Biotechnological Recovery of Zinc from Low-Grade Sulfide Concentrate during Two-Step Processing

M. Muravyov
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Abstract

Extended Abstract Biohydrometallurgical processes are based on leaching of nonferrous metals from sulfidic ores and concentrates in ferric iron containing sulfuric acid media with application of acidophilic chemolithotrophic microorganisms. Bioleaching of sulfide sources is used for decades around the world for recovery of metals [1]. Biohydrometallurgy has many advantages over conventional chemical hydrometallurgy and pyrometallurgy that include (i) lower cost, (ii) low environmental impact, (iii) generation of less hazardous waste, and (iv) no need for toxic chemicals and high energy. The environmental benefits of biohydrometallurgical processing of copper-zinc concentrates based on the use of acidophilic microorganisms were previously shown [2, 3]. Zinc concentrates produced from polymetallic sulfide ores of the Urals region (Russia) by flotation methods contain large amounts of iron and copper. Their further processing at metallurgical enterprises is therefore accompanied by significant losses of nonferrous metals in slags. Metal leaching from sulfides at elevated temperatures, using ferric sulfate solutions generated during biooxidation with acidophilic microorganisms (two-step process), can be promising for processing of the low-grade zinc concentrates. A flotation sulfide concentrate used in this study contained 43.3% of zinc, 2.03% of copper, and 13.6% of iron. The main minerals of the concentrate were sphalerite, pyrrhotite, and chalcopyrite. Ferric leaching during 14.3 hours at 80 °C, pH of 1.3, initial Fe concentration of 25 g/L, pulp density of 10% allowed to recover 92.3% of zinc and 51.6% of copper into the aqueous phase. Biooxidation of the ferric leaching products (leach solution and leach residue) during 21 days under batch conditions at 40 °C, pH of 0.6–2.0, pulp density of 10% by consortium of acidophilic microorganisms containing Acidithibacillus caldus, Leptospirillum ferriphilum, Ferroplasma acidiphilum, Sulfobacillus thermotolerans, S. thermosulfidooxidans, and Cuniculiplasma sp. led to an increase in zinc and copper recoveries up to 98.6 and 69.0%, respectively. The biooxidation residue was mainly composed of jarosite and gypsum and contained 0.52% of zinc, 0.55% of copper, and 0.40% of elemental sulfur. Therefore, this residue can be considered inert dump waste. The final oxidation levels (compared to the original concentrate) of pyrrhotite and sphalerite reached the highest values among sulfide minerals since these minerals have low rest potentials in comparison with chalcopyrite. Chalcopyrite is normally highly refractory to biooxidation in acidic media containing ferric iron. The ferrous iron in the leach solution can also be oxidized within 4 days by the same consortium of microorganisms at the pulp density of 1%. It allows to bioregenerate the oxidizer more rapidly for the ferric leaching step. Therefore, the two-step processing of low-grade zinc sulfide concentrate based on biohydrometallurgical approach was found to be effective for recovery of metals.
低品位硫化物精矿二步法生物回收锌的研究
生物湿法冶金工艺是利用嗜酸化化岩石营养微生物从含硫酸的含铁矿石和精矿中浸出有色金属。硫化物源的生物浸出在世界范围内用于金属回收已有几十年的历史[1]。与传统的化学湿法冶金和火法冶金相比,生物湿法冶金有许多优点,包括:(1)成本较低;(2)对环境的影响较小;(3)产生的有害废物较少;(4)不需要有毒化学品和高能量。基于嗜酸微生物的生物湿法冶金处理铜锌精矿的环境效益先前已被证明[2,3]。从乌拉尔地区(俄罗斯)的多金属硫化物矿石中采用浮选方法生产的锌精矿含有大量的铁和铜。因此,在冶金企业中,它们的进一步加工伴随着矿渣中有色金属的大量损失。在高温下,利用嗜酸微生物生物氧化过程中产生的硫酸铁溶液(两步法)从硫化物中浸出金属,可用于处理低品位锌精矿。本研究中使用的硫化浮选精矿含锌43.3%,铜2.03%,铁13.6%。精矿主要矿物为闪锌矿、磁黄铁矿和黄铜矿。在80℃、pH = 1.3、初始铁浓度为25 g/L、矿浆密度为10%的条件下,经过14.3小时的铁浸出,可回收92.3%的锌和51.6%的铜进入水相。铁浸出产物(浸出液和浸出渣)在40℃、pH为0.6-2.0、矿浆密度为10%的批处理条件下,由嗜酸硫杆菌、嗜铁细螺旋体、嗜酸铁原体、耐高温硫杆菌、嗜硫硫杆菌和cuuniculiplasma等嗜酸微生物联合进行21天的生物氧化,锌和铜的回收率分别达到98.6%和69.0%。生物氧化渣主要由黄钾铁矾和石膏组成,含锌0.52%、铜0.55%、单质硫0.40%。因此,这种残留物可视为惰性倾倒废物。磁黄铁矿和闪锌矿的最终氧化水平(与原始精矿相比)在硫化矿物中达到最高值,因为这些矿物与黄铜矿相比具有较低的静止电位。黄铜矿在含铁的酸性介质中通常高度难氧化。在矿浆浓度为1%的条件下,浸出液中的亚铁也可以在4天内被同一群微生物氧化。它允许在铁浸出步骤中更快地对氧化剂进行生物再生。因此,采用生物湿法两步法处理低品位硫化锌精矿是回收金属的有效方法。
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