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MgO/Al_2O_3 Sorbent for CO_2 Capture

机译:MgO / Al_2O_3吸附剂,用于CO_2捕集

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摘要

The MgO/Al_2O_3 sorbent for CO_2 capture under low temperatures was investigated in a fixed bed. It was found that, with MgO loading of 10 wt %, MgO/Al_2O_3 sorbent showed a maximum CO_2 capture capacity, which originated from the balance of physical adsorption and chemical absorption of the sorbent. The CO_2 capture capacity increased with the water vapor at first and then decreased. Typically, the total CO_2 capture capacities were as high as 0.97 and 1.36 mmol/g, with water vapor concentration of 0 and 13 vol %, respectively, at 60 ℃ with 13 vol % CO_2. The high CO_2 concentration could be approached by the multistage absorption/desorption cycles, during which the sorbent could be regenerated at 350 °C and maintained stable even after 5 cycles. In addition, a deactivation model was proposed that gave good predictions of the CO_2 breakthrough curves. Results showed that sorption rate parameters obtained in the presence of water vapor were found to be larger than the corresponding values in the absence of water vapor. It was possibly caused by increasing the reactivity of the sorbent prior to the sorption of CO_2 in the presence of water vapor.
机译:在固定床中研究了用于低温捕获CO_2的MgO / Al_2O_3吸附剂。已经发现,当MgO负载量为10wt%时,MgO / Al_2O_3吸附剂显示出最大的CO_2捕获能力,这源于吸附剂的物理吸附和化学吸收的平衡。首先,CO_2的捕集能力随水蒸气的增加而降低。通常,在60℃时,CO_2的总捕集能力分别为0.97和1.36 mmol / g,水蒸气浓度分别为0和13 vol%,CO 2为13 vol%。多阶段的吸收/解吸循环可以达到高的CO_2浓度,在此期间,吸附剂可以在350°C下再生,即使经过5个循环也可以保持稳定。此外,提出了一种失活模型,该模型可以很好地预测CO_2突破曲线。结果表明,发现在有水蒸气存在下获得的吸附速率参数大于在无水蒸气存在下获得的吸附速率参数。这可能是由于在水蒸气存在下吸附CO_2之前吸附剂的反应性增加所致。

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  • 来源
    《Energy & fuels》 |2010年第sepaaocta期|p.5773-5780|共8页
  • 作者单位

    State Key Laboratory of Coal Conversion, Institute of Coal Chemistry, Chinese Academy of Sciences, Taiyuan 030001, People's Republic of China,Graduate University of the Chinese Academy of Sciences, Beijing 100049, People's Republic of China;

    rnState Key Laboratory of Coal Conversion, Institute of Coal Chemistry, Chinese Academy of Sciences, Taiyuan 030001, People's Republic of China;

    rnState Key Laboratory of Coal Conversion, Institute of Coal Chemistry, Chinese Academy of Sciences, Taiyuan 030001, People's Republic of China,Graduate University of the Chinese Academy of Sciences, Beijing 100049, People's Republic of China;

    rnState Key Laboratory of Coal Conversion, Institute of Coal Chemistry, Chinese Academy of Sciences, Taiyuan 030001, People's Republic of China;

    rnState Key Laboratory of Coal Conversion, Institute of Coal Chemistry, Chinese Academy of Sciences, Taiyuan 030001, People's Republic of China;

    rnState Key Laboratory of Coal Conversion, Institute of Coal Chemistry, Chinese Academy of Sciences, Taiyuan 030001, People's Republic of China;

    rnState Key Laboratory of Coal Conversion, Institute of Coal Chemistry, Chinese Academy of Sciences, Taiyuan 030001, People's Republic of China;

    rnState Key Laboratory of Coal Conversion, Institute of Coal Chemistry, Chinese Academy of Sciences, Taiyuan 030001, People's Republic of China,Low Carbon Energy Center, Shanghai Advanced Research Institute, Chinese Academy of Sciences, Shanghai 201203,People's Republic of China;

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  • 正文语种 eng
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