Pilot-scale flue gas pyrolysis system for organic and plastic wastes with improved liquid properties in a non-thermal plasma reactor

被引:4
|
作者
Lim, Mook Tzeng [1 ]
Tan, Ee Sann [2 ]
Chai, Yee Ho [3 ]
Chin, Bridgid Lai Fui [4 ,5 ]
Juwono, Filbert H. [6 ]
Hisham, Danial Hakim Badrul [7 ]
Anuar, Muhammad Athir Mohamed [7 ]
机构
[1] Mid Valley City, NexantECA, Kuala Lumpur 59200, Malaysia
[2] Univ Tenaga Nas, Dept Mech Engn, Kajang 43000, Selangor, Malaysia
[3] Univ Teknol PETRONAS, Inst Selfsustainable Bldg, HICoE Ctr Biofuel & Biochem Res, Dept Chem Engn, Seri Iskandar 32610, Perak, Malaysia
[4] Curtin Univ Malaysia, Fac Engn & Sci, Chem & Energy Engn Dept, Energy & Environm Res Cluster, CDT 250, Miri 98009, Sarawak, Malaysia
[5] Curtin Univ Malaysia, Fac Engn & Sci, Energy & Envionrment Res Cluster, CDT 250, Miri 98009, Sarawak, Malaysia
[6] Univ Southampton Malaysia, Connected Intelligence Res Grp, Iskandar Puteri 79100, Johor, Malaysia
[7] TNB Res Sdn Bha, Biomass Plasma Perovskite Technol, Renewable Energy & Green Technol, Kajang 43000, Selangor, Malaysia
关键词
Co-pyrolysis; Organic waste; Plasma reactor; Plastic waste; Fast pyrolysis; CATALYTIC CO-PYROLYSIS; BIO-OIL; LIGNOCELLULOSIC BIOMASS; PARAMETERS;
D O I
10.1016/j.jaap.2023.106062
中图分类号
O65 [分析化学];
学科分类号
070302 ; 081704 ;
摘要
A fast, oxidative pyrolysis system was developed to produce a pyrolysis liquid (PyOL) upgraded with a nonthermal plasma (NTP) reactor. In addition to the 1.8 million tonnes per annum of plastic wastes, large amounts of municipal solid waste in Malaysia end up in landfills, of which 40-60 % is organic or food waste. Organic and plastic wastes (OPW) can be used as carbon feedstocks for the pyrolysis process to produce PyOL, reducing the OPW disposal in landfills, and carbon emissions. However, the current pyrolysis methods use pure nitrogen, implying increased operational cost, and are commonly performed at the lab scale. In this study, flue gas was used for the pyrolysis of OPW at a pilot scale. The use of flue gas for PyOL production reduces the operational costs and lifecycle carbon emissions. Results show that the addition of a small percentage of plastics at the pyrolysis temperature of 350 degrees C increased the yield of liquid. However, large amounts of plastics resulted in significant material agglomeration. A disadvantage of PyOL is the degradation of properties with respect to storage time. Therefore, a NTP reactor was developed to improve the PyOL properties. After NTP treatment, the aromatic and carbonyl ester groups decrease, the calorific value increased, and certain chemical compounds increased in concentration. This study provides operational parameters for the pilot scale pyrolysis (and wasteto-energy) process, improving the technical viability of scaling-up such systems.
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页数:10
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