Improving the Carbon Capture Efficiency for Gas Power Plants through Amine-Based Absorbents
Saman Hasan,
Abubakar Jibrin Abbas and
Ghasem Ghavami Nasr
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Saman Hasan: School of Science, Engineering and Environment, University of Salford, Manchester M5 4WT, UK
Abubakar Jibrin Abbas: School of Science, Engineering and Environment, University of Salford, Manchester M5 4WT, UK
Ghasem Ghavami Nasr: School of Science, Engineering and Environment, University of Salford, Manchester M5 4WT, UK
Sustainability, 2020, vol. 13, issue 1, 1-27
Abstract:
Environmental concern for our planet has changed significantly over time due to climate change, caused by an increasing population and the subsequent demand for electricity, and thus increased power generation. Considering that natural gas is regarded as a promising fuel for such a purpose, the need to integrate carbon capture technologies in such plants is becoming a necessity, if gas power plants are to be aligned with the reduction of CO 2 in the atmosphere, through understanding the capturing efficacy of different absorbents under different operating conditions. Therefore, this study provided for the first time the comparison of available absorbents in relation to amine solvents (MEA, DEA, and DEA) CO 2 removal efficiency, cost, and recirculation rate to achieve Climate change action through caron capture without causing absorbent disintegration. The study analyzed Flue under different amine-based solvent solutions (monoethanolamine (MEA), diethanolamine (DEA), and methyldiethanolamine (MDEA)), in order to compare their potential for CO 2 reduction under different operating conditions and costs. This was simulated using ProMax 5.0 software modeled as a simple absorber tower to absorb CO 2 from flue gas. Furthermore, MEA, DEA, and MDEA adsorbents were used with a temperature of 38 °C and their concentration varied from 10 to 15%. Circulation rates of 200–300 m 3 /h were used for each concentration and solvent. The findings deduced that MEA is a promising solvent compared to DEA and MDEA in terms of the highest CO 2 captured; however, it is limited at the top outlet for clean flue gas, which contained 3.6295% of CO 2 and less than half a percent of DEA and MDEA, but this can be addressed either by increasing the concentration to 15% or increasing the MEA circulation rate to 300 m 3 /h.
Keywords: process technology description of different amine solvents; amine-based chemical solvent using monoethanolamine (MEA); degradation of MEA and other solvents; diethanolamine (DEA) solvent; methyldiethanolamine (MDEA) (search for similar items in EconPapers)
JEL-codes: O13 Q Q0 Q2 Q3 Q5 Q56 (search for similar items in EconPapers)
Date: 2020
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Citations: View citations in EconPapers (3)
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Persistent link: https://EconPapers.repec.org/RePEc:gam:jsusta:v:13:y:2020:i:1:p:72-:d:467104
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