首页> 外文期刊>Chemical Engineering Science >Heat duty, heat of absorption, sensible heat and heat of vaporization of 2-Amino-2-Methyl-1-Propanol (AMP), Piperazine (PZ) and Monoethanolamine (MEA) tri-solvent blend for carbon dioxide (CO2) capture
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Heat duty, heat of absorption, sensible heat and heat of vaporization of 2-Amino-2-Methyl-1-Propanol (AMP), Piperazine (PZ) and Monoethanolamine (MEA) tri-solvent blend for carbon dioxide (CO2) capture

机译:用于二氧化碳(CO2)捕获的热量,吸收热量,吸收热和蒸发热和蒸发热量,哌嗪(PZ)和单乙醇胺(MEA)三溶剂共混物用于二氧化碳(CO2)捕获

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摘要

Chemical absorption using reactive amines for carbon dioxide (CO2) capture is characterized by absorption heat, heat of desorption and heat duty for regeneration (Qreg, kJ/mol CO2). This study experimentally investigated the heat duty of tri-solvent blends containing AMP-PZ-MEA and the individual contribution of desorption heat, sensible heat and heat of vaporization to heat duty. The experimental conditions for absorption were 15 v/v% CO2 at 40 degrees C and atmospheric pressure while desorption was carried out 90 degrees C for loaded amine also at atmospheric pressure. The heat of desorption was experimentally determined using the specific heat capacity (kJ/kg degrees C) difference between the CO2 free and CO2 saturated amine solutions at the stated absorption conditions. Results showed that the heat duty of all the tri-solvent blends was significantly lower than that of the standard 5 kmol/m(3) MEA. Interestingly, the AMP-PZ-MEA tri-solvent blends exhibited only slightly lower heats of absorption when compared to MEA; however, they also showed significantly lower sensible heat and slightly lower heat of vaporization. Consequently, the tri-solvent blends exhibited significantly lower heat duties than the standard 5 kmol/m(3) MEA. In addition, a model analogous to a power law kinetic model was developed and used to predict the specific heat capacity of the AMP-PZ-MEA tri-solvent blends. The model accurately predicted the experimental results with an AAD of 0.59%. The overall results highlight the potential of using AMP-PZ-MEA blends for CO2 capture. (C) 2017 Elsevier Ltd. All rights reserved.
机译:使用反应性胺用于二氧化碳(CO2)捕获的化学吸收的特征在于吸收热量,再生的解吸和热占用热量(Qreg,KJ / Mol CO 2)。本研究通过实验研究了含有AMP-PZ-MEA的三溶剂共混物的热义,以及解吸热,显性热量和蒸发热量的个体贡献。吸收的实验条件为40℃和大气压,大气压为15V / v%CO 2,同时在大气压下进行100摄氏度的胺进行90℃。在所述吸收条件下使用CO 2自由和CO 2饱和胺溶液之间的特定热容量(KJ / kg型C)差来实验解吸热量。结果表明,所有三溶剂共混物的热义明显低于标准5 kmol / m(3)Mea。有趣的是,与MEA相比,AMP-PZ-MEA三溶剂共混物仅表现出略微较低的吸收热量;然而,它们还表现出显着降低的明显热和略微较低的蒸发热。因此,三溶剂共混物比标准5 kmol / m(3)MEA显着呈显着较低。此外,开发了一种类似于动力法动力学模型的模型,并用于预测AMP-PZ-MEA三溶剂共混物的比热容。该模型准确地预测了0.59%的AAD的实验结果。总体结果突出了使用AMP-PZ-MEA混合物进行二氧化碳捕获的潜力。 (c)2017 Elsevier Ltd.保留所有权利。

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