2025 AIChE Annual Meeting

(399j) Evaluation of Regeneration Heat for Propylene Oxide-Functionalized Amine-Based Macroporous Silica Using Simulated Ngcc Flue Gas

Authors

Dongho Lee - Presenter, Korea Institute of Energy Research
Ji Hyeon Whang, KOREA INSTITUTE OF ENERGY RESEARCH
Yooseob Won, Korea institute of Energy Researcher
Yongseon Lee, KOREA INSTITUTE OF ENERGY RESEARCH
Ara Cho, Korea Institute of Energy Research
Dong-Kyu Moon, Yonsei University
Jae-Young Kim, Korea Institute of Energy Research
Yuntae Hwang, Korea institute of Energy Researcher
Sungho Jo, Korea Institute of Energy Research
Young Cheol Park, Korea Institute of Energy Research
Ki Bong Lee, Korea University
The macropore silica (MPS) adsorbent functionalized with pentaethylenehexamine (PEHA) at a 2:0 molar ratio using propylene oxide (PO) (2.0PO-PEHA/MPS) showed effective applicability not only to coal-fired power plant flue gas (15% CO₂) but also to NGCC flue gas (4% CO₂), as confirmed by CO₂ isotherm measurements. Based on this, the CO₂ and H₂O adsorption behaviors of 2.0 PO-PEHA/MPS and the regeneration heat requirements were experimentally and computationally evaluated using thermogravimetric analysis (TGA) and Temperature-programmed adsorption and desorption (TPAD) apparatus. By investigating the CO₂ uptake at various temperatures, the optimal adsorption and regeneration temperatures were determined to be 50℃ and 120℃, respectively. Additionally, periodic adsorption-regeneration experiments were conducted under adsorption conditions (4% CO₂, 3% H₂O, N₂ balance, 50℃) and regeneration conditions (100% CO₂, 120℃) to assess the adsorption behavior and stability over 20 cycles. The 2.0PO-PEHA/MPS adsorbent maintained stable working capacity with minimal decrease (< 8% decrease) from the second to the twentieth cycle. The H₂O uptake in TGA was calculated by subtracting the CO₂ uptake of 9.02 wt.% from the total CO₂ and H₂O amount of 13.43 wt.% measured in the cycle experiment. However, TGA overestimated the H₂O uptake to 4.41 wt.% by not considering the adsorption characteristics of CO₂ and H₂O, resulting in quantitative errors. In contrast, using the TPAD apparatus to analyze the simultaneous adsorption characteristics of CO₂ and H₂O, the CO₂ uptake was measured at 10.28 wt.% and the H₂O uptake at 3.51 wt.%, confirming that TPAD provides more reliable results than TGA. Based on the CO₂ and H₂O uptake measured by TPAD, the theoretical regeneration heat calculated was 2.96 GJ/tCO₂ at 120℃, showing the lowest value. This study demonstrates that the 2.0 PO-PEHA/MPS adsorbent can be effectively applied to CO₂ adsorption from NGCC flue gas and suggests the potential to maximize the efficiency of CO₂ capture processes by optimizing adsorption performance and regeneration heat requirements.