Breyer Sacha, Mekhitarian Loucine, Rimez Bart, Haut B
Transfers, Interfaces and Processes (TIPs), Chemical Engineering Unit, Université libre de Bruxelles (ULB), Av. F.D. Roosevelt 50 CP 165/67, 1050 Brussels, Belgium.
Transfers, Interfaces and Processes (TIPs), Chemical Engineering Unit, Université libre de Bruxelles (ULB), Av. F.D. Roosevelt 50 CP 165/67, 1050 Brussels, Belgium.
Waste Manag. 2017 Feb;60:363-374. doi: 10.1016/j.wasman.2016.12.011. Epub 2017 Jan 4.
This work is a preliminary study for the development of a co-pyrolysis process of plastic wastes excavated from a landfill and used lubrication oils, with the aim to produce an alternative liquid fuel for industrial use. First, thermogravimetric experiments were carried out with pure plastics (HDPE, LDPE, PP and PS) and oils (a motor oil and a mixture of used lubrication oils) in order to highlight the interactions occurring between a plastic and an oil during their co-pyrolysis. It appears that the main decomposition event of each component takes place at higher temperatures when the components are mixed than when they are alone, possibly because the two components stabilize each other during their co-pyrolysis. These interactions depend on the nature of the plastic and the oil. In addition, co-pyrolysis experiments were led in a lab-scale reactor using a mixture of excavated plastic wastes and used lubrication oils. On the one hand, the influence of some key operating parameters on the outcome of the process was analyzed. It was possible to produce an alternative fuel for industrial use whose viscosity is lower than 1Pas at 90°C, from a plastic/oil mixture with an initial plastic mass fraction between 40% and 60%, by proceeding at a maximum temperature included in the range 350-400°C. On the other hand, the amount of energy required to successfully co-pyrolyze, in lab conditions, 1kg of plastic/oil mixture with an initial plastic mass fraction of 60% was estimated at about 8MJ. That amount of energy is largely used for the thermal cracking of the molecules. It is also shown that, per kg of mixture introduced in the lab reactor, 29MJ can be recovered from the combustion of the liquid resulting from the co-pyrolysis. Hence, this co-pyrolysis process could be economically viable, provided heat losses are addressed carefully when designing an industrial reactor.
这项工作是对从垃圾填埋场挖掘出的塑料废物与废润滑油进行共热解工艺开发的初步研究,目的是生产一种可供工业使用的替代液体燃料。首先,对纯塑料(高密度聚乙烯、低密度聚乙烯、聚丙烯和聚苯乙烯)和油(一种机油和废润滑油混合物)进行了热重实验,以突出塑料和油在共热解过程中发生的相互作用。结果表明,各组分混合时的主要分解事件发生温度高于单独存在时,这可能是因为两种组分在共热解过程中相互稳定。这些相互作用取决于塑料和油的性质。此外,在实验室规模的反应器中对挖掘出的塑料废物和废润滑油的混合物进行了共热解实验。一方面,分析了一些关键操作参数对该工艺结果的影响。通过在350 - 400°C的最高温度下进行反应,使用初始塑料质量分数在40%至60%之间的塑料/油混合物,可以生产出一种90°C时粘度低于1Pas的可供工业使用的替代燃料。另一方面,在实验室条件下,成功共热解1kg初始塑料质量分数为60%的塑料/油混合物所需的能量估计约为8MJ。该能量主要用于分子的热裂解。研究还表明,每向实验室反应器中引入1kg混合物,共热解产生的液体燃烧可回收29MJ的能量。因此,只要在设计工业反应器时仔细解决热损失问题,这种共热解工艺在经济上可能是可行的。