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Catalytic co-pyrolysis of polycarbonate and polyethylene/polypropylene mixtures: Promotion of oil deoxygenation and aromatic hydrocarbon formation

机译:聚碳酸酯和聚乙烯/聚丙烯混合物的催化共热分解:促进油脱氧和芳烃形成

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The co-pyrolysis of polycarbonate (PC) and polyethylene (PE)/polypropylene (PP) in the presence of HZSM-5 catalyst was studied in a two-stage tube reactor with the objective of promoting simultaneous deoxygenation and aromatic hydrocarbon formation, at atmospheric pressure and without external hydrogen addition. As the blending ratio of PE/PP increased, the yield of oil phase product, coke, and solid decreased, and the yield of gas phase increased significantly. At the blending ratio of 75% PP, the concentration of oxygenates in the oil was reduced to 2.9% and that of aromatic hydrocarbons increased to 97.1%. Increasing the reaction temperature from 500 degrees C to 700 degrees C increased the yield of aromatic hydrocarbons further to 98.1%. Catalyst regeneration decreased the acidity of the HZSM-5 catalyst, resulting in a slight decrease in the deoxygenation and aromatization effects. The results showed that PP is an effective hydrogen donor in the catalytic deoxygenation and aromatization process; the hydrogen provided enhanced the adsorption of phenols produced by the pyrolysis of PC on HZSM-5 and their direct deoxygenation to form new aromatic hydrocarbons.
机译:在HzSM-5催化剂存在下,在两级管反应器中研究了聚碳酸酯(PC)和聚乙烯(PE)/聚丙烯(PP)的共热分解,其目的是在大气压下促进同时脱氧和芳烃形成的目的压力和没有外部氢添加。随着PE / PP的混合比增加,油相产物,焦炭和固体的产率下降,气相产量显着增加。以75%PP的混合比,油状物中的含氧浓度降低至2.9%,芳烃的浓度增加至97.1%。将反应温度从500℃升高至700摄氏度的增加提高至98.1%的芳烃的产率。催化剂再生降低了HZSM-5催化剂的酸度,导致脱氧和芳族化效应的略微降低。结果表明,PP是催化脱氧和芳族化工艺中有效的氢供体;氢提供通过在HZSM-5上的PC热解和它们的直接脱氧形成以形成新的芳烃,增强了苯酚的吸附。

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