A life cycle assessment of the laboratory-scale oxidative liquefaction as the chemical recycling method of the end-of-life wind turbine blades

被引:1
|
作者
Sobek, Szymon [1 ]
Lombardi, Lidia [2 ]
Mendecka, Barbara [2 ]
Mumtaz, Hamza [3 ]
Sajdak, Marcin [4 ]
Muzyka, Roksana [4 ]
Werle, Sebastian [3 ]
机构
[1] Silesian Tech Univ, Dept Heating Ventillat & Dust Removal Technol, Stanis lawa Konarskiego St 20, PL-44100 Gliwice, Poland
[2] Niccolo Cusano Univ, Dept Ind Engn, Via Don Carlo Gnocchi 3, I-00166 Rome, Italy
[3] Silesian Tech Univ, Dept Thermal Technol, Stanis lawa Konarskiego St 22, PL-44100 Gliwice, Poland
[4] Silesian Tech Univ, Dept Air Proteciton, Stanis lawa Konarskiego St 22B, PL-44100 Gliwice, Poland
关键词
Wind turbine blades; Oxidative liquefaction; Wet oxidation; Chemical recycling; LCA; Composite waste; GLASS-FIBER; WASTE;
D O I
10.1016/j.jenvman.2024.121241
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
According to the latest reports, estimated values of 50,000-66 000 t of end-of-life wind turbine blades (WTB) are expected to be decommissioned in Europe in 2025-2030, posing a significant threat from the environmental and waste management perspectives. This study aims to present the preliminary Life Cycle Assessment (LCA) with sensitivity and uncertainty analysis of the lab-scale oxidative liquefaction process of the WTB, as the original method to recover the high-quality glass fibers with simultaneous production of the secondary chemicals: phenols, ketones, acids, and fatty acids, from the oxidation of the epoxy resin from the polymer matrix. The LCA is based on the experimental results of the oxidative liquefaction process carried out on a laboratory scale using a Parr 500 ml batch reactor, at two different conditions sets for the functional unit (FU) of 1 kg of treated WTB. Each of the analyzed scenarios resulted in higher impact indicators compared to the landfilling. The highest quality fibers were obtained at 350 degrees C and 40 wt % H2O2 content resulted in 5.52 +/- 1.20 kgCO2 eq Climate change impact and 97.8 +/- 20.6 MJ of Resource use, fossil per kg of recycled WTB. The lowest quality fiber recovered in char, yet well separated from the matrix obtained at 250 degrees C and the lowest H2O2 content resulted in 0.0953 +/- 0.487 kgCO2 eq Climate change impact and 8.84 +/- 7.90 MJ of Resource use, fossil per kg of recycled WTB. The hot spot and sensitivity analysis indicated, that the oxidizer for the process - hydrogen peroxide, when acquired as a shelf product causes a significant burden on the whole process, with sensitivity ratios on the total impact indicators varying across the categories from 0.56 to 0.99. Substitution of H2O2 with theoretical 0-input oxidizer allowed to significantly lower environmental load of the recycling process, which in all of the analyzed scenarios presented environmental benefits compared to landfilling with recovery of the glass fiber and secondary chemicals.
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页数:15
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