In recent years, significant attention has been drawn to the advancement of high-performance solid acid catalysts, which enhance the CO2 desorption efficiency and concurrently lower energy requirements. Although solid acid catalysts show promise in reducing regeneration energy for amine-based CO2 capture, achieving an optimal balance between activity, cost, and stability remains a major challenge. Herein a series of solid acid catalysts were prepared by modifying attapulgite (ATP) with various CuOx loading, and the effect of Cu modification on CO2 desorption performance was compared systematically. The results showed that CO2 desorption performance of the as-prepared catalysts was in an order of 2/1-CuOx/ATP > 1/1-CuOx/ATP > 3/1-CuOx/ATP > CuO > ATP. The CO2 desorption capacity and rate were increased by 194 % and 205 %, respectively, the relative heat duty could be reduced by about 64.5 % by using 2/1-CuOx/ATP to regenerate the rich MEA solution. ATR-FTIR technique was employed to confirm the catalytic effect and a possible catalytic CO2 desorption mechanism was suggested. Additionally, the catalyst maintained 81% of its initial CO2 desorption capacity after seven consecutive absorption-desorption cycles, demonstrating excellent recoverability. This study provides a practical strategy for utilizing efficient, affordable and environmentally benign solid acid catalysts for CO2 desorption, thereby advancing energy-efficient CO2 capture technology.
Keywords: Attapulgite; CO(2) desorption; Reaction mechanism; Relative desorption heat duty; Solid acid catalyst.
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