首页> 外文OA文献 >Carbonylation of Nickel and Iron from Reduced Oxides and Laterite Ore
【2h】

Carbonylation of Nickel and Iron from Reduced Oxides and Laterite Ore

机译:还原性氧化物和红土矿石中镍和铁的羰基化

代理获取
本网站仅为用户提供外文OA文献查询和代理获取服务,本网站没有原文。下单后我们将采用程序或人工为您竭诚获取高质量的原文,但由于OA文献来源多样且变更频繁,仍可能出现获取不到、文献不完整或与标题不符等情况,如果获取不到我们将提供退款服务。请知悉。

摘要

Australia has abundant deposits of laterite ores which role in production of nickel is increasing with rising demand for nickel and depletion of sulphide reserves.Laterite ores cannot be efficiently upgraded prior to pyrometallurgical or hydrometallurgical processing what leads to significant challenges in extraction of nickel. The PhD project was undertaken within the ARC (Australian Research Council) Discovery Grant (Project No. DP1094880) which examined a novel approach to processing of laterite ores based on the selective reduction of the ore and extraction of nickel by carbonylation of the selectively reduced ore. Selective reduction of the laterite ore was studied by J. Yang in his PhD project (Yang, 2014). The ultimate aim of this project was to establish the feasibility of extraction of nickel by carbonylation of selectively reduced laterite ore. The project undertook a systematic study of carbonylation of pure nickel and iron, and carbonylation of selectively reduced laterite ore to develop a further understanding of carbonylation reactions and extraction of nickel from laterite ore by carbonylation.Specific objectives of this study included:1) to study the effects of reaction parameters on carbonylation of nickel and iron, including reaction temperature (80-100 °C), carbon monoxide (gauge) pressure (0-56atm), gas flow rate (0.14-0.50 L/min), nickel mass (0.8-3.2g) and particle sizes (0.29 – 2.67 µm), and the effect of sulphur-containing catalysts (sulphur, iron sulphide and hydrogen sulphide);2) to study the non-catalytic and catalytic carbonylation of laterite ores; the impacts of reduction conditions; and effects of reaction parameters;3) to develop further understanding of kinetics and mechanisms of carbonylation processes.Pure metals and nickel-iron mixture were prepared by the reduction of associated oxides by hydrogen at 500 °C (gas flow rate 1.0 L/min); the degree of reduction of oxides was over 98%. Two types of Australian laterite ores supplied by CSIRO were examined (labelled by CSIRO): BCS ore containing 1.35 wt% Ni, 10.4 wt% Fe and 0.038 wt% Co, particle size 53-200 µm; and MIN ore with particle sizes 38-53 µm, 75-90 µm, 140-200 µm, and 355-495 µm, containing 1.68-2.37 wt% Ni, 8.90-11.8 wt% Fe and 0.135-0.144 wt% Co). Selective reduction of laterite ores was conducted by CO-CO2 gas mixture (60 vol% CO) at 750 °C.Carbonylation experiments were conducted in a flexible U – shaped reactor (max pressure 68 atm) immersed into the oil bath. Carbonylation was studied using CO at different pressures. Carbonyls were absorbed by aqua regia in two Dreschel bottles. Samples were taken from the aqua regia solution at different times and analysed by ICP-OES. The