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Thermo-chemical extraction of fuel oil from waste lubricating grease

机译:从废润滑油中热化学提取燃油

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摘要

This study investigated the recovery of oil from waste grease through the process of thermal degradation in an aqueous solution of potassium hydroxide (KOH) followed by solvent extraction. Waste high temperature metal bearing grease was dissolved in a 15 w/w% KOH solution at 80 ℃ while being agitated at 2000 rpm using a shear action agitator for a period of 15 min. Two distinct layers were observed after 8 min of settling time. The top layer being of dark brown oil and the bottom layer was a heterogeneous mixture. The two layers were separated by decantation. The bottom layer was cooled down to 45 ℃ followed by slow addition of toluene (C_7H_8) while agitating at 1200 rpm for 15 min to prevent solids settling and minimise rapid volatilisation of the organic compounds in the mixture. Two distinct layers were also formed, the top homogeneous mixture of light brown oil-toluene mixture and the bottom sludge layer. The solvent was recovered from the oil for re-use by fractional distillation of the homogenous mixture. It was observed that 15 w/w% potassium hydroxide solution can chemically degrade the soap matrix in the grease and extract up to 49 w/w% of the fuel oil when subjected to high shear stress at a temperature of 80 ℃. The 26 w/w% extraction of oil in the remaining sludge was obtained by solvent extraction process with mass ratios of sludge to solvent of 2:1. Solvent recovery of 88% by mass was obtained via fractional distillation method. The combined extraction processes brought an overall oil yield of 75 w/w% from the waste grease. The fuel oil obtained from this process has similar properties to paraffin oil and can be blended with other oils as an alternative energy source.
机译:这项研究研究了通过在氢氧化钾(KOH)水溶液中进行热降解,然后进行溶剂萃取的过程,从废油脂中回收油。将废的高温金属轴承润滑脂在80℃下溶解于15 w / w%的KOH溶液中,同时使用剪​​切搅拌器以2000 rpm的速度搅拌15分钟。沉降时间8分钟后观察到两个不同的层。顶层是深棕色油,底层是非均质混合物。通过倾析将两层分开。将底层冷却至45℃,然后缓慢加入甲苯(C_7H_8),同时以1200 rpm的转速搅拌15分钟,以防止固体沉降并最大程度地减少混合物中有机化合物的快速挥发。还形成了两个不同的层,浅棕色油-甲苯混合物的顶部均匀混合物和底部污泥层。从油中回收溶剂,通过均质混合物的分馏进行再利用。观察到,当在80℃的温度下承受高剪切应力时,15 w / w%的氢氧化钾溶液可以化学降解油脂中的皂基并提取高达49 w / w%的燃油。剩余污泥中油的26 w / w%萃取是通过溶剂萃取工艺获得的,污泥与溶剂的质量比为2:1。通过分馏法得到88质量%的溶剂回收率。联合提取工艺从废油脂中获得的总油产量为75 w / w%。从该方法获得的燃料油具有与石蜡油相似的性质,并且可以与其他油混合作为替代能源。

著录项

  • 来源
    《Waste Management》 |2013年第6期|1509-1515|共7页
  • 作者单位

    University of Johannesburg, Department of Mechanical Engineering Science, PO Box 17011, Doornfontein 2028, Johannesburg, South Africa;

    University of Johannesburg, Department of Chemical Engineering Technology, PO Box 17011, Doornfontein 2028, Johannesburg, South Africa;

    University of Johannesburg, Department of Mechanical Engineering Technology, PO Box 17011, Doornfontein 2028, Johannesburg, South Africa,Mechanical Engineering Department, MNNIT, Allahabad 211 004, UP, India;

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  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

    Fuel; Flocculation extraction; Solvent extraction; Waste grease;

    机译:汽油;絮凝萃取;溶剂萃取;废油脂;

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