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        <identifier>oai:researchdata.se:2024-348/1</identifier>
        <datestamp>2024-07-01</datestamp>
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        <setSpec>principal:slug:lulea-university-of-technology</setSpec>
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          <dc:identifier>https://doi.org/10.5878/40dp-hx03</dc:identifier>
          <dc:title xml:lang="en">Dataset - Self-Heating of Biochar during Postproduction Storage by O₂ Chemisorption at Low Temperatures</dc:title>
          <dc:title xml:lang="sv">Dataset - Self-Heating of Biochar during Postproduction Storage by O₂ Chemisorption at Low Temperatures</dc:title>
          <dc:creator>https://orcid.org/0000-0001-6081-5736</dc:creator>
          <dc:contributor>0000-0001-8372-4386</dc:contributor>
          <dc:subject xml:lang="en">Energy Engineering</dc:subject>
          <dc:subject xml:lang="sv">Energiteknik</dc:subject>
          <dc:description xml:lang="en">Biochar is attracting attention as an alternative carbon/fuel source to coal in the process industry and energy sector. However, it is prone to self-heating and often leads to spontaneous ignition and thermal runaway during storage, resulting in production loss and health risks. This study investigates biochar self-heating upon its contact with O₂ at low temperatures, i.e., 50–300 °C. First, kinetic parameters of O₂ adsorption and CO₂ release were measured in a thermogravimetric analyzer using biochar produced from a pilot-scale pyrolysis process. Then, specific heat capacity and heat of reactions were measured in a differential scanning calorimeter. Finally, a one-dimensional transient model was developed to simulate self-heating in containers and gain insight into the influences of major parameters. The model showed a good agreement with experimental measurement in a closed metal container. It was observed that char temperature slowly increased from the initial temperature due to heat released during O₂ adsorption. Thermal runaway, i.e., self-ignition, was observed in some cases even at the initial biochar temperature of ca. 200 °C. However, if O₂ is not permeable through the container materials, the temperature starts decreasing after the consumption of O₂ in the container. The simulation model was also applied to examine important factors related to self-heating. The results suggested that self-heating can be somewhat mitigated by decreasing the void fraction, reducing storage volume, and lowering the initial char temperature. This study demonstrated a robust way to estimate the cooling demands required in the biochar production process.

The dataset was originally published in DiVA and moved to SND in 2024.</dc:description>
          <dc:description xml:lang="sv">Biochar is attracting attention as an alternative carbon/fuel source to coal in the process industry and energy sector. However, it is prone to self-heating and often leads to spontaneous ignition and thermal runaway during storage, resulting in production loss and health risks. This study investigates biochar self-heating upon its contact with O₂ at low temperatures, i.e., 50–300 °C. First, kinetic parameters of O₂ adsorption and CO₂ release were measured in a thermogravimetric analyzer using biochar produced from a pilot-scale pyrolysis process. Then, specific heat capacity and heat of reactions were measured in a differential scanning calorimeter. Finally, a one-dimensional transient model was developed to simulate self-heating in containers and gain insight into the influences of major parameters. The model showed a good agreement with experimental measurement in a closed metal container. It was observed that char temperature slowly increased from the initial temperature due to heat released during O₂ adsorption. Thermal runaway, i.e., self-ignition, was observed in some cases even at the initial biochar temperature of ca. 200 °C. However, if O₂ is not permeable through the container materials, the temperature starts decreasing after the consumption of O₂ in the container. The simulation model was also applied to examine important factors related to self-heating. The results suggested that self-heating can be somewhat mitigated by decreasing the void fraction, reducing storage volume, and lowering the initial char temperature. This study demonstrated a robust way to estimate the cooling demands required in the biochar production process.

Datasetet har ursprungligen publicerats i DiVA och flyttades över till SND 2024.</dc:description>
          <dc:rights>info:eu-repo/semantics/openAccess</dc:rights>
          <dc:publisher xml:lang="en">Luleå University of Technology</dc:publisher>
          <dc:publisher xml:lang="sv">Luleå tekniska universitet</dc:publisher>
          <dc:date>2022-01-04T00:00:00Z</dc:date>
          <dc:language>eng</dc:language>
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