2-氨基-2-甲基-1-丙醇(AMP)和哌嗪(PZ)水溶液中CO2吸收的热力学数据:CO2溶解度、N2O溶解度、CO2吸收热、pH和液体形态

Diego Morlando, Ardi Hartono, Hanna K. Knuutila
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摘要

本文测量了2-氨基-2-甲基-1-丙醇(AMP)和哌嗪(PZ)水溶液中CO2吸收的新热力学数据。在40 ~ 150℃的温度范围内测量了包括CESAR1共混物在内的AMP/PZ水溶液中的CO2溶解度,扩展了之前研究的CO2负载和温度范围。在40 ~ 80℃范围内测量了AMP水溶液和AMP/PZ溶液对CO2的吸收热。结果表明,吸收热随温度变化而变化,但受AMP/PZ浓度比的影响。测定了N2O在CESAR1溶剂中的溶解度,温度为25 ~ 80℃,CO2负荷为0.52 molCO2/molamine。由于盐析作用,N2O溶解度随温度和CO2负荷的变化而降低。实验测定了CO2、AMP和PZ浓度对pH的影响。在CO2浓度为0 ~ 0.80 molCO2/molamine的情况下,测量了CESAR1共混物和1.5 M AMP + 0.75 M PZ的水溶液的液态形态。结果表明:在较低的CO2负荷下(0.40 molCO2/molamine),溶解的CO2主要以pz -氨基甲酸酯形式存在;在较高的CO2负荷下,溶解的CO2主要以碳酸氢盐/碳酸盐和pz -二氨基甲酸酯形式存在;氨基甲酸酯AMP并不是整个二氧化碳浓度范围内的主要产物。实验数据拓宽了现有数据集,并可支持开发严格的热力学模型,这些模型对于使用CESAR1技术评估CO₂捕获的能源需求和环境影响至关重要。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Thermodynamic data for CO2 absorption in aqueous 2-amino-2-methyl-1-propanol (AMP) and piperazine (PZ) solutions: CO2 solubility, N2O solubility, heat of absorption of CO2, pH and liquid speciation
New thermodynamic data for CO2 absorption in aqueous blends of 2-amino-2-methyl-1-propanol (AMP) and piperazine (PZ) are measured in this work. The CO2 solubility in aqueous AMP/PZ solutions, including the CESAR1 blend, was measured at temperatures from 40 to 150 °C, extending the range of CO2 loading and temperature previously investigated.
The heat of absorption of CO2 of aqueous AMP and AMP/PZ solutions was measured from 40 to 80 °C. The results indicate that the heat of absorption is constant with the temperature but it is affected by the AMP/PZ concentration ratio.
The N2O solubility in the CESAR1 solvent was measured from 25 to 80 °C and up to CO2 loading of 0.52 molCO2/molamine. The N2O solubility decreases as a function of temperature and CO2 loading as a result of the salting-out effect.
The effect of CO2, AMP and PZ concentration on the pH was experimentally determined. Liquid speciation for the CESAR1 blend and an aqueous solution of 1.5 M AMP + 0.75 M PZ was measured at CO2 loading from 0 to 0.80 molCO2/molamine. The results indicate that the CO2 dissolved exists mainly as PZ-carbamate at relatively low CO2 loading up to 0.40 molCO2/molamine, while at higher CO2 loading, the bicarbonate/carbonate and PZ-dicarbamate are the major products. The AMP carbamate is not a major product across the whole range of CO2 concentration investigated.
The experimental data broaden the existing dataset and can support the development of rigorous thermodynamic models essential for evaluating energy requirements and environmental impacts of CO₂ capture using CESAR1 technology.
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