extent of carbonylation was calculated using results of the ICP-OES analysis.The non-catalytic carbonylation of nickel at 100 °C and CO pressure 27 atm was close to completion (extent of reaction was 98%) in about 5.5 hours. Carbonylation of pure iron was slow; the extent of iron carbonylation at 100 °C and CO pressure up to 55 atm (gauge) was less than 5.0%. The extent of cobalt carbonylation under these conditions was less than 0.5%.Sulphur containing catalysts accelerated the carbonylation reaction. The time for a complete carbonylation of nickel was shortened from 5.5 hours in the non-catalytic reaction to 2 hours in the catalytic carbonylation at 100 °C and CO pressure 14 atm. The extent of non-catalytic carbonylation of nickel from the selectively reduced BCS laterite ore at 100 °C and CO pressure 41 atm was below 50%. The use of catalysts in the carbonylation of selectively reduced ore was inefficient. The major parameter affecting the rate of ore carbonylation was the particle size. The rate of reaction increased significantly with decreasing particle size; the carbonylation of nickel in MIN ore with the particle size 38-53 and 75-90 µm, was close to completion after 4 hours reaction.Results of a systematic study of the carbonylation of nickel and selectively reduced laterite ores are significant for further understanding of carbonylation reactions. Promising results were obtained for further development of technology of extraction of nickel from laterite ores by the carbonylation process.
机译:澳大利亚有丰富的红土矿床,随着对镍的需求增加和硫化物储量的减少,在镍生产中的作用正在增加。在火法冶金或湿法冶金加工之前,红土矿无法有效地升级,这给镍的提取带来了巨大挑战。该博士项目是在ARC(澳大利亚研究委员会)发现补助金(项目号DP1094880)内进行的,该项目研究了一种基于选择性还原矿石和通过选择性还原矿石的羰基化镍提取镍的红土矿石加工新方法。 。 J. Yang在其博士项目中研究了红土矿石的选择性还原(Yang,2014年)。该项目的最终目的是确定通过选择性还原的红土矿石的羰基化提取镍的可行性。该项目对纯镍和铁的羰基化以及选择性还原的红土矿石的羰基化进行了系统的研究,以进一步了解羰基化反应以及通过羰基化从红土矿石中提取镍的研究。本研究的具体目标包括:1)研究反应参数对镍和铁羰基化的影响,包括反应温度(80-100°C),一氧化碳(表压)压力(0-56atm),气体流速(0.14-0.50 L / min),镍质量( 0.8-3.2g)和粒径(0.29 – 2.67 µm),以及含硫催化剂(硫,硫化铁和硫化氢)的影响; 2)研究红土矿石的非催化羰基化;减排条件的影响; 3)进一步了解羰基化过程的动力学和机理。通过在500°C下用氢气还原缔合的氧化物(气体流速为1.0 L / min)制备纯金属和镍铁混合物。 ;氧化物的还原度超过98%。考察了由CSIRO提供的两种类型的澳大利亚红土矿石(以CSIRO标记):含1.35 wt%镍,10.4 wt%铁和0.038 wt%Co的BCS矿石,粒度为53-200 µm;以及粒度为38-53 µm,75-90 µm,140-200 µm和355-495 µm的MIN矿石,其中含有1.68-2.37 wt%的Ni,8.90-11.8 wt%的Fe和0.135-0.144 wt%的Co)。红土矿石的选择性还原是在750°C的CO-CO2气体混合物(60%(体积)CO)下进行的。羰基化实验是在浸入油浴的柔性U型反应器(最大压力为68atm)中进行的。使用CO在不同压力下研究羰基化。羰基在两个Dreschel瓶中被王水吸收。在不同时间从王水溶液中取样并通过ICP-OES分析。使用ICP-OES分析的结果计算羰基化程度。在约5.5小时内,镍在100°C和CO压力27 atm下的非催化羰基化接近完成(反应程度为98%)。纯铁的羰基化反应缓慢。在100°C和高达55 atm(表压)的CO压力下铁羰基化程度小于5.0%。在这些条件下钴的羰基化程度小于0.5%。含硫的催化剂促进了羰基化反应。镍完全羰基化的时间从非催化反应中的5.5小时缩短为100°C和CO压力为14 atm时催化羰基化的2小时。选择性还原的BCS红土矿石在100°C和CO压力41 atm时镍的非催化羰基化程度低于50%。在选择性还原的矿石的羰基化中使用催化剂效率低下。影响矿石羰基化速率的主要参数是粒度。反应速度随着粒径的减小而显着增加。在反应4小时后,粒径为38-53和75-90 µm的MIN矿石中镍的羰基化接近完成。对镍羰基化和选择性还原的红土矿石进行系统研究的结果对于进一步了解羰基化反应。通过羰基化工艺从红土矿石中提取镍的技术的进一步发展取得了可喜的成果。

著录项

相似文献

  • 外文文献
  • 中文文献
  • 专利

客服邮箱:kefu@zhangqiaokeyan.com

京公网安备:11010802029741号 ICP备案号:京ICP备15016152号-6 六维联合信息科技 (北京) 有限公司©版权所有
  • 客服微信

  • 服务号