Pyrolysis of Automotive Shredder Residue (ASR): Thermogravimetry, In-Situ Synchrotron IR and Gas-Phase IR of Polymeric Components

被引:1
|
作者
Kohli, Isha [1 ]
Srivatsa, Srikanth Chakravartula [1 ]
Das, Oisik [2 ]
Devasahayam, Sheila [3 ]
Singh Raman, R. K. [1 ,4 ]
Bhattacharya, Sankar [1 ]
机构
[1] Monash Univ, Dept Chem & Biol Engn, Clayton, Vic 3800, Australia
[2] Lulea Univ Technol, Dept Civil Environm & Nat Resources Engn, S-97187 Lulea, Sweden
[3] Curtin Univ, WASM Minerals Energy & Chem Engn, Perth, WA 6845, Australia
[4] Monash Univ, Dept Mech & Aerosp Engn, Clayton, Vic 3800, Australia
基金
澳大利亚研究理事会;
关键词
automotive shredder residue; thermogravimetry; in situ synchrotron IR; gas-phase IR; heating rates; activation energy; THERMAL-DEGRADATION; PLASTIC WASTE; KINETICS; REACTOR;
D O I
10.3390/polym15173650
中图分类号
O63 [高分子化学(高聚物)];
学科分类号
070305 ; 080501 ; 081704 ;
摘要
This article reports the characterisation of pyrolysis of automotive shredder residue using in situ synchrotron IR, gas-phase IR, and thermal analyses to explore if the automotive shredder residue can be converted into value-added products. When heating to similar to 600 degrees C at different heating rates, thermal analyses suggested one-to two-stage pyrolysis. Transformations in the first stage, at lower temperatures, were attributed to the degradation of carbonyl, hydroxyl, or carboxyl functional stabilisers (aldehyde and ether impurities, additives, and stabilisers in the ASR). The second stage transformations, at higher temperatures, were attributed to the thermal degradation of the polymer char. Simultaneous thermal analyses and gas-phase IR spectroscopy confirmed the evolution of the gases (alkanes (CH4), CO2, and moisture). The synchrotron IR data have demonstrated that a high heating rate (such as 150 degrees C/min) results in an incomplete conversion of ASRs unless sufficient time is provided. The thermogravimetry data fit the linearised multistage kinetic model at different heating rates. The activation energy of reactions varied between 24.98 and 124.94 kJ/mol, indicating a surface-controlled reaction exhibiting high activation energy during the initial stages and a diffusion and mass transfer control showing lower activation energy at the final stages. The corresponding frequency factors were in the range of 3.34 x 10(13)-5.68 x 10(1) mg(-1)/min for different pyrolysis stages. The evolution of the functional groups decreased with an increase in the heating rate.
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页数:40
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