A porous media catalyst for waste polyethylene pyrolysis in a continuous feeding reactor

被引:3
|
作者
Yang, Youwei [1 ]
Pan, Ruming [1 ]
Wu, Yibo [1 ]
Pan, Qinghui [1 ]
Shuai, Yong [1 ]
机构
[1] Harbin Inst Technol, Sch Energy Sci & Engn, Harbin 150001, Peoples R China
基金
中国博士后科学基金; 中国国家自然科学基金;
关键词
Catalytic pyrolysis; Waste polyethylene; Porous media catalyst; ZSM-5/Al2O3; Continuous feeding; PLASTIC WASTE; PRODUCT YIELD; BIO-OIL; PERFORMANCE; DEGRADATION; ZEOLITE; BIOMASS;
D O I
10.1016/j.energy.2024.131855
中图分类号
O414.1 [热力学];
学科分类号
摘要
This study investigated the catalytic pyrolysis of waste polyethylene (PE) using a ZSM-5/Al2O3 porous media catalyst in a continuous feeding mode. The findings revealed that the porous media catalyst with 100 mm height and 40 PPI (pore per inch) pore size had the supreme catalytic performance, which could obtain the highest pyrolysis oil yield and the light fraction (<C12) and aromatics in the oil, and improve the catalytic stability of the porous media catalyst. The optimal operating conditions were the pyrolysis temperature of 460 degrees C, the carrier gas velocity of 65 mL/min, and the plastic feeding rate of 25 g/h, of which the light fraction and aromatics in the oil were up to 95.25 % and 97.33 %. Moreover, the catalytic cycling performance of the porous media catalyst was thoroughly investigated. The catalytic activity declined and the catalyst deactivation rate decreased after multiple regeneration cycles. This study presents a comprehensive investigation of waste PE catalytic cracking using the porous media catalyst in continuous feeding mode, which can provide insightful guidance on the industrialization of plastic waste valorization.
引用
收藏
页数:13
相关论文
共 50 条
  • [21] Influence of temperature and residence time in the pyrolysis of woody biomass waste in a continuous screw reactor
    Solar, J.
    de Marco, I.
    Caballero, B. M.
    Lopez-Urionabarrenechea, A.
    Rodriguez, N.
    Agirre, I.
    Adrados, A.
    BIOMASS & BIOENERGY, 2016, 95 : 416 - 423
  • [22] Pyrolysis of waste tires in CFB reactor
    Dai, Xianwen
    Zhao, Zengli
    Wu, Chuangzhi
    Chen, Yong
    Ranliao Huaxue Xuebao/Journal of Fuel Chemistry and Technology, 2000, 28 (01): : 71 - 75
  • [23] PYROLYSIS OF POLYETHYLENE IN A FLUIDIZED-BED REACTOR
    CONESA, JA
    FONT, R
    MARCILLA, A
    GARCIA, AN
    ENERGY & FUELS, 1994, 8 (06) : 1238 - 1246
  • [24] Kinetic study on the pyrolysis of low-density polyethylene (LDPE) waste using kaolin as catalyst
    Erawati, Emi
    Hamid
    Martenda, Danik
    26TH REGIONAL SYMPOSIUM ON CHEMICAL ENGINEERING (RSCE 2019), 2020, 778
  • [25] Catalytic upgrading of polyethylene plastic waste using GMOF catalyst: Morphology, pyrolysis, and product analysis
    Norouzi, Omid
    Haddadi, Seyyed Arash
    Salaudeen, Shakirudeen
    Soltanian, Salman
    Bartocci, Pietro
    Arjmand, Mohammad
    Dutta, Animesh
    FUEL, 2024, 369
  • [26] Tire Pyrolysis in a continuous screw Reactor
    Susa, D.
    Haydary, J.
    KGK-KAUTSCHUK GUMMI KUNSTSTOFFE, 2014, 67 (1-2): : 53 - 56
  • [27] Tire pyrolysis in a continuous screw reactor
    Slovak University of Technology, Institute of Chemical and Environmental Engineering, Faculty of Chemical and Food Technology, Radlinského 9, 812 37 Bratislava, Slovakia
    KGK Kautsch. Gummi Kunstst., 1-2 (53-56):
  • [28] Catalyst addition in polyethylene pyrolysis - Thermogravimetric study
    Marcilla, A
    Beltran, M
    Conesa, JA
    JOURNAL OF ANALYTICAL AND APPLIED PYROLYSIS, 2001, 58 : 117 - 126
  • [29] Catalyst addition in polyethylene pyrolysis: Thermogravimetric study
    Marcilla, A. (antonio.marcilla@ua.es), 1600, Elsevier (58-59):
  • [30] Catalytic Pyrolysis of Waste Polyethylene Terephthalate over Waste Concrete
    Lim, Sejeong
    Kim, Young-Min
    APPLIED CHEMISTRY FOR ENGINEERING, 2019, 30 (06): : 707 - 711