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不同浓度ZSM-5沸石催化剂作用下金属化食品包装塑料的催化热解动力学行为及TG-FTIR-GC-MS分析

Catalytic Pyrolysis Kinetic Behavior and TG-FTIR-GC-MS Analysis of Metallized Food Packaging Plastics with Different Concentrations of ZSM-5 Zeolite Catalyst.

作者信息

Eimontas Justas, Striūgas Nerijus, Abdelnaby Mohammed Ali, Yousef Samy

机构信息

Laboratory of Combustion Processes, Lithuanian Energy Institute, Breslaujos 3, LT-44403 Kaunas, Lithuania.

Department of Production Engineering and Printing Technology, Akhbar Elyom Academy, Cairo 12566, Egypt.

出版信息

Polymers (Basel). 2021 Feb 26;13(5):702. doi: 10.3390/polym13050702.

Abstract

Recently, the pyrolysis process has been adapted as a sustainable strategy to convert metallized food packaging plastics waste (MFPW) into energy products (paraffin wax, biogas, and carbon black particles) and to recover aluminum. Usually, catalysts are used in pyrolysis treatment to refine pyrolysis products and to increase their yield. In order to study the effect of a catalyst on the formulated volatile products, this work aims to study the pyrolysis behavior of MFPW in presence of catalyst, using TG-FTIR-GC-MS system. The pyrolysis experiments were conducted with ZSM-5 Zeolite catalyst with different concentrations (10, 30, and 50 wt.%) at different heating rates (5, 10, 15, 20, 25, and 30 °C/min). In addition, TG-FTIR system and GC-MS unit were used to observe and analyze the thermal and chemical degradation of the obtained volatile compounds at maximum decomposition peaks. In addition, the kinetic results of catalytic pyrolysis of ZSM-5/MFPW samples matched when model-free methods, a distributed activation energy model (DAEM), and an independent parallel reaction kinetic model (IPR) were used. The TGA-DTG results showed that addition of a catalyst did not have a significant effect on the features of the TGA-DTG curves with similar weight loss of 87-90 wt.% (without taking the weight of the catalyst into account). Meanwhile, FTIR results manifested strong presence of methane and high-intensity functional group of carboxylic acid residues, especially at high concentration of ZSM-5 and high heating rates. Likewise, GC-MS measurements showed that Benzene, Toluene, Hexane, p-Xylene, etc. compounds (main flammable liquid compounds in petroleum oil) generated catalysts exceeding 50%. Finally, pyrolysis kinetics showed that the whole activation energies of catalytic pyrolysis process of MFPW were estimated at 289 kJ/mol and 110, 350, and 174 kJ/mol for ZSM-5/MFPW samples (10, 30, and 50 wt.%, respectively), whereas DAEM and IPR approaches succeeded to simulate TGA and DTG profiles with deviations below <1.

摘要

最近,热解工艺已被用作一种可持续战略,将金属化食品包装塑料废物(MFPW)转化为能源产品(石蜡、沼气和炭黑颗粒)并回收铝。通常,在热解处理中使用催化剂来精制热解产物并提高其产率。为了研究催化剂对配制的挥发性产物的影响,本工作旨在使用TG-FTIR-GC-MS系统研究在催化剂存在下MFPW的热解行为。热解实验是在不同加热速率(5、10、15、20、25和30℃/分钟)下使用不同浓度(10、30和50重量%)的ZSM-5沸石催化剂进行的。此外,TG-FTIR系统和GC-MS装置用于在最大分解峰处观察和分析所得挥发性化合物的热降解和化学降解。此外,当使用无模型方法、分布式活化能模型(DAEM)和独立平行反应动力学模型(IPR)时,ZSM-5/MFPW样品的催化热解动力学结果相匹配。TGA-DTG结果表明,添加催化剂对TGA-DTG曲线的特征没有显著影响,失重相似,为87-90重量%(不考虑催化剂的重量)。同时,FTIR结果表明甲烷大量存在以及羧酸残基的高强度官能团,特别是在高浓度ZSM-5和高加热速率下。同样,GC-MS测量表明,苯、甲苯、己烷、对二甲苯等化合物(石油中主要的易燃液体化合物)在催化剂超过50%时产生。最后,热解动力学表明,MFPW催化热解过程的整体活化能估计为289 kJ/mol,ZSM-5/MFPW样品(分别为10、30和50重量%)的活化能为110、350和174 kJ/mol,而DAEM和IPR方法成功模拟了TGA和DTG曲线,偏差低于<1。

https://cdn.ncbi.nlm.nih.gov/pmc/blobs/4cb0/7956265/b3639b1cd784/polymers-13-00702-g001.jpg

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