A thermo-kinetic study on co-pyrolysis of oil shale and polyethylene terephthalate using TGA/FT-IR

被引:19
|
作者
Ozsin, Gamzenur [1 ]
Kilic, Murat [2 ]
Apaydin-Varol, Esin [2 ]
Putun, Ayse Eren [3 ]
Putun, Ersan [4 ]
机构
[1] Bilecik Seyh Edebali Univ, Fac Engn, Dept Chem Engn, TR-11210 Bilecik, Turkey
[2] Eskisehir Tech Univ, Fac Engn, Dept Chem Engn, TR-26555 Eskisehir, Turkey
[3] Anadolu Univ, Fac Engn, Dept Chem Engn, TR-26555 Eskisehir, Turkey
[4] Anadolu Univ, Fac Engn, Dept Mat Sci & Engn Engn, TR-26555 Eskisehir, Turkey
关键词
Pyrolysis; Kinetics; PET; Oil Shale; Synergetic Effect; TGA; FT-IR; LOW-DENSITY POLYETHYLENE; FIXED-BED; SEWAGE-SLUDGE; BIOMASS; DEGRADATION; MIXTURES; THERMOGRAVIMETRY; GASIFICATION; POLYSTYRENE; COMBUSTION;
D O I
10.1007/s11814-020-0614-2
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
This study explored the effects of polyethylene terephthalate (PET) blending during the pyrolysis of oil shale (OS). Dynamic pyrolysis and co-pyrolysis tests at heating rates in the range from 5 to 40 degrees C/min were carried out using a thermogravimetric analyzer (TGA) coupled to a Fourier transform infrared spectrometer (FT-IR) to determine the kinetic parameters of the process and for online detection of evolved gasses. Pyrolytic decomposition of OS included a multi-stage decomposition process, while PET decomposed only in a single step. The kinetics of pyrolysis and co-pyrolysis was determined via model-free iso-conversional methods, namely Friedman, FWO, Starink, Vyazovkin, in a conversion degree range of 0.1-0.9. The kinetic models were validated with the obtained data to describe pyrolytic and co-pyrolytic degradation mechanisms, and the regression coefficients were between 0.9823 and 0.9999. The results showed that the activation energy of co-pyrolysis was evidently lower than that of PET or OS pyrolysis. This led to the conclusion that co-pyrolysis could be a potential method for obtaining shale oil due to the synergy between OS and PET.
引用
收藏
页码:1888 / 1898
页数:11
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