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Sustainable treatment of bimetallic (Ag-Pd/α-Al_2O_3) catalyst waste from naptha cracking process: An innovative waste-to-value recycling of precious metals

机译:来自石脑油裂解工艺的双金属(Ag-Pd /α-Al_2O_3)催化剂废物的可持续处理:贵金属的创新浪费价值回收

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摘要

Bimetallic (Ag-Pd/αAl_2O_3) catalysts are essentially applied to naptha-cracking process with a controlled CO_2 emission. After losing the catalytic properties in long run, the landfilling disposal of spent catalysts poses severe stress to the environment and deprivation of precious metals. Therefore, an innovative solvo-chemical recycling approach that involving the solid-liquid and liquid-liquid mass transfer phenomena was studied. The parametric variations for dissolving precious metals yielded >98% efficiency at a lixiviant concentration, 2.0 mol L~(-1) HC1; pulp density, 20% (wt./vol.); agitation speed, 300 rpm, temperature, 90°C, and duration, 60 min. The activation energy of silver (6.9 kJ mol~(-1)) and palladium (11.9 kJ mol~(-1)) leaching indicated that the process was governed by a diffusion-controlled mechanism. Subsequently, silver and palladium were separated using 0.15 mol L~(-1) LIX 84-I at different acid concentration that yielding the maximum separation factor (/Vg/Pd) = 12,501) at 2.0 mol L~(-1) HC1. Stripping of separately (Ag/Pd)-loaded organic solutions with different solutions of HNO3, (NH_4)_2SO_4, and CH4N2S showed higher affinity for thiourea, yielding 56%, 38%, and 87% efficiency, respectively. Thus the counter-current extraction at an organic-to-aqueous (O:A) ratio of 1:2.5 and stripping with 0.5 mol L~(-1) CH_4N_2S at an O:A ratio of 2:1 yielded a five-fold enrich solutions of precious metals (75.2 mg L~(-1) Ag and 188.5 mg L~(-1) Pd) with a purity of >99.9%. The process essentially aims to Goal 12 under the United Nations' Sustainable Development Goals for sustainable recycling of industrial wastes consequently conserving the natural mineral reserves.
机译:双金属(Ag-Pd /αAl_2O_3)催化剂基本上应用于具有受控CO_2发射的Naptha开裂过程。在长期失去催化性质后,废催化剂的填埋场处理对环境和剥夺贵金属的严重应激。因此,研究了涉及固液和液体液体传递现象的创新溶剂化学回收方法。溶解贵金属的参数变化在唇炎浓度下产生> 98%的效率,2.0mol L〜(-1)HCl;纸浆密度,20%(wt./vol。);搅拌速度,300rpm,温度,90°C和持续时间,60分钟。银的活化能量(6.9 kJ mol〜(-1))和钯(11.9kJ mol〜(-1))浸出表明该过程由扩散控制机制控制。随后,在不同的酸浓度下使用0.15mol L〜(-1)LiX 84-1分离银和钯,其在2.0mol L〜(-1)HCl下产生最大分离因子(/mg / pd)= 12,501)。分别剥离(Ag / Pd) - 具有不同HNO3,(NH_4)_2SO_4和CH 4N 2的不同溶液的有机溶液对硫脲显示出较高的亲和力,分别产生56%,38%和87%的效率。因此,在有机 - 水 - 水溶液(O:A)的比例为1:2.5的逆流萃取,并在O的0.5mol L〜(-1)CH_4N_2S中剥离:比例为2:1,产生五倍丰富贵金属的溶液(75.2mg L〜(-1)Ag和188.5mg L〜(-1)Pd),纯度> 99.9%。这一过程基本上旨在根据“联合国”可持续发展目标,为可持续回收工业废物的可持续发展目标,因此保护天然矿产储备。

著录项

  • 来源
    《Journal of Environmental Management》 |2021年第1期|112748.1-112748.11|共11页
  • 作者单位

    Department of Environment and Energy Jeonbuk National University Jeonju Jeonbuk 54896 Republic of Korea;

    Department of Mineral Resources and Energy Engineering Jeonbuk National University Jeonju Jeonbuk 54896 Republic of Korea;

    Department of Mineral Resources and Energy Engineering Jeonbuk National University Jeonju Jeonbuk 54896 Republic of Korea;

    Department of Environment and Energy Jeonbuk National University Jeonju Jeonbuk 54896 Republic of Korea Department of Mineral Resources and Energy Engineering Jeonbuk National University Jeonju Jeonbuk 54896 Republic of Korea;

  • 收录信息 美国《科学引文索引》(SCI);美国《化学文摘》(CA);
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

    Industrial ecology; Amber-listed petro-refinery waste; Precious metals' recycling; Solvo-chemical mass transfer; Sustainable development goals;

    机译:工业生态;琥珀色的石油炼油厂垃圾;贵金属的回收;Solvo-化学传质;可持续发展目标;

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