利用酸性矿山排水(AMD)处理污泥催化剂对废咖啡渣和高密度聚乙烯(HDPE)进行催化共热解的深入研究:动力学、机理和热力学特性分析

Deepak Bhushan , Sanjeevani Hooda , Susmit Chitransh , Prasenjit Mondal
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引用次数: 0

摘要

本研究旨在探讨酸性矿山排水(AMD)处理污泥催化剂对废咖啡渣和高密度聚乙烯共热解的催化作用。污泥是在使用蛋壳和过氧化氢处理 AMD 的过程中产生的。在 10 ℃/分钟、20 ℃/分钟、30 ℃/分钟和 40 ℃/分钟的不同加热速率下,分别对废咖啡渣(SC)、高密度聚乙烯(HDPE)、废咖啡渣与高密度聚乙烯混合物(SC+HDPE)(比例为 1:1)以及混合原料与污泥衍生催化剂(SC+HDPE_AMDC)(重量比为 1:1)进行了热解热重分析。利用等转换模型,如 Ozawa Flynn Wall (OFW)、Kissinger Akahira Sunose (KAS)、Friedman 和 Starink,确定了该过程的活化能 (Ea)。结果表明,在热解过程中使用经 AMD 处理的污泥催化剂可降低活化能 (Ea),从而提高其整体功效(OFW- Ea:209.11 至 177.14 KJ/mol;KAS-Ea:208.30 至 173.06 KJ/mol;Friedman-Ea:210.54 至 176.28 KJ/mol;Starink-Ea:208.60 至 173.44 KJ/mol)。利用 Criado's z-master plot (CZMP) 方法分析了反应机理。此外,还评估了前指数因子和热力学参数。结论是,加入污泥催化剂(AMDC)降低了系统的焓和随机性。催化共热解所需的能量较少,因此在生物质和塑料的可持续加工方面更环保。本研究将有助于设计、优化和扩展。
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Insights into catalytic co-pyrolysis of spent coffee grounds and high density polyethylene (HDPE) using acid mine drainage (AMD) treated sludge based catalyst: Analysis of kinetics, mechanism and thermodynamic properties

The present study aims to investigate the catalytic effect of acid mine drainage (AMD) treated sludge based catalyst on the co-pyrolysis of spent coffee grounds and HDPE. The sludge was generated during the treatment of AMD using eggshell and hydrogen peroxide. Theromogravimetric analysis of pyrolysis of spent coffee grounds (SC), HDPE (High density polyethylene), blend of spent coffee grounds and HDPE (SC+HDPE) in the ratio of 1:1, and blended feedstock with sludge derived catalyst (SC+HDPE_AMDC) (1:1 wt. ratio) was conducted at various heating rates of 10 °C/min, 20 °C/min, 30 °C/min and 40 °C/min respectively. Iso-conversional models such as Ozawa Flynn Wall (OFW), Kissinger Akahira Sunose (KAS), Friedman, and Starink were utilized for the determination of activation energy (Ea) of the process. The results showed that using AMD treated sludge based catalyst to the pyrolysis process, enhances its overall efficacy by lowering the activation energy (Ea) (OFW- Ea: 209.11 to 177.14 KJ/mol, KAS-Ea: 208.30 to 173.06 KJ/mol, Friedman- Ea:210.54 to 176.28 KJ/mol, and Starink- Ea:208.60 to 173.44 KJ/mol). Criado's z-master plot (CZMP) method was utilized to analyze the mechanism of the reaction. The pre-exponential factor and thermodynamic parameters were also evaluated. It is concluded that the incorporation of sludge based catalyst (AMDC) lowered enthalpy and randomness of system. Catalytic co-pyrolysis requires less energy, making it more environmental friendly choice for the sustainable processing of biomass and plastics. The present investigation will aid in the design, optimization and scalability.

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