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THE ASTER PROCESS: TECHNOLOGY DEVELOPMENT THROUGH TO PILOTING, DEMONSTRATION AND COMMERCIALIZATION

机译:艾斯特流程:技术开发通过试验,演示和商业化

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Environmental legislation associated with the land disposal of cyanidation tailings and water discharge is becoming increasingly stringent world-wide, thus enforcing the treatment or recycling of contaminated water streams. Furthermore, micro organisms used in the bioleaching of sulphide minerals in particular, have a low tolerance to thiocyanate and cyanide species making the recycle of contaminated process water to BIOX? plants impossible. It is predominantly the reaction between residual cyanide and reactive sulphur species which results in the formation of SCN" up to ~ 5000 mg/L, which renders the upstream recycling of this solution impractical.The delivery therefore of an improved and integrated water mass balance for subsequent upstream re-usage in BIOX? applications saw the development of the ASTER process, viz., the Activated Sludge Tailings Effluent Remediation process.Laboratory and pilot scale testing of the ASTER process in batch flasks and continuous fed reactors at scales of 0.08, 0.8, 2, 6 and 25m3 showed batch degradation rates of approximately 75 mg/L/hr SCN" was attainable at 25°C, while up to 87 mg/L/hr (un-optimised) SCN" (corresponding to +66% removal) was attainable in the first stage reactor. These derived degradation rates corresponded to batch start test SCN" concentrations of 1800 mg/L and continuous fed reactor feed concentrations of ~ 2100 mg/L respectively.The success and process robustness demonstrated during various pilot runs, on different mine tailings solutions prompted Barberton Mines in the Mpumalanga province of South Africa to go ahead with a full scale ASTER plant in 2009. The plant was designed to treat tailings dam solution at their Consort plant for concentrate preparation to be fed to their BIOX? plant. To facilitate the fundamental process aspects, a development program between Gold Fields and the University of Cape Town (UCT) was initiated which draws on advanced microbiological analyses and sequencing techniques. The first phase focuses on optimising the process conditions and effects of heavy metals and cyanide, and a second more fundamental phase involves modelling and characterisation of the microbial consortium.The Consort ASTER commercial plant has a capacity of 320 m~3/d tailings solution, a design retention time of 12 hours with feed SCN" and free CN" concentrations of 120 mg/L and 30 mg/L respectively. To date the plant has been performing well with degradations in excess of 99% being achieved.This paper discusses the development of the ASTER process through to its first commercialisation at the Barberton Mines, Consort plant. Finally, a further two case studies is described showing how the ASTER process is developing to support projects in the Philippines and Australia.
机译:与氰化尾矿和排水的土地处理相关的环境立法正在全球越来越严格,因此加强了污染的水流的治疗或回收。此外,特别是在硫化矿物的生物浸出中使用的微生物,对硫代氰酸酯和氰化物物种具有低耐受性,使得污染的工艺水循环到Biox?植物不可能。它主要是残留氰化物和反应性硫物质之间的反应,这导致SCN“高达约〜5000mg / L的反应,这使得该解决方案的上游再循环是不切实际的。因此,递送改善和综合水质平衡在Biox中的后游重新使用?应用程序看到了ASTER过程的开发,即激活的污泥尾矿流出物修复过程。在批量烧瓶中的Aster过程和连续馈电反应器的制造性和试验规模测试0.08,0.8在25℃下,2,6和25m 3显示出约75mg / l / hr / hr scN“的批量降解速率,而最高可达87mg / l / hr(未优化)scn”(对应于+ 66%的去除)可在第一阶段反应器中获得。这些衍生的降解率与分批开始试验SCN“1800mg / L的浓度”分别为2100mg / L的连续供给反应器饲料浓度。成功和过程鲁棒性DEM在各种飞行员运行过程中,在不同的矿山尾矿解决方案促使南非普马兰加省麦卢兰加省的麦芽尔顿矿山,于2009年继续全面翠菊厂。该工厂旨在将尾矿坝溶液在其聚会厂进行矿物厂,以浓缩植物,以浓缩制剂喂养他们的生物蛋吗?植物。为促进基本流程方面,启动了黄金领域和开普敦大学(UCT)之间的发展计划,涉及先进的微生物分析和测序技术。第一阶段侧重于优化重金属和氰化物的过程条件和影响,第二个更基本的阶段涉及微生物联盟的建模和表征。联盟艾斯特商业设备的容量为320米〜3 / d尾矿溶液, 12小时的设计保留时间为12小时,进料SCN“和FREC CN”浓度分别为120mg / L和30mg / L.迄今为止,该工厂的表现良好,降低超过99%。本文讨论了艾斯特流程的发展,通过在Barberton Mines,Consort工厂的首次商业化。最后,描述了另外两种案例研究,展示了艾斯特过程如何发展以支持菲律宾和澳大利亚的项目。

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