Aeration-enhanced leaching mechanism and kinetics for column bioleaching of copper sulfide ores

IF 2.4 4区 生物学 Q3 BIOTECHNOLOGY & APPLIED MICROBIOLOGY
Mingqing Huang, Jia-wei Li, Ming Zhang, Zhao-lan Li
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Abstract

BACKGROUND

Artificial aeration plays a pivotal role in the bioleaching of sulfide ores by influencing microbial activity, oxygen supply, and mineral dissolution kinetics. However, the quantitative relationship between aeration rate and leaching efficiency for low-grade copper sulfide ores, particularly under column leaching conditions, remains insufficiently characterized.

RESULTS

Through systematic column leaching experiments conducted at 30–45 °C with aeration rates ranging from 0 to 150 L h−1, we observed that the Cu recovery rate throughout bioleaching was not entirely positively correlated with the aeration rate. Column leaching performance at 95 L h−1 aeration rate is comparable to that at 110–150 L h−1 in the initial leaching phase. By the end of leaching, Cu recovery rate reaches 80.1% at 150 L h−1 aeration rate, which is an increase of 11.4% from the 68.7% achieved without forced aeration. Analysis of the leaching mechanism indicates that artificial aeration (>95 L h−1) enhances the positive cycle among factors such as leaching microorganisms, Fe2+ and Fe3+, while also improving the temperature and pore structure of the leaching system.

CONCLUSION

These findings provide both fundamental insights and practical tools for industrial applications. The identified aeration threshold of 95 L h−1 offers a cost-effective operational target, while the validated oxygen demand model serves as a predictive framework for scaling up bioleaching processes. This work advances the scientific understanding of aeration effects in bioleaching systems and enables more efficient design of industrial heap leaching operations through optimized oxygen management strategies. © 2025 Society of Chemical Industry (SCI).

Abstract Image

Abstract Image

硫化铜矿柱式生物浸出曝气强化浸出机理及动力学研究
人工曝气通过影响微生物活动、供氧和矿物溶解动力学,在硫化物矿石的生物浸出中起着关键作用。然而,对于低品位硫化铜矿石,特别是在柱式浸出条件下,曝气速率与浸出效率之间的定量关系还没有得到充分的表征。结果通过在30-45℃、曝气速率0 ~ 150 L h−1条件下进行的系统柱浸实验,我们观察到整个生物浸出过程中Cu的回收率与曝气速率不完全正相关。95 L h−1曝气速率下的柱浸效果与初始阶段110 ~ 150 L h−1的柱浸效果相当。浸出结束时,当曝气率为150 L h−1时,铜回收率达到80.1%,比未强制曝气时的68.7%提高了11.4%。浸出机理分析表明,人工曝气(>95 L h−1)增强了浸出微生物、Fe2+、Fe3+等因子之间的正向循环,同时也改善了浸出系统的温度和孔隙结构。结论本研究结果为工业应用提供了基础见解和实用工具。确定的曝气阈值为95 L h−1,提供了一个具有成本效益的操作目标,而经过验证的需氧量模型可作为扩大生物浸出过程的预测框架。这项工作推进了对生物浸出系统曝气效果的科学理解,并通过优化氧气管理策略,使工业堆浸操作的设计更有效。©2025化学工业学会(SCI)。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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来源期刊
CiteScore
7.00
自引率
5.90%
发文量
268
审稿时长
1.7 months
期刊介绍: Journal of Chemical Technology and Biotechnology(JCTB) is an international, inter-disciplinary peer-reviewed journal concerned with the application of scientific discoveries and advancements in chemical and biological technology that aim towards economically and environmentally sustainable industrial processes.
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