Department of Chemical and Biomolecular Engineering, Sogang University , 35 Baekbeom-ro, Mapo-gu, Seoul 121-742, Korea.
Environ Sci Technol. 2015 Feb 3;49(3):1478-85. doi: 10.1021/es504684x. Epub 2015 Jan 20.
Among various CO2 capture processes, the aqueous amine-based absorption process is considered the most promising for near-term deployment. However, the performance evaluation of newly developed solvents still requires complex and time-consuming procedures, such as pilot plant tests or the development of a rigorous simulator. Absence of accurate and simple calculation methods for the energy performance at an early stage of process development has lengthened and increased expense of the development of economically feasible CO2 capture processes. In this paper, a novel but simple method to reliably calculate the regeneration energy in a standard amine-based carbon capture process is proposed. Careful examination of stripper behaviors and exploitation of energy balance equations around the stripper allowed for calculation of the regeneration energy using only vapor-liquid equilibrium and caloric data. Reliability of the proposed method was confirmed by comparing to rigorous simulations for two well-known solvents, monoethanolamine (MEA) and piperazine (PZ). The proposed method can predict the regeneration energy at various operating conditions with greater simplicity, greater speed, and higher accuracy than those proposed in previous studies. This enables faster and more precise screening of various solvents and faster optimization of process variables and can eventually accelerate the development of economically deployable CO2 capture processes.
在各种 CO2 捕获工艺中,水基胺基吸收工艺被认为是最有前途的近期部署工艺。然而,新开发溶剂的性能评估仍然需要复杂和耗时的程序,例如中试工厂测试或严格模拟器的开发。在工艺开发的早期阶段缺乏准确和简单的能量性能计算方法,延长和增加了经济可行的 CO2 捕获工艺的开发成本。本文提出了一种新颖但简单的方法,可可靠地计算标准胺基碳捕获工艺中的再生能量。通过仔细检查汽提器的行为并利用汽提器周围的能量平衡方程,可以仅使用汽液平衡和热量数据来计算再生能量。通过与两种知名溶剂(MEA 和哌嗪(PZ))的严格模拟进行比较,验证了所提出方法的可靠性。与之前的研究相比,该方法可以在各种操作条件下以更高的简单性、速度和准确性来预测再生能量。这可以更快、更精确地筛选各种溶剂,并更快地优化工艺变量,最终可以加速经济可行的 CO2 捕获工艺的开发。