Sulfur dioxide removal: an overview of regenerative flue gas desulfurization and factors affecting desulfurization capacity and sorbent regeneration

Numerous mitigation techniques have been incorporated to capture or remove SO2 with flue gas desulfurization (FGD) being the most common method. Regenerative FGD method is advantageous over other methods due to high desulfurization efficiency, sorbent regenerability, and reduction in waste handling....

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Main Authors: Hanif, M. A., Ibrahim, N., Abdul Jalil, L.
Format: Article
Published: Springer 2020
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Online Access:http://eprints.utm.my/id/eprint/87558/
http://www.dx.doi.org/10.1007/s11356-020-09191-4
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Institution: Universiti Teknologi Malaysia
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spelling my.utm.875582020-11-30T09:03:48Z http://eprints.utm.my/id/eprint/87558/ Sulfur dioxide removal: an overview of regenerative flue gas desulfurization and factors affecting desulfurization capacity and sorbent regeneration Hanif, M. A. Ibrahim, N. Abdul Jalil, L. TP Chemical technology Numerous mitigation techniques have been incorporated to capture or remove SO2 with flue gas desulfurization (FGD) being the most common method. Regenerative FGD method is advantageous over other methods due to high desulfurization efficiency, sorbent regenerability, and reduction in waste handling. The capital costs of regenerative methods are higher than those of commonly used once-through methods simply due to the inclusion of sorbent regeneration while operational and management costs depend on the operating hours and fuel composition. Regenerable sorbents like ionic liquids, deep eutectic solvents, ammonium halide solutions, alkyl-aniline solutions, amino acid solutions, activated carbons, mesoporous silica, zeolite, and metal-organic frameworks have been reported to successfully achieve high SO2 removal. The presence of other gases in flue gas, e.g., O2, CO2, NOx, and water vapor, and the reaction temperature critically affect the sorption capacity and sorbent regenerability. To obtain optimal SO2 removal performance, other parameters such as pH, inlet SO2 concentration, and additives need to be adequately governed. Due to its high removal capacity, easy preparation, non-toxicity, and low regeneration temperature, the use of deep eutectic solvents is highly feasible for upscale utilization. Metal-organic frameworks demonstrated highest reported SO2 removal capacity; however, it is not yet applicable at industrial level due to its high price, weak stability, and robust formulation. Springer 2020-08 Article PeerReviewed Hanif, M. A. and Ibrahim, N. and Abdul Jalil, L. (2020) Sulfur dioxide removal: an overview of regenerative flue gas desulfurization and factors affecting desulfurization capacity and sorbent regeneration. Environmental Science and Pollution Research, 27 (22). pp. 27515-27540. ISSN 0944-1344 http://www.dx.doi.org/10.1007/s11356-020-09191-4 DOI: 10.1007/s11356-020-09191-4
institution Universiti Teknologi Malaysia
building UTM Library
collection Institutional Repository
continent Asia
country Malaysia
content_provider Universiti Teknologi Malaysia
content_source UTM Institutional Repository
url_provider http://eprints.utm.my/
topic TP Chemical technology
spellingShingle TP Chemical technology
Hanif, M. A.
Ibrahim, N.
Abdul Jalil, L.
Sulfur dioxide removal: an overview of regenerative flue gas desulfurization and factors affecting desulfurization capacity and sorbent regeneration
description Numerous mitigation techniques have been incorporated to capture or remove SO2 with flue gas desulfurization (FGD) being the most common method. Regenerative FGD method is advantageous over other methods due to high desulfurization efficiency, sorbent regenerability, and reduction in waste handling. The capital costs of regenerative methods are higher than those of commonly used once-through methods simply due to the inclusion of sorbent regeneration while operational and management costs depend on the operating hours and fuel composition. Regenerable sorbents like ionic liquids, deep eutectic solvents, ammonium halide solutions, alkyl-aniline solutions, amino acid solutions, activated carbons, mesoporous silica, zeolite, and metal-organic frameworks have been reported to successfully achieve high SO2 removal. The presence of other gases in flue gas, e.g., O2, CO2, NOx, and water vapor, and the reaction temperature critically affect the sorption capacity and sorbent regenerability. To obtain optimal SO2 removal performance, other parameters such as pH, inlet SO2 concentration, and additives need to be adequately governed. Due to its high removal capacity, easy preparation, non-toxicity, and low regeneration temperature, the use of deep eutectic solvents is highly feasible for upscale utilization. Metal-organic frameworks demonstrated highest reported SO2 removal capacity; however, it is not yet applicable at industrial level due to its high price, weak stability, and robust formulation.
format Article
author Hanif, M. A.
Ibrahim, N.
Abdul Jalil, L.
author_facet Hanif, M. A.
Ibrahim, N.
Abdul Jalil, L.
author_sort Hanif, M. A.
title Sulfur dioxide removal: an overview of regenerative flue gas desulfurization and factors affecting desulfurization capacity and sorbent regeneration
title_short Sulfur dioxide removal: an overview of regenerative flue gas desulfurization and factors affecting desulfurization capacity and sorbent regeneration
title_full Sulfur dioxide removal: an overview of regenerative flue gas desulfurization and factors affecting desulfurization capacity and sorbent regeneration
title_fullStr Sulfur dioxide removal: an overview of regenerative flue gas desulfurization and factors affecting desulfurization capacity and sorbent regeneration
title_full_unstemmed Sulfur dioxide removal: an overview of regenerative flue gas desulfurization and factors affecting desulfurization capacity and sorbent regeneration
title_sort sulfur dioxide removal: an overview of regenerative flue gas desulfurization and factors affecting desulfurization capacity and sorbent regeneration
publisher Springer
publishDate 2020
url http://eprints.utm.my/id/eprint/87558/
http://www.dx.doi.org/10.1007/s11356-020-09191-4
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