Carbon dioxide capture through reaction with potassium hydroxide and reject brine: A kinetics study
<p dir="ltr">The aim of this research is to investigate the reaction kinetics for a modified Solvay process based on KOH. The global reaction rate was measured within 3−15% CO<sub>2</sub> inlet concentration, 10−50 °C reaction temperature, 30–190 g/L KOH concentration, 40...
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| مؤلفون آخرون: | , , , , |
| منشور في: |
2022
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| _version_ | 1864513538559574016 |
|---|---|
| author | Aya A-H. Mourad (17380423) |
| author2 | Ameera F. Mohammad (14778271) Ali H. Al-Marzouqi (13047092) Mohammednoor Altarawneh (1414522) Mohamed H. Al-Marzouqi (17151088) Muftah H. El-Naas (2662543) |
| author2_role | author author author author author |
| author_facet | Aya A-H. Mourad (17380423) Ameera F. Mohammad (14778271) Ali H. Al-Marzouqi (13047092) Mohammednoor Altarawneh (1414522) Mohamed H. Al-Marzouqi (17151088) Muftah H. El-Naas (2662543) |
| author_role | author |
| dc.creator.none.fl_str_mv | Aya A-H. Mourad (17380423) Ameera F. Mohammad (14778271) Ali H. Al-Marzouqi (13047092) Mohammednoor Altarawneh (1414522) Mohamed H. Al-Marzouqi (17151088) Muftah H. El-Naas (2662543) |
| dc.date.none.fl_str_mv | 2022-10-01T00:00:00Z |
| dc.identifier.none.fl_str_mv | 10.1016/j.ijggc.2022.103768 |
| dc.relation.none.fl_str_mv | https://figshare.com/articles/journal_contribution/Carbon_dioxide_capture_through_reaction_with_potassium_hydroxide_and_reject_brine_A_kinetics_study/24551434 |
| dc.rights.none.fl_str_mv | CC BY 4.0 info:eu-repo/semantics/openAccess |
| dc.subject.none.fl_str_mv | Engineering Chemical engineering Reject brine Desalination Carbon dioxide Reaction rate Kinetics Modified Solvay process Potassium hydroxide |
| dc.title.none.fl_str_mv | Carbon dioxide capture through reaction with potassium hydroxide and reject brine: A kinetics study |
| dc.type.none.fl_str_mv | Text Journal contribution info:eu-repo/semantics/publishedVersion text contribution to journal |
| description | <p dir="ltr">The aim of this research is to investigate the reaction kinetics for a modified Solvay process based on KOH. The global reaction rate was measured within 3−15% CO<sub>2</sub> inlet concentration, 10−50 °C reaction temperature, 30–190 g/L KOH concentration, 400–2000 mL/min CO<sub>2</sub> gas flow rate, and 1–5 bar total applied pressure range, changing one factor at a time while keeping the values of the remaining parameters fixed. As part of each set of experimental runs, temporal changes in ion reduction and pH value were also monitored. The results revealed that the reaction rate is directly proportional to the increase in the inlet CO<sub>2</sub> concentration. This finding was supported by CO<sub>2</sub> uptake, whereby the maximum value of almost 0.69 g CO<sub>2</sub>/g KOH was achieved at the highest CO<sub>2</sub> inlet concentration of 15%. However, the selected range of reaction temperature and KOH concentration exerted no influence on the overall CO<sub>2</sub> absorption rate, which remained nearly constant within the selected ranges for these parameters. Under the chosen operating conditions, a first-order overall reaction rate with respect to CO<sub>2</sub> concentration was established, whereby the reaction rate constant (k) was∼ 0.0003 mol/(L·min).</p><h2>Other Information</h2><p dir="ltr">Published in: International Journal of Greenhouse Gas Control<br>License: <a href="http://creativecommons.org/licenses/by/4.0/" target="_blank">http://creativecommons.org/licenses/by/4.0/</a><br>See article on publisher's website: <a href="https://dx.doi.org/10.1016/j.ijggc.2022.103768" target="_blank">https://dx.doi.org/10.1016/j.ijggc.2022.103768</a></p> |
| eu_rights_str_mv | openAccess |
| id | Manara2_ee9dd8db242abc15bb28b643df2191cc |
| identifier_str_mv | 10.1016/j.ijggc.2022.103768 |
