Krell Katina, Keller Florian, Gräbner Martin
Institute of Energy Process Engineering and Chemical Engineering (IEC), TU Bergakademie Freiberg (TUBAF), Fuchsmuehlenweg 9D, 09599 Freiberg, Germany.
Institute of Energy Process Engineering and Chemical Engineering (IEC), TU Bergakademie Freiberg (TUBAF), Fuchsmuehlenweg 9D, 09599 Freiberg, Germany.
Waste Manag. 2025 Sep;206:115090. doi: 10.1016/j.wasman.2025.115090. Epub 2025 Aug 26.
Pyrolysis-based chemical recycling (P-CR) of non-recyclable plastic containing waste to generate chemical feedstock is a developing alternative to conventional treatment options. Currently, polyolefin-rich waste fractions (MPO) are primarily targeted, which represent only a fraction of plastics in post-consumer waste and possibly compete with direct mechanical recycling. In this investigation, treatment options of residual fractions from mechanical sorting of lightweight packaging waste (LWP) in mixed polyolefins, mixed plastics and sorting residues are assessed in terms of greenhouse gas (GHG) emissions. The focus is placed on the varying composition depending on sorting plant configuration and the subsequent impact on the pyrolysis and oil processing steps, while maintaining consistency in mass, element and enthalpy balances. Applied methods include the component-specific material flow balancing of the mechanical recycling process using EASETECH and thermodynamic modelling of pyrolysis oil treatment using Aspen Plus. Results show that the application of P-CR instead of incineration with energy recovery of sorting residual fractions can potentially enable GHG reductions up to 435 kg COeq ton LWP processed. The specific GHG reduction potential by CR application of different fractions varies between 0.74 and 1.33 kg COeq kg fraction, while the respective sorting yield determines the total reduction potential. Mechanical recycling is shown to be superior to chemical recycling under all circumstances if applicable, including for recovered MPO fractions. Sensitivity analysis reveals critical process balancing parameters, including the electricity mix, substitution factors for mechanical recycling, energy efficiency of waste incineration and oil treatment hydrogen demand.
基于热解的不可回收含塑料废物化学循环利用(P-CR)以生成化学原料,是一种有别于传统处理方式的新兴方法。目前,富含聚烯烃的废物流(MPO)是主要目标,而这仅占消费后废物中塑料的一部分,并且可能与直接机械回收存在竞争。在本研究中,针对混合聚烯烃、混合塑料和分拣残渣中轻质包装废物(LWP)机械分拣产生的残余馏分的处理方案,从温室气体(GHG)排放方面进行了评估。重点在于取决于分拣厂配置的不同组成,以及随后对热解和油品加工步骤的影响,同时保持质量、元素和焓平衡的一致性。应用的方法包括使用EASETECH对机械回收过程进行特定组分的物料流平衡分析,以及使用Aspen Plus对热解油处理进行热力学建模。结果表明,采用P-CR而非对分拣残余馏分进行能量回收的焚烧方式,有可能使处理每吨LWP的温室气体减排高达435千克二氧化碳当量。不同馏分采用化学循环利用的特定温室气体减排潜力在0.74至1.33千克二氧化碳当量/千克馏分之间,而各自的分拣产率决定了总减排潜力。结果表明,在所有适用情况下,包括对回收的MPO馏分,机械回收均优于化学回收。敏感性分析揭示了关键的过程平衡参数,包括电力结构、机械回收的替代因子、废物焚烧的能源效率以及油品处理的氢气需求。