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Influence of dissolved oxygen on the bioleaching efficiency of a mesophile to moderate thermophile consortium under oxygen enriched atmosphere

机译:溶解氧对富含氧气气氛下嗜渗嗜硒骨生物浸出效率的影响

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The use of oxygen is a well-known practice in high-temperature bioleaching reactors whereas air is usually preferred in medium and low-temperature operations due to economic constraints. Under high-sulfide loading conditions, as it is the case with high-grade metal sulfide concentrates, the microbial and chemical demand for oxygen is significantly increased during the bioleaching process, which requires the injection of large amounts of air and thus increases the energy costs of the process. Sparging with oxygen enriched gas instead of air may offer an interesting alternative process option to improve gas transfer in the bioleaching reactor and to provide an adequate oxygen supply in order to satisfy the oxygen demand. However the use of such conditions can lead to much higher dissolved oxygen (DO) concentrations than those encountered with air sparging. Very few papers have been devoted to the study of the optimal range of DO concentrations for bioleaching processes. However most of them reported an inhibitory effect of DO concentrations above 5 ppm. The purpose of this study was to investigate the influence of DO on the bioleaching efficiency under oxygen-enriched atmosphere in 21L stirred tank reactor at 42°C. Bioleaching experiments were performed in continuous mode on a sulfide-rich tailings wastes composed mainly of pyrite (51%) and quartz using the "BRGM-KCC" bacterial consortia. The solid load was closed to 20% (w/w). The DO concentration in the reactor was varied between 4 and 17 ppm. For a DO ranging from 4 to 13 ppm the results obtained show a good bacterial oxidizing activity, no inhibitory effect of the DO was observed and the sulfide dissolution increased with the DO concentration. It is assumed that this improvement of the bioleaching efficiency was linked to an increase of the oxygen transfer rate from the gas phase to the liquid phase rather than a direct effect of the DO level. When the DO concentration reached 17 ppm a significant decrease of the microbial activity and consequently of the oxygen consumption was noticed. This results show that there is a critical value above which the DO concentration is detrimental to the activity of the bioleach microorganisms present in the "BRGM-KCC" consortia but this value is much higher than the one usually mentioned in the literature.
机译:氧气的使用是高温生物浸入反应器中的众所周知的实践,而由于经济限制,空气通常优选在培养基和低温操作中。在高硫化物装载情况下,因为它与高档金属硫化物的浓缩物的情况下,微生物和对氧的化学需求显著在生物浸出过程,这需要大量空气的喷射增加,并且因此增加了能量成本这个过程。使用富氧气体而不是空气喷射可以提供有趣的替代方法选择,以改善生物浸出反应器中的气体转移,并提供足够的氧气供应,以满足氧气需求。然而,这种条件的使用可以导致比空气喷射的溶解氧(DO)浓度更高。很少有篇章已经致力于研究生物浸出过程的最佳浓度范围。然而,他们中的大多数报道了在5ppm以上的浓度的抑制作用。本研究的目的是研究在42℃下在21L搅拌槽反应器中富氧气氛下对生物浸入效率的影响。在使用“BRGM-KCC”细菌组织的硫化物 - 富含硫化物尾矿废物上以连续模式进行生物浸出实验,其主要由黄铁矿(51%)和石英组成。固体载荷关闭至20%(w / w)。反应器中的浓度在4至17ppm之间变化。对于4至13ppm的实用性,获得的结果显示出良好的细菌氧化活性,未观察到抑制作用,并且硫化物溶解随浓度的增加而增加。假设这种改善的生物浸入效率与来自气相的氧转移速率的增加与液相而不是直接效应的脂肪率。当DO浓度达到17ppm时,注意到微生物活性的显着降低,并且因此被注意到氧气消耗。这个结果表明,有在其上方的DO浓度是不利的存在于“BRGM-KCC”财团生物浸出微生物的活性的临界值,但该值是比平常在文献中提到的高得多。

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