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Absorption and desorption of carbon dioxide and carbon monoxide in alkanolamine systems.

机译:链烷醇胺系统中二氧化碳和一氧化碳的吸收和解吸。

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摘要

Absorption and desorption of carbon dioxide (CO2) and carbon monoxide (CO) in aqueous alkanolamine solutions are modeled and important kinetic and physical property data are obtained using novel experimental methods. The model is based on the principle of diffusional mass transfer accompanied With fast to very slow chemical reactions in the liquid phase. Fast reactions are represented by CO2 absorption/desorption in aqueous alkanolamines and slow reactions are represented by CO absorption in aqueous diethanolamine (DEA).; The experiments for CO2 absorption and desorption were conducted in a novel hemispherical contactor designed and developed in this work. The absorption experiments were conducted at near atmospheric pressure using pure CO2 saturated with water at 293 to 323 K with initially unloaded solutions. The desorption experiments were performed at 333 to 383 K for CO 2 loadings between 0.02 to 0.7 moles of CO2 per mole of amine using humidified N2 gas as a stripping medium.; The experiments for CO absorption were carried out in a 660 mL batch autoclave reactor at 313 to 413 K with amine concentration between 5 to 50-wt% in distilled water. The partial pressure of CO in the reactor was varied from 800 to 1100 kPa.; The data for CO2 absorption and desorption in aqueous amine systems were analyzed using a new, rigorous mathematical model. The model predicts the experimental results well for all amine systems studied. The results indicate that the theory of absorption with reversible chemical reaction could be used to predict desorption rates. The kinetic data obtained show that desorption experiments could be used to determine both forward and backward rate constants accurately. The absorption experiments on the other hand could only be used to determine forward rate constants.; The data for CO absorption in aqueous diethanolamine (DEA) solutions were analyzed using the model for mass transfer with extremely slow reactions. The data are consistent with a mechanism by which formyl-diethanolamine (DEAF) is predominantly formed by direct insertion of CO into DEA. The data also confirm that DEAF formation via the DEA-formate reaction is relatively slow and reversible.
机译:对烷醇胺水溶液中二氧化碳(CO 2 )和一氧化碳(CO)的吸收和解吸进行了建模,并使用新颖的实验方法获得了重要的动力学和物理性质数据。该模型基于扩散质量转移的原理,伴随着液相中快速到非常慢的化学反应。快反应由在链烷醇胺水溶液中的CO 2 吸收/解吸表示,慢反应由在二乙醇胺水溶液(DEA)中的CO吸收表示。在这项工作中设计和开发的新型半球形接触器中进行了CO 2 吸收和解吸的实验。吸收实验是在接近大气压的条件下,使用纯净的CO 2 在293至323 K时用水饱和,并先加入溶液后进行的。使用湿润的N 2 在每摩尔胺中0.02至0.7摩尔CO 2 的CO 2 负载量在333至383 K下进行了解吸实验>气体作为汽提介质。用于CO吸收的实验在660mL间歇式高压釜反应器中于313至413K下进行,其中胺浓度在蒸馏水中为5至50重量%。反应器中CO的分压为800至1100kPa。使用新的严格数学模型分析了胺水溶液中CO 2 的吸收和解吸数据。该模型可以很好地预测所研究的所有胺体系的实验结果。结果表明,具有可逆化学反应的吸收理论可用于预测解吸速率。所获得的动力学数据表明,解吸实验可用于准确确定正向和反向速率常数。另一方面,吸收实验只能用于确定正向速率常数。使用该模型以极慢的反应进行传质分析了二乙醇胺(DEA)水溶液中CO的吸收数据。该数据与主要通过将CO直接插入DEA中形成甲酰基-二乙醇胺(DEAF)的机理一致。数据还证实通过DEA-甲酸酯反应形成DEAF相对缓慢且可逆。

著录项

  • 作者

    Jamal, Aqil.;

  • 作者单位

    The University of British Columbia (Canada).;

  • 授予单位 The University of British Columbia (Canada).;
  • 学科 Engineering Chemical.
  • 学位 Ph.D.
  • 年度 2002
  • 页码 349 p.
  • 总页数 349
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类 化工过程(物理过程及物理化学过程);
  • 关键词

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