{"title":"Advancing carbon dioxide capture: investigation into the kinetics and efficiency of absorption in molten calcium oxide–chloride†","authors":"Melissa Hall, Sean P. Rigby and George Z. Chen","doi":"10.1039/D4SU00354C","DOIUrl":null,"url":null,"abstract":"<p >One promising carbon capture technology is the absorption of carbon dioxide (CO<small><sub>2</sub></small>) by molten salt, specifically the molten mixture of calcium oxide and chloride (CaO + CaCl<small><sub>2</sub></small>, COC), as it solves some of the key issues with alternative methods, including thermal stability and capture efficiency. The kinetics of CO<small><sub>2</sub></small> absorption in a column of COC is examined by deriving a simple kinetic model and determining the kinetic constants under various conditions. The model emphasises the importance of the oxide anion (O<small><sup>2−</sup></small>) concentration and CO<small><sub>2</sub></small> partial pressure in driving the absorption rates. Applying this model to reported experimental data on CO<small><sub>2</sub></small> absorption with varying molten salt height, or CaO wt% in molten CaCl<small><sub>2</sub></small> produced values for the kinetic constants with high accuracy. The fastest rate of absorption, with a rate constant of 0.00313 L mol<small><sup>−1</sup></small> min<small><sup>−1</sup></small> was achieved at a 15 cm molten salt height. Conversely, the slowest rate, 0.00062 L mol<small><sup>−1</sup></small> min<small><sup>−1</sup></small>, occurred at 20 wt% CaO in CaCl<small><sub>2</sub></small>. Comparative analysis with conventional amine-based CO<small><sub>2</sub></small> capture systems reveals a slower absorption rate for the molten salt. Nonetheless, there are further elements which need to be explored to perform a full comparison with the amine system, for example the desorption kinetics or absorption capacity. This reinforces the need for further research into molten salt absorption kinetics to gain a more holistic understanding of this technology and enable an optimal process design for further assessment of the feasibility and scalability of molten salt-based CO<small><sub>2</sub></small> capture in current and future processes. Ultimately, this will promote the adoption of carbon capture technology, cultivating more sustainable practices in industry.</p>","PeriodicalId":74745,"journal":{"name":"RSC sustainability","volume":" 1","pages":" 341-351"},"PeriodicalIF":0.0000,"publicationDate":"2024-10-24","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"https://pubs.rsc.org/en/content/articlepdf/2025/su/d4su00354c?page=search","citationCount":"0","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"RSC sustainability","FirstCategoryId":"1085","ListUrlMain":"https://pubs.rsc.org/en/content/articlelanding/2025/su/d4su00354c","RegionNum":0,"RegionCategory":null,"ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"","JCRName":"","Score":null,"Total":0}
引用次数: 0
Abstract
One promising carbon capture technology is the absorption of carbon dioxide (CO2) by molten salt, specifically the molten mixture of calcium oxide and chloride (CaO + CaCl2, COC), as it solves some of the key issues with alternative methods, including thermal stability and capture efficiency. The kinetics of CO2 absorption in a column of COC is examined by deriving a simple kinetic model and determining the kinetic constants under various conditions. The model emphasises the importance of the oxide anion (O2−) concentration and CO2 partial pressure in driving the absorption rates. Applying this model to reported experimental data on CO2 absorption with varying molten salt height, or CaO wt% in molten CaCl2 produced values for the kinetic constants with high accuracy. The fastest rate of absorption, with a rate constant of 0.00313 L mol−1 min−1 was achieved at a 15 cm molten salt height. Conversely, the slowest rate, 0.00062 L mol−1 min−1, occurred at 20 wt% CaO in CaCl2. Comparative analysis with conventional amine-based CO2 capture systems reveals a slower absorption rate for the molten salt. Nonetheless, there are further elements which need to be explored to perform a full comparison with the amine system, for example the desorption kinetics or absorption capacity. This reinforces the need for further research into molten salt absorption kinetics to gain a more holistic understanding of this technology and enable an optimal process design for further assessment of the feasibility and scalability of molten salt-based CO2 capture in current and future processes. Ultimately, this will promote the adoption of carbon capture technology, cultivating more sustainable practices in industry.