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Experimental evaluation of electrochemically mediated amine regeneration integrated with amine thermal swing for CO2 capture at optimized desorption temperatures.
- Source :
- Journal of CO2 Utilization; Sep2024, Vol. 87, pN.PAG-N.PAG, 1p
- Publication Year :
- 2024
-
Abstract
- In the present study, the integration of electrochemically mediated amine regeneration (EMAR) with amine thermal swing process is investigated as a novel method for CO 2 capture, utilizing experimental practical data. The aim is to increase the absorption-desorption temperature difference in order to improve the energy efficiency of the capture process and hamper the amine degradation issue at high desorption temperatures. A comprehensive experimental procedure is presented, and an experimental process setup is designed and constructed. As the main novelty of the study a special heating-cooling subsystem is incorporated with the base EMAR process in order to devise a combined electrochemical-thermal system. The performance of the system is evaluated at sequential incremental desorption temperatures while the absorption temperature is kept constant. Relevant data, including the desorbed CO 2 flow, absorbed CO 2 flow, stream points temperature, and cell voltage are collected. Based on the data collected, two performance parameters are calculated, including normalized carbon separation work, and CO 2 desorption density. Based on these performance parameters the system's capability is assessed, and the optimal desorption temperature is ultimately selected. The presented electrochemical-thermal CO 2 separation system, operating with a chloride salt system, demonstrates its best energetics performance at a desorption temperature of 44 °C, resulting in a normalized capture work of 95.2 kJ/molCO 2. Under these optimal conditions, the cell's average voltage is measured to be 0.37 V, and the CO 2 desorption density is determined to be 0.71 l.min<superscript>−1</superscript>.m<superscript>−2</superscript>. • Novel integration of EMAR and thermal swing for energy-efficient CO 2 capture is proposed. • Unique heating-cooling subsystem enhances the electrochemical-thermal system. • Performance evaluated by calculating capture work and CO 2 desorption density. • Optimal desorption at 44°C, achieving work of 95.2 kJ/molCO 2 with 0.37 V voltage. [ABSTRACT FROM AUTHOR]
Details
- Language :
- English
- ISSN :
- 22129820
- Volume :
- 87
- Database :
- Supplemental Index
- Journal :
- Journal of CO2 Utilization
- Publication Type :
- Academic Journal
- Accession number :
- 179601118
- Full Text :
- https://doi.org/10.1016/j.jcou.2024.102922