Method for recycling lead-containing waste acid by utilizing adsorption method
A technology of resource utilization and adsorption method, applied in chemical instruments and methods, water/sludge/sewage treatment, water pollutants, etc., can solve the problems of lack of efficient and economically feasible industrialized treatment processes and constraints on sustainable development
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Embodiment 1
[0021] Pack 20ml of pyrrolidone-based adsorption resin into an adsorption column (Φ35×250mm) with a heat preservation jacket.
[0022] Take waste hydrochloric acid with a lead chloride content of 2000mg / L, and use it as the upper column liquid after filtration; then, at 40°C, let the waste hydrochloric acid pass through the resin column at a flow rate of 1.5BV / h, so that the chlorination in the purified waste acid When the lead content is below 30mg / L, the treatment capacity is 5-8BV.
[0023] After the resin is adsorbed and saturated, it is desorbed with 4%-10% aqueous sodium hydroxide solution at a temperature of 20°C and a flow rate of 0.5BV / h.
[0024] Concentrated hydrochloric acid is added to the purified waste acid, and the water purifying agent is obtained after acidification.
[0025] The pH of the desorption waste liquid is adjusted by acid to convert sodium plumbate into lead hydroxide, which can be sold as a by-product after further treatment.
[0026] The pyrrol...
Embodiment 2
[0039] Pack 600ml of pyrrolidone-based adsorption resin into an adsorption column (Φ35×1000mm) with a heat preservation jacket.
[0040] Take the waste acid with a lead chloride content of 1000mg / L, and filter the waste acid as the upper column liquid; then, under the condition of 25°C, let the waste acid pass through the resin column at a flow rate of 0.5BV / h, so that the purified waste acid When the lead chloride content in the medium is below 30mg / L, the treatment capacity is 11-15BV.
[0041] After the resin is adsorbed and saturated, 4%-10% sodium hydroxide aqueous solution is used for desorption at a temperature of 20° C. and a flow rate of 1 BV / h.
[0042] Concentrated hydrochloric acid is added to the purified waste acid, and the water purifying agent is obtained after acidification.
[0043] The pH of the desorption waste liquid is adjusted by acid to convert sodium plumbate into lead hydroxide, which can be sold as a by-product after further treatment.
Embodiment 3
[0045] Pack 600ml of pyrrolidone-based adsorption resin into an adsorption column (Φ35×1000mm) with a heat preservation jacket.
[0046] Take the waste acid with a lead chloride content of 1000mg / L, and the waste acid is filtered as the upper column liquid; then, under the condition of 10°C, the waste acid is passed through the resin column at a flow rate of 3BV / h, so that the purified waste acid When the lead chloride content is below 30mg / L, the treatment capacity is 6-10BV.
[0047] After the resin is adsorbed and saturated, 4%-10% sodium hydroxide aqueous solution is used for desorption at a temperature of 25°C and a flow rate of 2BV / h.
[0048] Concentrated hydrochloric acid is added to the purified waste acid, and the water purifying agent is obtained after acidification.
[0049] The pH of the desorption waste liquid is adjusted by acid to convert sodium plumbate into lead hydroxide, which can be sold as a by-product after further treatment.
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