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Experimental evaluation of effect of oxidative degradation of aqueous monoethanolamine on heat of CO2 absorption, vapor liquid equilibrium and CO2 absorption rate

机译:单乙醇胺水溶液降解对二氧化碳吸收,蒸气液平衡和CO2吸收率的实验评价

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Oxidative degradation produces carboxylic acids which are one of the undesirable degradation products and may have a negative impact on the CO2 separation energy of post combustion capture system. 30wt% MEA solutions mixed with carboxylic acids were regarded as a simulated solution for degraded MEA and effect of the additives on heat of CO2 absorption, equilibrium CO2 loading and CO2 absorption rate were experimentally evaluated by using a differential reaction calorimetry (DRC) apparatus, a pressurized vessel to obtain vapor liquid equilibrium (VLE) data and a gas-liquid contactor, respectively. At the range of CO2 loading from 0.0 to 0.3 mol-CO2/mol-amine, the heat of CO2 absorption of the simulated solution increased by around 10% compared to the normal MEA solution. Moreover, the changing-point of the heat of CO2 absorption of the simulated solution moved to a leaner CO2 loading compared to the normal solution. Result of a ~(13)C-NMR analysis also indicated the change in reaction mechanism. At the absorber condition, the equilibrium CO2 loading of the simulated solution decreased by 20% in comparison with the normal solution, where it decreased by 10% at the stripper condition and therefore the cyclic CO2 loading also decreased. Both CO2 absorption rates decreased linearly but in different gradients with increasing CO2 loading. Higher pH in the simulated solution kept higher CO2 absorption rate, which is consistent with the result of pH measurement.
机译:氧化降解产生羧酸,其是不希望的降解产物之一,并且可能对燃烧后燃烧系统的CO 2分离能量产生负面影响。将30wt%与羧酸混合的MEA溶液被认为是用于降解的MEA的模拟溶液和添加剂对CO 2吸收热的影响,通过使用差分反应量热法(DRC)装置进行实验评估平衡CO 2负载和CO 2吸收率加压容器分别获得蒸汽液平衡(VLE)数据和气液接触器。在0.0至0.3mol-CO 2 / mol-胺的CO 2负荷范围内,与正常的MEA溶液相比,模拟溶液的CO2吸收的热量增加约10%。此外,与正常溶液相比,模拟溶液的二氧化碳吸收的热量的变化点移动到稀释剂CO 2负载。 〜(13)C-NMR分析的结果还表明了反应机制的变化。在吸收条件下,与正常溶液相比,模拟溶液的平衡二氧化碳加载量减少了20%,在汽提塔状况下降低10%,因此环状CO 2负载也降低。二氧化碳吸收率均线性降低,但随着CO 2负荷的增加,梯度不同。在模拟溶液中的较高pH保持较高的CO 2吸收率,这与pH测量结果一致。

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