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通过中心复合设计和响应面法对包装塑料废弃物催化热解制备类煤油燃料的优化:铁掺杂白云石和活性炭的性能

Optimization of Kerosene-like Fuels Produced via Catalytic Pyrolysis of Packaging Plastic Waste via Central Composite Design and Response Surface Methodology: Performance of Iron-Doped Dolomite and Activated Carbon.

作者信息

Arjharnwong Oratepin, Vitidsant Tharapong, Permpoonwiwat Aminta, Phowan Naphat, Charusiri Witchakorn

机构信息

Master of Programme in Environmental Technology and Resources Management, Faculty of Environmental Culture and Ecotourism, Srinakharinwirot University, Bangkok 10110, Thailand.

Department of Chemical Technology, Faculty of Science, Chulalongkorn University, Bangkok 10110, Thailand.

出版信息

Molecules. 2025 Jul 7;30(13):2884. doi: 10.3390/molecules30132884.

Abstract

Rapid economic growth has led to an increase in the use of multilayer plastic packaging, which involves complex polymer compositions and hinders recycling. This study investigated the catalytic pyrolysis of plastic packaging waste in a 3000 cm semibatch reactor, aiming to optimize kerosene-like hydrocarbon production. The temperature (420-500 °C), N flow rate (25-125 mL/min), and catalyst loading (5-20 wt.%) were examined individually and in combination with activated carbon and an Fe-doped dolomite (Fe/DM) catalyst. Central composite design (CCD) and response surface methodology (RSM) were used to identify the optimal conditions and synergistic effects. Pyrolysis product analysis involved simulation distillation gas chromatography (Sim-DGC), gas chromatography/mass spectrometry (GC/MS), and Fourier transform infrared (FT-IR) spectroscopy. The optimal conditions (440 °C, 50 mL/min N flow, catalyst loading of 10 wt.% using a 5 wt.% Fe-doped dolomite-activated carbon 0.6:0.4 mass/molar ratio) yielded the highest pyrolysis oil (79.6 ± 0.35 wt.%) and kerosene-like fraction (22.3 ± 0.22 wt.%). The positive synergistic effect of Fe/DM and activated carbon (0.6:0.4) enhanced the catalytic activity, promoting long-chain polymer degradation into mid-range hydrocarbons, with secondary cracking yielding smaller hydrocarbons. The pore structure and acid sites of the catalyst improved the conversion of intermediate hydrocarbons into aliphatic compounds (C-C), increasing kerosene-like hydrocarbon production.

摘要

经济的快速增长导致多层塑料包装的使用增加,这种包装涉及复杂的聚合物成分,不利于回收利用。本研究在一个3000立方厘米的半间歇式反应器中对塑料包装废弃物的催化热解进行了研究,旨在优化类煤油烃的产量。分别考察了温度(420 - 500℃)、氮气流量(25 - 125毫升/分钟)和催化剂负载量(5 - 20重量%),并将其与活性炭和铁掺杂白云石(Fe/DM)催化剂结合使用。采用中心复合设计(CCD)和响应面方法(RSM)来确定最佳条件和协同效应。热解产物分析包括模拟蒸馏气相色谱法(Sim-DGC)、气相色谱/质谱联用仪(GC/MS)和傅里叶变换红外光谱仪(FT-IR)。最佳条件(440℃、50毫升/分钟氮气流量、使用质量/摩尔比为0.6:0.4的5重量%铁掺杂白云石 - 活性炭时催化剂负载量为10重量%)产生了最高的热解油产量(79.6 ± 0.35重量%)和类煤油馏分(22.3 ± 0.22重量%)。Fe/DM和活性炭(0.6:0.4)的正协同效应增强了催化活性,促进长链聚合物降解为中等链长的烃类,二次裂解生成较小的烃类。催化剂的孔结构和酸性位点提高了中间烃类向脂肪族化合物(C-C)的转化,增加了类煤油烃的产量。

https://cdn.ncbi.nlm.nih.gov/pmc/blobs/1e8c/12250723/16f75b28782f/molecules-30-02884-g001.jpg

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