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Combined method for electrolyzing and recovering lead

A technology of electrolytic recovery and electrolytic method, which is applied in the field of electrolytic recovery of lead, can solve the problems of large power consumption, long time-consuming pre-oxidation and reduction reaction process, and large corrosiveness of equipment to achieve the effect of industrialization

Active Publication Date: 2012-03-07
BEIJING UNIV OF CHEM TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0007] Although the advantage of this type of process is that it can directly obtain electrolytic lead, the serious shortcomings of this type of process itself have seriously restricted the industrial application of these processes, and the described shortcomings generally include the following points:
[0008] 1. The pre-redox reaction process takes a long time and consumes a lot of Pb, Fe and SO 2 Such reducing agents and sulfuric acid not only increase the cost of this step, but also increase the processing cost of subsequent alkaline desulfurization;
[0009] 2. The power consumption is relatively high. The voltage of the electrolyzer in the electrolysis process is 2.7-3.2V, and the energy consumption per ton of lead is generally about 700-950KWh;
[0010] 3. There is a relatively high concentration of lead ions remaining in the pre-oxidation reduction process and electrolytic waste liquid, which is not only highly corrosive to equipment, but also highly toxic to the environment;
[0011] 4. A large amount of lead dioxide by-products are precipitated during the electrolysis process of the anode, which reduces the recovery efficiency of lead and leads to a large load of secondary reduction treatment
[0021] 1. In the pretreatment step of lead recovery, it is often necessary to consume a large amount of reducing agent and a large amount of alkaline substances to desulfurize the sulfur-containing compounds in lead, which greatly increases the process cost; and
[0022] 2. The lead recovery process still consumes a lot of electricity

Method used

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  • Combined method for electrolyzing and recovering lead
  • Combined method for electrolyzing and recovering lead
  • Combined method for electrolyzing and recovering lead

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0105] The 12V, 10AH waste lead-acid batteries sold on the market were crushed and separated to obtain 2.6kg of lead paste. Get wherein 200 grams of lead plaster and wash with 150ml deionized water and filter to obtain 2% (wt.) dilute sulfuric acid and 196 grams of lead plaster. Then the lead paste and 1 liter of 10M NaOH were subjected to alkaline desulfurization reaction at 95°C. After keeping the reaction time for 1.5h, hot filtration was performed immediately to obtain 1 liter of NaOH solution containing 70g / LPbO and 95 grams of Pb and PbO 2 solid mixture.

[0106] The lead-containing mother liquor enters the electrolytic cell for ionic membrane electrolysis after conventional standing and purification. First, constant current electrolysis is carried out in the electrolytic cell, and the current density of the cathode and anode is controlled to be 700A / m 2 , the electrolysis temperature is 90°C, and the electrolysis voltage is 1.44V. When the electrolysis time reaches 1...

Embodiment 2

[0110] Take a 12V, 45Ah waste lead-acid battery for automobiles, and the total weight of the battery pack is 13.2 kg. Use conventional mechanical methods to crush and separate waste batteries to obtain lead paste, grids, separators and plastics.

[0111] Get about 5.9 kg of lead plaster and 5 liters of 2% dilute sulfuric acid after washing with 6 kg of lead plaster powder obtained in the above process and 5 liters of deionized water.

[0112] The lead plaster obtained by solid-liquid separation and 27 liters of 10.5M NaOH were subjected to alkaline desulfurization reaction at 100°C. After keeping the reaction time for 1.0h, they were immediately filtered while hot to obtain 28 liters of NaOH solution containing 75g / L PbO and 2.8 kg contains Pb and PbO 2 solid mixture.

[0113] The alkaline solution containing 75g / L lead oxide obtained by the above process is injected into the cathode chamber of the ion-exchange membrane (Nafion982) electrolyzer, and the anode chamber is then...

Embodiment 3

[0117] From the 12V, 14Ah lead-acid battery workshop, 13 kg of scrap negative plates mixed with waste lead-acid battery positive plates were obtained. After the waste battery plates were crushed, about 10 kg of lead powder was obtained, and the main components were Pb and PbSO in the electrodes themselves. 4 , PbO and a small amount of PbO 2 .

[0118] Get about 10 kilograms of lead plaster powder and 5 liters of 0.2% dilute sulfuric acid after washing the 10 kilograms of lead plaster powder obtained in the above process and 5 liters of deionized water.

[0119] The lead plaster obtained by solid-liquid separation and 50 liters of 11M NaOH were subjected to alkaline desulfurization reaction at 100°C. After keeping the reaction time for 1.0h, they were immediately filtered while hot to obtain about 50 liters of NaOH solution containing 89g / L PbO and 3.7 kg contains Pb and PbO 2 solid mixture.

[0120] The alkaline solution containing 89g / L lead oxide obtained by the above pr...

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Abstract

The invention provides a method for electrolyzing and recovering lead from lead plaster, which comprises the following steps: 1) washing the lead plaster by deionized water and performing solid-liquid separation to obtain a mixture of lead sulphate, lead and lead dioxide as well as a dilute sulphuric acid solution; 2) reacting the solution and excessive NaOH solution, and performing a second solid-liquid separation to obtain a mixed solution containing Na2[Pb(OH)4] and sodium hydroxide, and a solid mixture containing Pb and PbO2; 3) performing phase-divided electrolysis containing a constant current electrolytic phase and a constant voltage electrolytic phase to the mixed solution composed of Na2[Pb(OH)4] and sodium hydroxide in an ion-exchange membrane electrolyzer for recovering pure lead; and 4) electrolyzing a mixture of lead and lead dioxide by constant current controlled by using two-phase voltage, and combining electrolytic deposition to recover pure lead. The combined method for electrolyzing and recovering lead is capable of substantially minimizing the recovery of reducing agent, alkaline matter and lead consumed by electric energy, and raising purity of the recovered lead.

Description

technical field [0001] The invention belongs to the technical field of lead recovery by electrolysis. The invention relates to a method for recovering lead from waste battery lead paste by electrolysis. The method pretreats and separates the lead substance in the waste battery lead paste and the compounds containing lead in different valence states, and then according to the lead Different valence states adopt different electrolysis methods for joint electrolysis to realize the recovery of high-purity metallic lead. Background technique [0002] The regeneration and recycling of resources is the key to the sustainable development of human society and an important way to reduce environmental pollution. Lead-acid battery, as a battery with cheap price, mature technology and stable performance, has been widely used in electric vehicles, automobiles and energy storage power sources since it was invented by Plante in France in 1859. Although lead-acid batteries are facing compe...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C25C1/18
CPCY02P10/20
Inventor 潘军青孙艳芝伊晓波
Owner BEIJING UNIV OF CHEM TECH
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