Lorbach Sebastian-Mark, Lechleitner Andreas Erwin, Zapf Fabian, Lehner Markus
Chair of Process Technology and Industrial Environmental Protection, Montanuniversitaet Leoben, Franz-Josef-Straße 18, 8700 Leoben, Austria.
OMV Downstream GmbH, Mannswoerther Straße 28, 2320 Schwechat, Austria.
Chem Bio Eng. 2024 Apr 30;1(7):623-632. doi: 10.1021/cbe.4c00032. eCollection 2024 Aug 22.
Chemical recycling of plastic wastes through pyrolysis, gasification, or partial oxidation is a promising alternative to landfill disposal and incineration which must be applied in a future circular economy. These technologies enable the chemical industry, which currently heavily relies on crude oil, to obtain necessary chemical feedstock from postconsumer plastic waste. Kinetic models of pyrolysis and gasification reactions are required to dimension and design these processes on an industrial scale. The creation of detailed kinetic networks is often not feasible due to their complexity in this application, which is when the lumped kinetic modeling approach is used. This work develops and compares five lumped kinetic models for the co-pyrolysis of LDPE with a heavy petroleum fraction in a tubular reactor. A priori lumping is used for four models, and the fifth is created using a posteriori principle whereby in each model the product mixture is defined by eight lumps distinguished by their boiling point. The aim of this work is to compare different approaches for modeling reaction pathways in lumped kinetic models and to identify their impact on the predictive accuracy of the model. It was shown that all of the modeling approaches and the resulting models have similar prediction accuracies and deviations but with different kinetic parameters. Each model was used for a scale-up of an industrial-sized reactor to check whether the model had an influence on the design or predicted operation of the reactor.
通过热解、气化或部分氧化对塑料废物进行化学循环利用,是填埋处理和焚烧的一种有前景的替代方案,而填埋处理和焚烧在未来的循环经济中必须得到应用。这些技术使目前严重依赖原油的化学工业能够从消费后塑料废物中获取必要的化学原料。热解和气化反应的动力学模型对于在工业规模上确定这些工艺的尺寸和进行设计是必需的。由于在该应用中详细动力学网络的复杂性,创建详细的动力学网络通常不可行,此时需采用集总动力学建模方法。这项工作开发并比较了五种用于低密度聚乙烯(LDPE)与重质石油馏分在管式反应器中共热解的集总动力学模型。其中四个模型采用先验集总,第五个模型采用后验原理创建,即在每个模型中,产物混合物由八个按沸点区分的集总来定义。这项工作的目的是比较集总动力学模型中反应途径建模的不同方法,并确定它们对模型预测准确性的影响。结果表明,所有建模方法及由此产生的模型具有相似的预测准确性和偏差,但动力学参数不同。每个模型都用于工业规模反应器的放大,以检查该模型是否对反应器的设计或预测运行有影响。