferric halides, etc., can solve the problems of high energy consumption, and achieve the effects of low energy consumption, complete reaction, and good stability
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[0027] Example 1
[0028] Settling and filtering 4000 kilograms of seamless steel pipe pickling waste liquid, pumping it into a 6 cubic meter enamel acid-resistant reactor with an acid-proof pump, adding 1000 kilograms of industrial hydrochloric acid (36wt%), and adjusting the HCl content in the solution to 10wt%; start Stir, control the stirring speed to 60 rpm, add 25 kg of 36wt% nitric acid (0.5wt% of the total reaction solution) as a catalyst at room temperature; blow in air at a rate of 3 liters / min, and oxidize for 6 hours; then add 250 kg of trichloroisocyanuric acid (5w% of the total reaction liquid), continue the oxidation reaction for 3 hours, the air ventilation rate is 1,440 liters per ton of the reaction liquid; after the oxidation reaction, add 25 kg (accounting for the total reaction liquid 0.5w%) isopropanolamine as a stabilizer, and the reaction liquid is filtered and transferred to an acid-resistant storage tank to obtain a polyferric chloride coagulant. It is ...
Example Embodiment
[0029] Example 2
[0030] Settling and filtering 4000 kilograms of seamless steel pipe pickling waste liquid, using an acid-proof pump to pump into a 6 cubic meter enamel acid-proof reactor, adding 1000 kilograms of industrial hydrochloric acid (36wt%), control the HCl content in the solution to 10wt%; start Stir, the stirring speed is controlled at 80 rpm, add 36wt% nitric acid 50 kg (1wt% of the total reaction solution) as a catalyst at room temperature; oxygen gas is introduced at a rate of 2 liters / min for oxidation reaction for 6 hours; then 250 kg are added Trichloroisocyanuric acid (5wt% of the total reaction liquid) continues the oxidation reaction for 3 hours, the oxygen ventilation rate is 960 liters per ton of the reaction liquid; after the oxidation reaction, add 25 kg (0.5wt% of the total reaction liquid ) Isopropanolamine is used as a stabilizer, and the reaction liquid is filtered and transferred to an acid-resistant storage tank to obtain a polyferric chloride coa...
Example Embodiment
[0031] Example 3
[0032] Settling and filtering 4000 kilograms of seamless steel pipe pickling waste liquid, using an acid-proof pump to pump into a 6 cubic meter enamel acid-proof reactor, adding 1000 kilograms of industrial hydrochloric acid (36wt%), control the HCl content in the solution to 10wt%; start Stir, the stirring speed is controlled at 80 revolutions / min, and 75 kg of 36wt% nitric acid (accounting for 1.5wt% of the total reaction liquid) is added as a catalyst at room temperature; oxygen is introduced at a rate of 2 liters / min for oxidation reaction for 6 hours; then 150 is added Kg of trichloroisocyanuric acid (3wt% of the total reaction liquid) continues the oxidation reaction for 3 hours, the oxygen ventilation rate is 960 liters per ton of the reaction liquid; add 25 kg (0.5wt% of the total reaction liquid) isopropanol Amine acts as a stabilizer, after filtering, the reaction solution is transferred to an acid-resistant storage tank to obtain a polyferric chlori...
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