Yayın: Fraction-resolved pyrolysis behavior, conversion-dependent kinetics, and predictive severity framework for engineered biochars from fig-processing residues
| dc.contributor.author | Soomro, Ahsanullah | |
| dc.contributor.author | Kocer, Anil Tevfik | |
| dc.contributor.author | Balkanli, Didem | |
| dc.date.accessioned | 2026-06-27T15:37:02Z | |
| dc.date.issued | 2026 | |
| dc.description.abstract | Industrial fig processing generates seed-rich and skin-rich residues that remain underutilized as biochar precursors. This study treated fractionation as a process-design variable by comparing separately recovered fig seed and fig skin under matched pyrolysis conditions and multi-rate thermogravimetric analysis. Across a severity matrix of 350-500 degrees C with varied heating rates and holding times, biochar yield decreased from 30.3 to 24.52% for fig seed and from 32.0 to 27.73% for fig skin, with fig skin consistently retaining more solid under identical programmes. ATR-FTIR analysis revealed different carbonization pathways: seed-derived chars showed stronger attenuation of O-H and aliphatic C-H bands together with a more pronounced condensed/aromatic region, whereas skin-derived chars retained clearer oxygen-containing features. TG-DTG analysis at 5-40 degrees C min(-1) showed contrasting devolatilization behavior, with fig seed dominated by a broad mid-temperature event and fig skin characterized by an early dominant peak followed by a secondary higher-temperature contribution. Gaussian DTG-stage partitioning converted these differences into quantitative descriptors, with fig skin retaining a persistent Stage I contribution ( = 400 degrees C; up to 52.17%). Isoconversional analysis showed higher and more conversion-sensitive apparent activation energies for fig seed (similar to 107-327 kJ mol(-1)) than for fig skin (similar to 74-151 kJ mol(-1)). DAEM analysis supported this contrast, while screening gate-to-gate LCA showed that midpoint burdens were governed mainly by programme-level electricity demand, with Program 3 giving the lowest burdens for both fractions. These results support a fraction-specific severity framework for targeted biochar production. | en |
| dc.description.sponsorship | European Union [101126655] | |
| dc.description.sponsorship | Scientific and Technological Research Council of Turkiye (TUEBITAK) [123C459] | |
| dc.description.uri | https://doi.org/10.1016/j.biombioe.2026.109556 | |
| dc.identifier.doi | 10.1016/j.biombioe.2026.109556 | |
| dc.identifier.eissn | 1873-2909 | |
| dc.identifier.issn | 0961-9534 | |
| dc.identifier.uri | https://hdl.handle.net/20.500.14981/72054 | |
| dc.identifier.volume | 214 | |
| dc.identifier.wos | 001768629700001 | |
| dc.language.iso | eng | |
| dc.publisher | PERGAMON-ELSEVIER SCIENCE LTD | |
| dc.relation.ispartof | BIOMASS & BIOENERGY | |
| dc.rights | openAccess | |
| dc.subject | Fig-processing residues | |
| dc.subject | Biochar | |
| dc.subject | Pyrolysis | |
| dc.subject | Isoconversional kinetics | |
| dc.subject | Distributed activation energy model | |
| dc.subject | Life-cycle assessment | |
| dc.subject | ACTIVATION-ENERGY MODEL | |
| dc.subject | THERMOGRAVIMETRIC ANALYSIS | |
| dc.subject | MASTER PLOTS | |
| dc.subject | BIO-OIL | |
| dc.subject | BIOMASS | |
| dc.subject | CARBONIZATION | |
| dc.subject | CELLULOSE | |
| dc.subject | NUMBER | |
| dc.subject | Agriculture | |
| dc.subject | Biotechnology & Applied Microbiology | |
| dc.subject | Energy & Fuels | |
| dc.title | Fraction-resolved pyrolysis behavior, conversion-dependent kinetics, and predictive severity framework for engineered biochars from fig-processing residues | |
| dc.type | Article | |
| dspace.entity.type | Publication | |
| local.import.source | WOS |