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Microwave-assisted in-situ catalytic pyrolysis of polystyrene: Analysis of product formation and energy consumption using machine learning approach
被引:17
|作者:
Terapalli, Avinash
[1
]
Kamireddi, Dinesh
[1
]
Sridevi, Veluru
[1
]
Tukarambai, M.
[1
]
Suriapparao, Dadi, V
[2
]
Rao, Chinta Sankar
[3
]
Gautam, Ribhu
[4
]
Modi, Prerak R.
[5
]
机构:
[1] Andhra Univ, AU Coll Engn A, Dept Chem Engg, Visakhapatnam 530003, India
[2] Pandit Deendayal Energy Univ, Dept Chem Engn, Gandhinagar 382007, India
[3] Natl Inst Technol Karnataka, Dept Chem Engn, Mangalore 575025, India
[4] King Abdullah Univ Sci & Technol, Clean Combust Res Ctr, Thuwal 23955, Saudi Arabia
[5] BJ Med Coll & Civil Hosp, Dept Obstet & Gynecol, Ahmadabad 380016, India
关键词:
Microwave;
Pyrolysis;
Graphite;
Polystyrene;
KOH;
Reaction mechanism;
LOW-DENSITY POLYETHYLENE;
CATALYTIC CO-PYROLYSIS;
WASTE POLYPROPYLENE;
ACTIVATED CARBON;
OIL YIELD;
OPTIMIZATION;
HYDROCARBONS;
SUSCEPTOR;
RECOVERY;
D O I:
10.1016/j.psep.2022.08.016
中图分类号:
X [环境科学、安全科学];
学科分类号:
08 ;
0830 ;
摘要:
Microwave-assisted catalytic pyrolysis is a prominent technology for the production of high-quality fuel intermediates and value-added chemicals from polystyrene waste. The objectives of this study were to understand the role of catalyst (KOH) on polystyrene (PS) pyrolysis. Pyrolysis experiments were conducted using a microwave oven at a power of 450 W and a temperature of 600 ?. Graphite susceptor (10 g) was used to achieve the required pyrolysis conditions. In addition, the design of experiments (DoE) with machine learning (ML) was used to understand the loading of PS (5 g, 27.5 g, and 50 g), and KOH (5 g, 7.5 g, and 10 g). The products including oil, gas, and char were collected in every experiment. The average heating rates achieved were in the range of 30-50 ?/min. The specific microwave power (microwave power per unit mass of feedstock) decreased with an increase in PS amount from 90 to 9 W/g. However, the specific microwave energy (microwave energy per unit mass of feedstock) (27-73 kJ/g) was in line with the average heating rate. The maximum yield of pyrolysis oil was found to be 95 wt%, which was obtained with a PS:KOH ratio of 27.5 g: 7.5 g. The oil yield increased from 80 to 95 wt% when the mass of the catalyst increased from 5 to 7.5 g. On the other hand, the gas yield (3-18 wt%) varied significantly and char yield (1-2 wt%) was not influenced. The yields predicted by ML matched well with the experimental yields. This study demonstrated the potential of KOH as a catalyst for PS pyrolysis technology as the formation of aliphatic hydrocarbons in the oil fraction was significantly promoted.
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页码:57 / 67
页数:11
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