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Attrition-Driven Carbon and Mineral Matter Distribution during Biochar Production from Pine Bark in Fluidized Beds
Luleå University of Technology, Department of Engineering Sciences and Mathematics, Energy Science.ORCID iD: 0000-0002-3283-9674
Consiglio Nazionale Delle Ricerche, STEMS, Napoli 80125, Italy.
Consiglio Nazionale Delle Ricerche, STEMS, Napoli 80125, Italy.
Universitá Degli Studi di Napoli Federico II, Dipartamento di Ingegneria Chimica, Dei Materiali E della Produzione Industriale, Napoli 80125, Italy.
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2026 (English)In: Energy & Fuels, ISSN 0887-0624, E-ISSN 1520-5029, Vol. 40, no 26, p. 14048-14060Article in journal (Refereed) Published
Abstract [en]

During thermochemical conversion inside a fluidized bed, biomass and char particles experience physical breakup, commonly known as attrition. However, its consequences for the distribution of carbon and mineral matter among coarse biochar (referred to hereafter as biocarbon) particles, elutriated fines, and fines retained within the bed remain poorly quantified, despite its direct impact on product yields and properties. This study aims to fill this gap in the literature by devolatilizing pine bark in a lab-scale bubbling fluidized bed reactor at various temperatures, superficial gas velocities, and feed particle sizes. Coarse biocarbon, elutriated fines, and bed material were recovered and characterized for chemical compositions and physical properties. Increased porosity at higher temperatures resulted in greater susceptibility to fragmentation, thereby linking structural degradation with attrition. High gas velocity increased elutriated fines, while the coarse fraction exhibited lower pore volume, indicating the preferential fragmentation and removal of the most porous fragments as fines. A persistent fraction of unrecovered carbon was also identified within the bed, representing a hidden loss pathway that is often neglected in mass closure assessments. Major mineral matter elements exhibited retention levels significantly below 100% in the coarse biocarbon. Notably, phosphorus and calcium were consistently redistributed from the coarse fraction to fines but remained in intermediate bed-associated particles owing to their low volatility under the study conditions. Meanwhile, the increase in total ash, Na, and Al contents above feedstock levels indicates the contamination of coarse biocarbon and elutriated fines with bed material. These observations have direct implications for mass closure evaluation and downstream solids management. Overall, the results show that attrition affects not only fines generation but also carbon and mineral matter distributions. The observed effect can potentially be utilized as a tunable physical fractionation tool whose outcome is governed by the coupled effects of temperature, hydrodynamics, and feedstock properties.

Place, publisher, year, edition, pages
American Chemical Society (ACS), 2026. Vol. 40, no 26, p. 14048-14060
National Category
Energy Engineering
Research subject
Energy Engineering
Identifiers
URN: urn:nbn:se:ltu:diva-112722DOI: 10.1021/acs.energyfuels.6c01922ISI: 001800629800001Scopus ID: 2-s2.0-105043534669OAI: oai:DiVA.org:ltu-112722DiVA, id: diva2:1959256
Note

Full text license: CC BY 4.0;

Funder: Università degli Studi di Napoli Federico II

Available from: 2025-05-19 Created: 2025-05-19 Last updated: 2026-08-17Bibliographically approved
In thesis
1. Biocarbon Production in Fluidized Bed Reactors
Open this publication in new window or tab >>Biocarbon Production in Fluidized Bed Reactors
2025 (English)Licentiate thesis, comprehensive summary (Other academic)
Alternative title[sv]
Biokolproduktion i fluidiserad bädd reaktörer
Abstract [en]

This study explores the production of biocarbon from forest biomass through pyrolysis in fluidized bed reactors, emphasizing the relationship between the operating conditions, ash behavior, and physicochemical properties of the resulting solid biocarbon. Fluidized bed reactors offer distinct advantages for biocarbon production, including efficient heat transfer, isothermal operation, and scalability. These characteristics make them particularly suitable for integration into existing energy infrastructures.

A key strategy investigated in this study is the use of a weakly oxidizing atmosphere composed of recycled flue gases from combustion processes as the fluidization medium. This approach enables heat integration with fluidized bed boilers and reduces the need for external inert gases, thereby lowering operational costs and improving the overall energy efficiency and circularity of the system. The impact of this atmosphere on biocarbon yield and composition was studied in detail, particularly regarding its influence on the behavior of ash-forming elements and textural properties.

Special attention is given to the transformation and retention of ash-forming elements, such as potassium and phosphorus, which affect the suitability of biocarbon for industrial applications. The experimental and modeling results show that fluidized bed conditions favor the selective removal and distribution of these elements. Analytical techniques, including inductively coupled plasma (ICP), scanning electron microscopy with energy-dispersive X-ray spectroscopy (SEM-EDS), and thermodynamic equilibrium calculations (TECs), were used to assess the mechanisms of ash transformation.

In parallel, the evolution of particle properties, such as size, density, porosity, and surface area, was evaluated under different conversion regimes. Structural degradation owing to attrition and fragmentation was found to play significant roles in carbon retention and fines generation. Preliminary pilot-scale tests conducted with a different woody feedstock showed trends similar to those observed at the laboratory scale when comparable devolatilization severities were applied, reinforcing the transferability of key process–property relationships.

Overall, these findings support the development of integrated and sustainable fluidized bed systems for biocarbon production, offering practical pathways to reduce fossil carbon use and improve resource efficiency in biomass valorization processes.

Place, publisher, year, edition, pages
Luleå: Luleå University of Technology, 2025. p. 30
Series
Licentiate thesis / Luleå University of Technology, ISSN 1402-1757
Keywords
biocarbon, fluidized bed reactors, devolatilization, pine bark, ash-forming elements, physical evolution, structural evolution
National Category
Energy Engineering
Research subject
Energy Engineering
Identifiers
urn:nbn:se:ltu:diva-112720 (URN)978-91-8048-843-3 (ISBN)978-91-8048-844-0 (ISBN)
Presentation
2025-09-26, E632, Luleå University of Technology, Luleå, 09:00 (English)
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Supervisors
Available from: 2025-05-20 Created: 2025-05-19 Last updated: 2026-06-01Bibliographically approved

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Arango Durango, EduardoUmeki, Kentaro

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