2016
DOI: 10.1016/j.jclepro.2015.12.056
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Optimal design and sensitivity analysis of post-combustion CO 2 capture process by chemical absorption with amines

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Cited by 32 publications
(5 citation statements)
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“…CO2 needs to be removed from flue gas streams from power plants and industries due to its high contribution to global warming. There are different technologies to address this important issue (Arias et al, 2016). Among these technologies, chemical absorption using solvents is a promising method and many studies have been performed so far (Borhani et al, 2015).…”
Section: Introductionmentioning
confidence: 99%
“…CO2 needs to be removed from flue gas streams from power plants and industries due to its high contribution to global warming. There are different technologies to address this important issue (Arias et al, 2016). Among these technologies, chemical absorption using solvents is a promising method and many studies have been performed so far (Borhani et al, 2015).…”
Section: Introductionmentioning
confidence: 99%
“…The capital recovery factor (CRF) is calculated using Eq. (70) assuming an interest rate (i) of 8 % and a project lifespan (n) of 25 years [83,143]:…”
Section: Mathematical Optimization Modelmentioning
confidence: 99%
“…Different strategies have been considered and adopted by several countries aiming to reduce the CO 2 emissions, such as the improvement of energy efficiency, increasing the use of low carbon fuels or nuclear energy, renewable energy development, geo-engineering approaches and CO 2 capture and storage (CCS) (Garcés et al, 2013;Leung et al, 2014). Among these different strategies, CCS is considered crucial because it reduces the CO 2 emission from large emission sources (Arias et al, 2016;Garđarsdóttir et al, 2015;Kamarudin and Alias, 2013;Leung et al, 2014).…”
Section: Introductionmentioning
confidence: 99%
“…Chemical absorption using amine aqueous solutions is a benchmark technology for CO 2 capture (Arias et al, 2016;Bachelor and Toochinda, 2012;Kamarudin and Alias, 2013). However, it has some operational drawbacks, such as high power consumption required for solvent regeneration, equipment corrosion (Gray et al, 2005;Kamarudin and Alias, 2013), degradation/ evaporation of amines, the need of a large-volume absorber , besides additional operating costs due to substitution of solvents (Seo et al, 2014).…”
Section: Introductionmentioning
confidence: 99%