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Application of the microchannel reactor to carbon dioxide absorption

机译:微通道反应器在二氧化碳吸收中的应用

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摘要

In this study, the absorption of carbon dioxide (CO2) in a microchannel reactor by use of the three solvents monoethanolamine (MEA), diethanolamine (DEA) and activated methyldiethanolamine (a-MDEA) was investigated under different operating conditions, including temperature, solvent and gas flow rates, and amine concentration. The results show that increasing solvent flow rate or amine concentration has effect of increasing the mass transfer flux. Raising the gas flow rate increased the mass transfer flux for MEA and DEA, while for a-MDEA it initially increased and then reduced the flux. The temperature was found to be a less effective parameter. Additionally, the performance of the microreactor in the enhancement of the absorption rate was demonstrated. The optimum molar flux of volumetric mass transfer was determined to be 12,826, 11,374 and 8241 kmol per cubic meter-hour for MEA, DEA and a-MDEA respectively. (C) 2019 Published by Elsevier Ltd.
机译:在这项研究中,研究了在不同的操作条件(包括温度,溶剂)下,使用三种溶剂单乙醇胺(MEA),二乙醇胺(DEA)和活性甲基二乙醇胺(a-MDEA)在微通道反应器中吸收二氧化碳(CO2)的情况。气体流速和胺浓度。结果表明,增加溶剂流速或胺浓度具有增加传质通量的作用。增大气体流速会增加MEA和DEA的传质通量,而对于a-MDEA则首先增加,然后减小通量。发现温度是不太有效的参数。另外,证明了微反应器在吸收率提高方面的性能。对于MEA,DEA和α-MDEA,确定的最佳质量传质摩尔通量分别为每立方米12,826、11,374和8241 kmol /立方米。 (C)2019由Elsevier Ltd.发布

著录项

  • 来源
    《Journal of Cleaner Production》 |2019年第10期|723-732|共10页
  • 作者单位

    Kermanshah Univ Technol, Fac Energy, Dept Chem Engn, Kermanshah, Iran;

    Univ Sao Paulo, Sch Engn, Dept Chem Engn, Caixa Postal 61548, BR-05424970 Sao Paulo, SP, Brazil|Imperial Coll London, Dept Chem Engn, South Kensington Campus, London SW7 2AZ, England;

    Kermanshah Univ Technol, Fac Energy, Dept Chem Engn, Kermanshah, Iran;

    Kermanshah Univ Technol, Fac Energy, Dept Chem Engn, Kermanshah, Iran;

  • 收录信息
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

    Microreactor; CO2 capture; Amine solvent;

    机译:微反应器;CO2捕集;胺溶剂;

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