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Municipal solid waste processing and separation employing wet torrefaction for alternative fuel production and aluminum reclamation

机译:使用湿法焙烧的城市固体废物处理和分离,用于替代燃料生产和铝回收

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This study employs wet torrefaction process (also known as hydrothermal) at low temperature. This process simultaneously acts as waste processing and separation of mixed waste, for subsequent utilization as an alternative fuel. The process is also applied for the delamination and separation of non-recyclable laminated aluminum waste into separable aluminum and plastic. A 2.5-L reactor was used to examine the wet torrefaction process at temperatures below 200 °C. It was observed that the processed mixed waste was converted into two different products: a mushy organic part and a bulky plastic part. Using mechanical separation, the two products can be separated into a granular organic product and a plastic bulk for further treatment. TGA analysis showed that no changes in the plastic composition and no intrusion from plastic fraction to the organic fraction. It can be proclaimed that both fractions have been completely separated by wet torrefaction. The separated plastic fraction product obtained from the wet torrefaction treatment also contained relatively high calorific value (approximately 44 MJ/kg), therefore, justifying its use as an alternative fuel. The non-recyclable plastic fraction of laminated aluminum was observed to be delaminated and separated from its aluminum counterpart at a temperature of 170 °C using an additional acetic acid concentration of 3%, leaving less than 25% of the plastic content in the aluminum part. Plastic products from both samples had high calorific values of more than 30 MJ/kg, which is sufficient to be converted and used as a fuel.
机译:这项研究采用了低温湿法烘焙工艺(也称为水热法)。该过程同时用作废物处理和混合废物的分离,以随后用作替代燃料。该方法还适用于将不可回收的层压铝废料分层和分离为可分离的铝和塑料。使用2.5升反应器检查温度低于200°C的湿法烘焙过程。观察到,已处理的混合废料被转化为两种不同的产品:糊状的有机部分和笨重的塑料部分。使用机械分离,可以将两种产品分离为颗粒状有机产品和塑料块,以进行进一步处理。 TGA分析表明,塑料组成没有变化,也没有从塑料级分侵入有机级分。可以断言,两个部分均已通过湿法烘焙完全分离。通过湿法焙烧处理获得的分离的塑料馏分产品还包含相对较高的热值(约44 MJ / kg),因此有理由将其用作替代燃料。观察到层压铝的不可回收塑料级分在170°C的温度下使用3%的额外乙酸浓度分层并与铝对应部分分离,剩下的铝部分中塑料含量不到25% 。来自两个样品的塑料产品的热值均超过30 MJ / kg,足以转化为燃料。

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