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廢覆銅板分選殘渣生物脫毒工藝優化及機理

Cu extraction from waste copper clad laminate sorting residue in a two-stage bioleaching process: Process optimization and mechanism

  • 摘要: 廢覆銅板分選殘渣量大,殘留銅質量分數約為1%,潛在利用價值高。為了獲得廢覆銅板分選殘渣生物浸出脫毒工藝最優條件及探明其生物浸出相關機理,首先采用Box?Behnken響應曲面法設計三因素(參數因子包括初始pH值、固形物含量和Fe2+濃度;響應值為銅浸出率)三水平共計17個實驗的優化實驗方案。響應面多項回歸擬合分析指出:銅浸出率回歸模型與實際試驗擬合性較好,實驗誤差較小,對廢覆銅板分選殘渣中銅生物浸出過程優化具有一定參考性。在最優化條件下(初始pH值為 1.65、廢覆銅板分選殘渣投加量300 g·L?1和Fe2+質量濃度為6.13 g·L?1)經過4 h生物浸出獲得(92.2±0.27)%的銅浸出率。其次,廢覆銅板殘渣生物浸出脫毒放大改進實驗中(100 L攪拌槽):增加曝氣和攪拌,同時外加酸調控體系pH值<2.5,延長浸出至6 h,銅最大浸出率>98%,浸出渣中銅殘留質量分數≤0.02%。未反應縮核動力學模型顯示殘渣中銅生物浸出過程受界面傳質和固體膜層內擴散混合控制。綜上所述,廢覆銅板分選殘渣中的銅主要通過Fe3+氧化和H+攻擊溶出;嗜酸氧化亞鐵微生物持續氧化Fe2+→Fe3+,不僅降低了總鐵消耗量,也促進了殘渣中銅的釋放。研究結果將為廢舊電子電器綠色資源化再生利用提供理論支撐。

     

    Abstract: Much waste copper clad laminate sorting residue is generated from the flotation process of recovering copper resources from waste printed circuit boards. The improper treatment and disposal of waste copper clad laminate sorting residue harms the environment and human health. According to the National Hazardous Waste List (2021 edition) of China, this waste belongs to HW13 (900-451-13) hazardous waste. The sorting residue contains approximately 1% copper, which is similar to the average copper grade of 0.8% in China. Therefore, this residue is an important copper renewable resource and has a high potential for copper recycling. To optimize the effective factors, including the Fe2+ concentration, initial solution pH value, and pulp density, and clarify the mechanism during the bioleaching process of waste copper clad laminate sorting residue, a Box–Behnken design of response surface methodology was first used, and a scheme consisting of 17 experiments was designed in the present study. Through the multiple regression fitting analysis of experimental results, a quadratic polynomial regression model was established. The regression model showed high reliability and simulation accuracy and was then used to optimize the bioleaching process. Under the optimal conditions (6.13 g·L?1 Fe2+, initial leaching solution pH value of 1.65, and pulp density of 30%), 92.2% maximum Cu extraction was obtained. Then, a modified scale-up bioleaching experiment in a 100-L stirred tank was performed. The results indicated that the maximum copper recovery reached 98%, and less than 0.02% of copper was detected in the bioleaching residue after 6 h of bioleaching because of the improved bioleaching operating conditions in the 100-L stirred tank, including slowly adding the sorting residue, additional stirring (200 r·min?1), aerating (20 L·h?1), and controlling the bulk pH value (solution pH value <2.5 adjusted with 50% (v/v) H2SO4). Leaching kinetic data described by a modi?ed shrinking core model indicated that interfacial transfer and diffusion across the solid ?lm layer controlled the copper dissolution kinetics. In conclusion, copper in the sorting residue was dissolved primarily by Fe3+ oxidation and secondarily by H+ attack throughout the bioleaching process. Notably, the continuous regeneration of Fe3+ by an iron-oxidation microbial consortium led to more Fe3+ distributed across the solid film layer of residual iron/calcium compounds and accumulated on the reacted core, which not only reduced total iron consumption (particularly Fe3+) but also substantially improved copper extraction from waste copper clad laminate sorting residue. These findings should have important implications for the green recycling and reuse of waste printed circuit boards and other waste electronic appliances.

     

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