放热反应
生物炭
吸热过程
活化能
微型多孔材料
材料科学
化学工程
活性炭
流化床
多孔性
吸附
碳纤维
比表面积
废物管理
放热过程
打赌理论
过程(计算)
化学
产量(工程)
流化床燃烧
体积流量
多孔介质
流量(数学)
作者
Reyhane Aghaei Dinani,Neda ASASIAN KOLUR,Michael Harasek
出处
期刊:Molecules
[Multidisciplinary Digital Publishing Institute]
日期:2026-02-20
卷期号:31 (4): 724-724
被引量:2
标识
DOI:10.3390/molecules31040724
摘要
Biochar activation is critical for producing high-performance adsorbents; however, conventional activation methods are energy-intensive and difficult to control, particularly when air is used as an activating agent. This study investigates CO2–air co-activation in a laboratory-scale fluidized bed reactor as an energy-efficient alternative. Experiments were conducted at 750–850 °C under varying gas flow rates with a constant CO2/O2 ratio. Optimal properties were achieved at 800 °C and 0.2–0.3 L/min CO2, yielding a maximum BET surface area of 479 m2/g, a micropore contribution of 42%, and controlled carbon conversion (~25–35% yield). Aspen Plus equilibrium simulations also confirm that CO2-only activation remains endothermic (heat duty up to +0.07 kW), air-only activation becomes strongly exothermic (down to −0.13 kW), while the CO2–air mixture exhibits near-thermoneutral to mildly exothermic behavior (+0.13 to −0.10 kW), thereby reducing external energy demand potentially by approximately 60–70% compared with CO2-only activation and significantly improving process stability. These results demonstrate that CO2–air co-activation offers a practical route to produce high-quality activated biochar with controlled porosity and improved energy efficiency.
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