Co-pyrolysis of sugarcane bagasse and polystyrene with ex-situ catalytic bed of metal oxides/HZSM-5 with focus on liquid yield

被引:63
作者
Iftikhar, Hera [1 ]
Zeeshan, Muhammad [1 ]
Iqbal, Saeed [2 ]
Muneer, Bushra [1 ]
Razzaq, Madiha [1 ]
机构
[1] Natl Univ Sci & Technol, IESE, Sch Civil & Environm Engn, H-12 Campus, Islamabad 44000, Pakistan
[2] Natl Univ Sci & Technol, Us Pakistan Ctr Adv Studies Energy, H-12 Campus, Islamabad 44000, Pakistan
关键词
Catalytic co-pyrolysis; HZSM-5; Pyrolysis oil; Bi-functional catalyst; Dual-catalyst bed; LOW-DENSITY POLYETHYLENE; BIO-OIL YIELD; PINE SAWDUST; BIOMASS; WASTE; HZSM-5; CAO; KINETICS; VAPORS; WOOD;
D O I
10.1016/j.biortech.2019.121647
中图分类号
S2 [农业工程];
学科分类号
0828 ;
摘要
Catalytic co-pyrolysis of sugarcane bagasse (SCB) and polystyrene (PS) was conducted in a fixed bed reactor over microporous HZSM-5, mesoporous metal oxides (MgO, CaO) and their blends to examine the effect on pyrolytic liquid yields and quality. Though the catalyst addition decreased the liquid yield, improvement in mono-aromatic hydrocarbon yield with the least content of oxygenates was achieved in the catalytic trials. Results revealed that HZSM-5 showed maximum conversion efficiency of acids, furans and phenols acting as hydrocarbon source for aromatic production. Basic MgO, with acidic HZSM-5, was found to conduce better catalytic performance yielding improved oil quality compared to HZSM-5:CaO catalyst. Mass ratio of 1:3 HZSM-5:MgO exhibited most eminent synergistic effect with maximum (56.8 wt%) mono-aromatic hydrocarbon (MAH) yield and lowest (20.8 wt%) poly-aromatic hydrocarbon (PAH) content. Additionally, increased calorific value and density upgradation comparable to standard diesel fuel quality were observed in the presence of dual catalyst layout.
引用
收藏
页数:9
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