Integrating microwave pyrolysis and hydrotreating for converting low-density polyethylene into jet fuel

被引:3
作者
Luo, Ting [1 ,2 ]
Zhou, Wenguang [1 ,2 ]
Wang, Yunpu [3 ]
Jiang, Haiwei [4 ]
Wu, Jiabo [1 ,2 ]
Hu, Jinye [1 ,2 ]
Wang, Mengjiao [1 ,2 ]
Wang, Weixin [1 ,2 ]
Wang, Qi [1 ,2 ]
Hu, Yuhang [1 ,2 ]
Fan, Liangliang [1 ,2 ]
机构
[1] Nanchang Univ, Sch Resources & Environm, Minist Educ, Nanchang 330031, Peoples R China
[2] Nanchang Univ, Key Lab Poyang Lake Environm & Resource Utilizat, Minist Educ, Nanchang 330031, Peoples R China
[3] Nanchang Univ, Engn Res Ctr Biomass Convers, Minist Educ, Nanchang 330047, Peoples R China
[4] Jiangxi Acad Sci, Inst Energy Res, Nanchang 330096, Peoples R China
基金
中国国家自然科学基金;
关键词
LDPE; Microwave pyrolysis; Hydroreforming; Ni/Biochar; Jet fuel; LDPE THERMAL-CRACKING; CATALYTIC PYROLYSIS; ASSISTED PYROLYSIS; ACTIVATED CARBON; PLASTIC WASTES; ZSM-5; ZEOLITE; CO-PYROLYSIS; IN-SITU; OIL; LIGNIN;
D O I
10.1016/j.renene.2024.121432
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
With the increasing plastic waste and its environmental impact, finding effective recycling solutions is essential. Cracking plastic waste followed by hydrogenation could be a promising method for producing jet fuels. In the present work, microwave-assisted pyrolysis (MAP) with MgO combined with hydrotreating with a Ni/Biochar catalyst was firstly proposed to convert low-density polyethylene (LDPE) into jet fuel. The pyrolysis process yielded 48.5 wt% of liquid product, with C-5-C-15 hydrocarbons and olefins accounting for 87.6% and 65.5%, respectively. During the hydrotreating process with 10% Ni/Biochar at 300 degrees C of temperature and 2 MPa of initial H-2 pressure, the pyrolysis oil was successfully hydrotreated, resulting in 98.4% paraffins and 1.6% aromatics with liquid yield of 80.6 wt%. Among them, C-5-C-15 hydrocarbons created 96.1%. The kinetic analysis indicated an activation energy of 89.9 kJ/mol for hydrogenated LDPE pyrolysis oil (HPPO). Characterization of the Ni/Biochar catalyst after reaction showed a BET surface area of 438 m(2)/g, similar to that of the fresh catalyst, with minimal coke formation noted via XRD, TEM, and TG analyses. XPS and FTIR indicated negligible oxidation of Ni-0 during hydroprocessing. After 6 cycles, the catalyst remained high abundance for paraffins and C-5-C-15 hydrocarbons, namely, 98.4% and 94.0%, respectively, demonstrating its stability.
引用
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页数:12
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