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Fraction-resolved pyrolysis behavior, conversion-dependent kinetics, and predictive severity framework for engineered biochars from fig-processing residues

dc.contributor.authorSoomro, Ahsanullah
dc.contributor.authorKocer, Anil Tevfik
dc.contributor.authorBalkanli, Didem
dc.date.accessioned2026-06-27T15:37:02Z
dc.date.issued2026
dc.description.abstractIndustrial 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.sponsorshipEuropean Union [101126655]
dc.description.sponsorshipScientific and Technological Research Council of Turkiye (TUEBITAK) [123C459]
dc.description.urihttps://doi.org/10.1016/j.biombioe.2026.109556
dc.identifier.doi10.1016/j.biombioe.2026.109556
dc.identifier.eissn1873-2909
dc.identifier.issn0961-9534
dc.identifier.urihttps://hdl.handle.net/20.500.14981/72054
dc.identifier.volume214
dc.identifier.wos001768629700001
dc.language.isoeng
dc.publisherPERGAMON-ELSEVIER SCIENCE LTD
dc.relation.ispartofBIOMASS & BIOENERGY
dc.rightsopenAccess
dc.subjectFig-processing residues
dc.subjectBiochar
dc.subjectPyrolysis
dc.subjectIsoconversional kinetics
dc.subjectDistributed activation energy model
dc.subjectLife-cycle assessment
dc.subjectACTIVATION-ENERGY MODEL
dc.subjectTHERMOGRAVIMETRIC ANALYSIS
dc.subjectMASTER PLOTS
dc.subjectBIO-OIL
dc.subjectBIOMASS
dc.subjectCARBONIZATION
dc.subjectCELLULOSE
dc.subjectNUMBER
dc.subjectAgriculture
dc.subjectBiotechnology & Applied Microbiology
dc.subjectEnergy & Fuels
dc.titleFraction-resolved pyrolysis behavior, conversion-dependent kinetics, and predictive severity framework for engineered biochars from fig-processing residues
dc.typeArticle
dspace.entity.typePublication
local.import.sourceWOS

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