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Copyrolysis of Waste Paint Oil and Algae Biomass to Produce High-Energy Biochar: Physicochemical Characterization and Solid-Fuel Performance

Parthasarathi MishraDepartment of Mechanical Engineering, Government College of Engineering, Keonjhar, Jamunalia, Keonjhar, IndiaC. MeeraSchool of Management Studies, Karpagam College of Engineering, Coimbatore, IndiaSrinivas TadepalliImam Muhammad Ibin Saud Islamic University, Riyadh, Department of Chemical Engineering-College of Engineering, CITY, Kingdom of Saudi ArabiaT. MohankumarMechanical Engineering, Thirumalai Engineering College, Kanchipuram, IndiaS. KarvendhanD. HemalathaDepartment of Electrical and Electronics Engineering, St.Josephs Institute of Technology, Chennai, IndiaS. DeepankumarDepartment of Robotics and Automation, Erode Sengunthar Engineering College, Erode, IndiaMadaminov Sanjarbek Maxmudjon UgliHead of Department of Transport systems, Urgench state university named after Abu Rayhan Biruni, Urgench city, Uzbekistan
2026en
ABI

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Abstract This study investigates the copyrolysis of waste paint oil (WPO) and algae biomass as an integrated waste-to-energy pathway for producing high-energy biochar while mitigating the environmental risks associated with WPO disposal. Copyrolysis experiments were conducted in a laboratory-scale fixed-bed reactor using WPO–algae weight ratios of 1 : 0.5 to 1 : 1.5 under an inert nitrogen atmosphere (150 mL/min), with temperatures ranging from 400 to 600°C, a heating rate of 10°C/min, and a residence time of 60 min. The physicochemical properties of WPO (density 0.88–0.89 g/mL; kinematic viscosity 4.5–5.0 mm2/s) were controlled to ensure feedstock consistency. The resulting biochars exhibited markedly improved solid-fuel characteristics compared to single-feed pyrolysis. Fixed carbon content increased from 65.3 to 72.8 wt % (ASTM D3172), exceeding the baseline value of 62.4 wt %, while volatile matter decreased to 16.2–21.5 wt %. The higher heating value (HHV) increased systematically from 29.7 to 32.5 MJ/kg (ASTM D5865), reflecting enhanced carbonization and aromatic structure development. Ultimate analysis confirmed increased carbon content (72.4–76.0 wt %) and reduced H/C ratios (0.58–0.70), indicative of synergistic aromatization during copyrolysis. Structural and thermal analyses supported these findings. FTIR spectra revealed intensified aromatic C=C stretching bands at ~1600 cm–1, with peak intensities increasing by up to 2.1× at higher algae ratios. GC–MS analysis of volatile fractions identified stable polyaromatic compounds, including naphthalene (18–25%) and phenanthrene (12–19%) within the C9–C24 range. Thermogravimetric analysis (TGA/DTG) demonstrated enhanced thermal stability, with onset decomposition temperatures exceeding 420°C and three distinct degradation stages: moisture removal (30–150°C), devolatilization (150–450°C; 25–35 wt % mass loss), and fixed carbon oxidation (450–750°C). Activation energy values determined using the Kissinger–Akahira–Sunose method increased from 125 to 142 kJ/mol, confirming the formation of stronger aromatic carbon networks. Fixed-bed combustion tests conducted at 850–950°C (λ = 1.2–1.4) validated the fuel performance of the co-pyrolyzed biochars, yielding ignition temperatures of 360–375°C, reactivity indices (Rᵢ) of 0.85–1.42 min–1, and favorable ash fusion characteristics (IDT/HT/FT: 780/790/1120–1280°C; ASTM D1857) with moderate slagging indices (Rs = 4.2–6.8). Gaseous emissions remained low, with CO concentrations of 120–180 ppm and NOx levels of 85–110 ppm. The biochars also exhibited well-developed hierarchical porosity and BET surface areas of 110–130 m2/g. Overall, the results demonstrate that copyrolysis of waste paint oil and algae biomass is an effective industrial waste valorization strategy, producing thermally stable, high-energy biochar suitable for 30–50% co-firing blends with sub-bituminous coal, while simultaneously addressing hazardous waste management challenges.

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