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Hydrotreatment of pyrolysis oil from waste tire in tetralin for production of high-quality hydrocarbon rich fuel

机译:三特兰林废轮胎的热解油的加氢分解生产优质烃富含燃料

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摘要

Pyrolysis is a green method for waste tires processing with aim to produce oil. However, the resulting oil contains a relatively large amount of sulfur and nitrogen compounds, limiting its direct use. Therefore, this study aimed to improve properties of the waste tire pyrolysis oil (TPO) particular to reduce the N and S contents. The combination of tetralin and H-2 was employed to provide hydrogen source to enhance the hydrotreatment of the TPO. Effects of catalyst type (AC, Ir/C, Pt/C, Ru/C, and Pd/C), temperature (350-450 degrees C), catalyst loading (1-20 wt %), time (0.5-4 h), and hydrogen pressure (1 atm-9 MPa) on the upgraded products distribution and properties of the upgraded oil (UO) were examined. Positive synergetic effect between tetralin and H-2 existed in favoring the reduction of gas and solid products and improving the quality of the UO. Tetralin played a very important role in transferring molecular hydrogen to activated hydrogen and favored the hydrogenation reactions. Among the noble metals examined, Pt/C presented the highest performance toward the N, O, and S removal. The lowest N (0.09 wt%) and S (15 ppm) contents of UO were obtained at 430 degrees C, 2 h, 3gTPO + 3gTHN, 15 wt% Pt/C, and 6 MPa H-2. The UO had higher-heating values ranging from 42.42 to 44.63 MJ/kg depending on the reaction conditions. The chemical components of the UO are mainly aromatic compounds. Especially, monocyclic aromatic hydrocarbons account for about 40% of the total content.
机译:热解是一种用于废气处理的绿色方法,其目的是生产油。然而,所得油含有相对大量的硫和氮化合物,限制其直接使用。因此,本研究旨在改善废弃轮胎热解油(TPO)的性质,特别是降低N和S含量。采用四rralin和H-2的组合来提供氢气源以增强TPO的水溶性。催化剂型(AC,IR / C,Pt / C,Ru / C和PD / C),温度(350-450℃),催化剂负载(1-20重量%),时间(0.5-4小时) )和氢气压力(1atm-9MPa)对升级的产物分布和升级的油(UO)的性质进行检查。四特兰林和H-2之间的阳性协同作用,涉及降低气体和固体产品,提高UO的质量。转罗拉伦在将分子氢转移到活性氢气中并赞成氢化反应的作用非常重要。在检查的贵金属中,PT / C向N,O和S脱离呈现最高性能。在430℃,2小时,3GTPO + 3gTH,15wt%Pt / C和6MPa H-2中获得UO的最低N(0.09wt%)和S(15ppm)含量。根据反应条件,UO的较高加热值范围为42.42至44.63mJ / kg。 UO的化学成分主要是芳族化合物。特别是,单环芳烃占总含量的约40%。

著录项

  • 来源
    《Fuel》 |2021年第2期|119185.1-119185.10|共10页
  • 作者单位

    Xi An Jiao Tong Univ Sch Chem Engn & Technol Shaanxi Key Lab Energy Chem Proc Intensificat Xian 710049 Shaanxi Peoples R China;

    Xi An Jiao Tong Univ Sch Chem Engn & Technol Shaanxi Key Lab Energy Chem Proc Intensificat Xian 710049 Shaanxi Peoples R China;

    Xi An Jiao Tong Univ Sch Chem Engn & Technol Shaanxi Key Lab Energy Chem Proc Intensificat Xian 710049 Shaanxi Peoples R China;

    Henan Polytech Univ Coll Chem & Chem Engn Dept Energy & Chem Engn 2001 Century Ave Jiaozuo 454003 Henan Peoples R China;

    Henan Polytech Univ Coll Chem & Chem Engn Dept Energy & Chem Engn 2001 Century Ave Jiaozuo 454003 Henan Peoples R China;

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

    Waste tire; Pyrolysis; Pyrolysis oil; Hydrotreatment; Hydrogen donor; Fuel;

    机译:废弃轮胎;热解;热解油;加氢处理;氢气供体;燃料;

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