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Parametric study on the regeneration heat requirement of an amine-based solid adsorbent process for post-combustion carbon capture

机译:胺基固体吸附剂燃烧后碳捕集的再生热量需求参数研究

摘要

The thermal energy required for regeneration of CO2-rich adsorbents or absorbents is usually regarded as the most important criterion to evaluate different materials and processes for application in commercialscale CO2 capture systems. It is expected that the regeneration heat can be greatly reduced by replacing the mature aqueous monoethanolamine (MEA) technology with amine-based solid adsorbents capturing systems, due to the much lower heat capacity of solid adsorbents comparing to aqueous MEA and the avoidance of evaporating a large amount of water in the regenerator. Comparing to the MEA technology, the regeneration heat for solid adsorbent based systems has not received adequate attention especially on the impacts of process related parameters. Further, the methodologies used in previous investigations to calculate the regeneration heat may have deficiencies in defining the working capacities, adopting proper heat recovery strategies and/or evaluating the effect of moisture co-adsorption. In this study, an energy equation to calculate the regeneration heat has been revised and proposed to systematically evaluate the most important parameters affecting the regeneration heat, including the physical properties of the adsorbents and process related variables including the heat of adsorption, specific heat capacity, working capacity, moisture adsorption of the polyethyleneimine (PEI)/silica adsorbent, the swing temperature difference and the degree of heat recovery. Based on the parametric analysis, the calculated regeneration heat for the PEI/silica adsorbent based system is found to be around 2.46 GJ/tCO2, which is much lower than the value of 3.9 GJ/tCO2 for a typical aqueous MEA system and is also lower than 3.3 GJ/tCO2 for an advanced MEA system. Sensitivity analysis of all the parameters has also been conducted and the results have shown that working capacity, moisture adsorption and heat recovery ratios are the most influential factors. With more proficiency and development in the energy efficient process designs, the advantages of a solid adsorbent based capturing system over typical MEA systems will be justified.
机译:再生富含CO2的吸附剂或吸收剂所需的热能通常被认为是评估用于商业规模CO2捕集系统的不同材料和工艺的最重要标准。可以预期,通过将成熟的单乙醇胺水溶液(MEA)替换为基于胺的固体吸附剂捕获系统,可以大大降低再生热量,这是因为与MEA水溶液相比,固体吸附剂的热容低得多,并且避免了蒸发。再生器中有大量的水。与MEA技术相比,基于固体吸附剂的系统的再生热量尚未得到足够的重视,尤其是在与过程相关的参数的影响方面。此外,先前研究中用于计算再生热量的方法在定义工作能力,采用适当的热量回收策略和/或评估湿气共吸附效果方面可能存在缺陷。在这项研究中,对用于计算再生热量的能量方程式进行了修订,并提出了系统地评估影响再生热量的最重要参数,包括吸附剂的物理性质和与过程相关的变量,包括吸附热,比热容,工作能力,聚乙烯亚胺(PEI)/二氧化硅吸附剂的水分吸附,摆动温度差和热回收程度。基于参数分析,发现基于PEI /二氧化硅吸附剂的系统的计算再生热约为2.46 GJ / tCO2,这比典型的水性MEA系统的3.9 GJ / tCO2的值低得多,并且也较低先进的MEA系统的排放量不超过3.3 GJ / tCO2。还对所有参数进行了敏感性分析,结果表明,工作能力,水分吸附和热回收率是最重要的影响因素。随着在节能工艺设计方面的进一步提高和发展,基于固体吸附剂的捕集系统相对于典型MEA系统的优势将得到证明。

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