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Pyrolysis-Catalytic-Dry Reforming of Waste Plastics and Mixed Waste Plastics for Syngas Production

机译:用于合成气生产的废塑料和混合废塑料的热解-催化-干燥重整

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摘要

The CO2 dry reforming of various types of waste plastics (LDPE, HDPE, PS, PET, and PP) and a simulated mixture of the different waste plastics was investigated over a Ni-Co-Al catalyst using a two-stage reactor. The first stage pyrolyzed the plastics, and the second stage involved catalytic-dry reforming of the product pyrolysis gases with CO2. The introduction of CO2 without a catalyst markedly increased the dry reforming reaction and significantly improved the production of H-2/CO synthesis gas (syngas). The introduction of the Ni-Co-Al catalyst further significantly improved the production of syngas. LDPE produced the highest yield of syngas at 154.7 mmol(syngas) g(plastic)(-1) from the pyrolysis-catalytic-dry reforming process. The order of syngas production for the different plastics was LDPE < HDPE < PP < PS < PET. The syngas yield from the processing of the simulated waste plastic mixture was 148.6 7 mmol(syngas) g(plastic)(-1) which reflected the high content of the linear polyalkene plastics (LDPE, HDPE, PP) in the simulated waste plastic mixture.
机译:在Ni-Co-Al催化剂上使用两级反应器研究了各种废塑料(LDPE,HDPE,PS,PET和PP)的二氧化碳干重整以及不同废塑料的模拟混合物。第一阶段将塑料热解,第二阶段涉及将产物热解气体与CO2进行催化干重整。在没有催化剂的情况下引入CO2显着提高了干重整反应,并显着提高了H-2 / CO合成气(合成气)的生产。 Ni-Co-Al催化剂的引入进一步显着改善了合成气的生产。 LDPE通过热解-催化-干重整过程产生的合成气产率最高,为154.7 mmol(合成气)g(塑料)(-1)。不同塑料的合成气生产顺序为LDPE

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  • 来源
    《Energy & fuels》 |2016年第4期|3198-3204|共7页
  • 作者单位

    Univ Leeds, Sch Chem & Proc Engn, Leeds LS2 9JT, W Yorkshire, England;

    Univ Leeds, Sch Chem & Proc Engn, Leeds LS2 9JT, W Yorkshire, England;

  • 收录信息 美国《科学引文索引》(SCI);美国《工程索引》(EI);美国《生物学医学文摘》(MEDLINE);
  • 原文格式 PDF
  • 正文语种 eng
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