| network_acronym_str | Manara2 |
| network_name_str | Manara2 |
| oai_identifier_str | oai:figshare.com:article/24551434 |
| publishDate | 2022 |
| repository.mail.fl_str_mv | |
| repository.name.fl_str_mv | |
| repository_id_str | |
| rights_invalid_str_mv | CC BY 4.0 |
| spelling | Carbon dioxide capture through reaction with potassium hydroxide and reject brine: A kinetics studyAya A-H. Mourad (17380423)Ameera F. Mohammad (14778271)Ali H. Al-Marzouqi (13047092)Mohammednoor Altarawneh (1414522)Mohamed H. Al-Marzouqi (17151088)Muftah H. El-Naas (2662543)EngineeringChemical engineeringReject brineDesalinationCarbon dioxideReaction rateKineticsModified Solvay processPotassium hydroxide<p dir="ltr">The aim of this research is to investigate the reaction kinetics for a modified Solvay process based on KOH. The global reaction rate was measured within 3−15% CO<sub>2</sub> inlet concentration, 10−50 °C reaction temperature, 30–190 g/L KOH concentration, 400–2000 mL/min CO<sub>2</sub> gas flow rate, and 1–5 bar total applied pressure range, changing one factor at a time while keeping the values of the remaining parameters fixed. As part of each set of experimental runs, temporal changes in ion reduction and pH value were also monitored. The results revealed that the reaction rate is directly proportional to the increase in the inlet CO<sub>2</sub> concentration. This finding was supported by CO<sub>2</sub> uptake, whereby the maximum value of almost 0.69 g CO<sub>2</sub>/g KOH was achieved at the highest CO<sub>2</sub> inlet concentration of 15%. However, the selected range of reaction temperature and KOH concentration exerted no influence on the overall CO<sub>2</sub> absorption rate, which remained nearly constant within the selected ranges for these parameters. Under the chosen operating conditions, a first-order overall reaction rate with respect to CO<sub>2</sub> concentration was established, whereby the reaction rate constant (k) was∼ 0.0003 mol/(L·min).</p><h2>Other Information</h2><p dir="ltr">Published in: International Journal of Greenhouse Gas Control<br>License: <a href="http://creativecommons.org/licenses/by/4.0/" target="_blank">http://creativecommons.org/licenses/by/4.0/</a><br>See article on publisher's website: <a href="https://dx.doi.org/10.1016/j.ijggc.2022.103768" target="_blank">https://dx.doi.org/10.1016/j.ijggc.2022.103768</a></p>2022-10-01T00:00:00ZTextJournal contributioninfo:eu-repo/semantics/publishedVersiontextcontribution to journal10.1016/j.ijggc.2022.103768https://figshare.com/articles/journal_contribution/Carbon_dioxide_capture_through_reaction_with_potassium_hydroxide_and_reject_brine_A_kinetics_study/24551434CC BY 4.0info:eu-repo/semantics/openAccessoai:figshare.com:article/245514342022-10-01T00:00:00Z |
| spellingShingle | Carbon dioxide capture through reaction with potassium hydroxide and reject brine: A kinetics study Aya A-H. Mourad (17380423) Engineering Chemical engineering Reject brine Desalination Carbon dioxide Reaction rate Kinetics Modified Solvay process Potassium hydroxide |
| status_str | publishedVersion |
| title | Carbon dioxide capture through reaction with potassium hydroxide and reject brine: A kinetics study |
| title_full | Carbon dioxide capture through reaction with potassium hydroxide and reject brine: A kinetics study |
| title_fullStr | Carbon dioxide capture through reaction with potassium hydroxide and reject brine: A kinetics study |
| title_full_unstemmed | Carbon dioxide capture through reaction with potassium hydroxide and reject brine: A kinetics study |
| title_short | Carbon dioxide capture through reaction with potassium hydroxide and reject brine: A kinetics study |
| title_sort | Carbon dioxide capture through reaction with potassium hydroxide and reject brine: A kinetics study |
| topic | Engineering Chemical engineering Reject brine Desalination Carbon dioxide Reaction rate Kinetics Modified Solvay process Potassium hydroxide |