Desulfurization process for waste material containing lead sulfate and circulation method of desulfurization mother liquor thereof
A desulfurization process, technology containing sulfuric acid, applied in the direction of improving process efficiency, etc., can solve the problems of aggravating lead and sulfur dioxide pollution, and achieve the effect of reducing lead pollution and mild process conditions
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Embodiment 1
[0033] Commercially available Fengfan valve-regulated sealed lead-acid batteries with specifications of 12V and 55Ah were crushed and separated to obtain lead paste and waste sulfuric acid solution. According to the traditional chemical titration analysis of the lead paste, the lead-containing components and contents thereof are respectively 9.8% of Pb, 15.6% of PbO, 15.6% of PbO 2 content of 33.7% and PbSO 4 The content is 39.8%. Then the lead paste is subjected to desulfurization reaction, and the treatment process is as follows:
[0034] (1) Weigh 1.0kg of lead paste and add it to a 10L leaching reactor, and add 5L of NH with a concentration of 10mol / L to the reactor 3 ·H 2 O and 2mol / L (NH 4 ) 2 SO 4 The solution was stirred and reacted at a constant temperature of 30° C. for 25 minutes, and the stirring rate was 150 rpm. Carry out solid-liquid separation to obtain the filtrate and unreacted filter residue of the complex of dissolved lead sulfate;
[0035] (2) tran...
Embodiment 2
[0040] Take 1 kg of lead-containing flue ash from Anyang Minshan Smelter, and analyze it by chemical titration to obtain its PbSO 4 The content is 63.5%, and the balance is iron oxide, silicon dioxide and clay. Then the flue ash will be subjected to desulfurization reaction, the treatment process is as follows:
[0041] (1) Add 1.0kg of flue ash to a 10L leaching reactor, and add 5L of NH with a concentration of 12mol / L to the reactor 3 ·H 2 O and 1mol / L (NH 4 ) 2 SO 4 solution, and added 0.1 kg of glycine as a leaching accelerator, stirred and reacted at a constant temperature of 40° C. for 15 minutes, and the stirring rate was 100 rpm. Carry out solid-liquid separation to obtain the filtrate and unreacted filter residue of the complex of dissolved lead sulfate;
[0042] (2) transfer the lead sulfate complex solution obtained above to the closed carbonization reactor, and feed CO 2 , the control pressure is 0.02MPa, the flow rate is 4L / min, the reaction temperature is ...
Embodiment 3
[0047] Get the same 1 kg of lead-containing flue ash from Minshan Smelter in Anyang as in Example 2 and the desulfurization circulating liquid recovered in Example 2 step (3). Its processing is as follows:
[0048] (1) Add the above-mentioned 1.0kg of flue ash into a 10L leaching reactor, add the desulfurization circulating liquid recovered in step (3) into the reactor, stir and react at a constant temperature of 40°C for 15min, and the stirring rate is 100rpm. Carry out solid-liquid separation to obtain the filtrate and unreacted filter residue of the complex of dissolved lead sulfate;
[0049] (2) transfer the lead sulfate complex solution obtained above to the closed carbonization reactor, and feed CO 2 , the control pressure is 0.015MPa, the flow rate is 4L / min, the reaction temperature is 50°C and the stirring rate is 200rpm, so that the dissolved lead sulfate is transformed into lead carbonate precipitate. Stir continuously for 20 min until no more precipitation occurs...
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