Three-stage pyrolysis–steam reforming–water gas shift processing of household, commercial and industrial waste plastics for hydrogen production

Rayed Alshareef, Robert Sait-Stewart, Mohamad A. Nahil, Paul T. Williams
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Abstract

Five common single plastics and nine different household, commercial and industrial waste plastics were processed using a three-stage (i) pyrolysis, (ii) catalytic steam reforming and (iii) water gas shift reaction system to produce hydrogen. Pyrolysis of plastics produces a range of different hydrocarbon species which are subsequently catalytically steam reformed to produce H2 and CO and then undergo water gas shift reaction to produce further H2. The process mimics the commercial process for hydrogen production from natural gas. Processing of the single polyalkene plastics (high-density polyethylene (HDPE), low-density polyethylene (LDPE), and polypropylene (PP)) produced similar H2 yields between 115 mmol and 120 mmol per gram plastic. Even though PS produced an aromatic product slate from the pyrolysis stage, further stages of reforming and water gas shift reaction produced a gas yield and composition similar to that of the polyalkene plastics (115 mmol H2 per gram plastic). PET gave significantly lower H2 yield (41 mmol per gram plastic) due to the formation of mainly CO, CO2 and organic acids from the pyrolysis stage which were not conducive to further reforming and water gas shift reaction. A mixture of the single plastics typical of that found in municipal solid waste produced a H2 yield of 102 mmol per gram plastic. Knowing the gas yields and composition from the single plastics enabled an estimation of the yields from a simulated waste plastic mixture and a ‘real-world’ waste plastic mixture to be determined. The different household, commercial and industrial waste plastic mixtures produced H2 yields between 70 mmol and 107 mmol per gram plastic. The H2 yield and gas composition from the single waste plastics gave an indication of the type of plastics in the mixed waste plastic samples.

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家用、商用和工业废塑料三段式热解-蒸汽重整-水煤气变换处理制氢
五种常见的单一塑料和九种不同的家用,商业和工业废塑料采用三段式(i)热解,(ii)催化蒸汽重整和(iii)水煤气变换反应系统进行处理,以产生氢气。塑料的热解产生一系列不同的碳氢化合物,这些碳氢化合物随后被催化蒸汽重整生成H2和CO,然后进行水气转换反应进一步生成H2。这个过程模仿了从天然气中生产氢气的商业过程。单聚烯烃塑料(高密度聚乙烯(HDPE),低密度聚乙烯(LDPE)和聚丙烯(PP))的加工产生的氢气产量相似,在每克塑料115至120毫摩尔之间。尽管PS在热解阶段产生芳香产物板岩,但在重整和水气转换反应的后续阶段,其产气率和组成与聚烯烃塑料相似(每克塑料115 mmol H2)。PET的H2产率较低(41 mmol / g塑料),这主要是由于热解阶段主要生成CO、CO2和有机酸,不利于进一步重整和水煤气转移反应。在城市固体废物中发现的典型的单一塑料混合物产生的H2产率为每克塑料102毫摩尔。了解了单一塑料的气体产量和成分,就可以估计模拟废塑料混合物和“现实世界”废塑料混合物的产量。不同的家用、商业和工业废塑料混合物产生的H2产率在每克塑料70至107 mmol之间。单个废塑料的H2产率和气体组成表明了混合废塑料样品中塑料的类型。图形抽象
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