{"title":"推进二氧化碳捕获:在熔融氧化钙-氯化钙†中吸收动力学和效率的研究","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":"{\"title\":\"Advancing carbon dioxide capture: investigation into the kinetics and efficiency of absorption in molten calcium oxide–chloride†\",\"authors\":\"Melissa Hall, Sean P. 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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. 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引用次数: 0
摘要
一种很有前途的碳捕获技术是通过熔盐吸收二氧化碳(CO2),特别是氧化钙和氯化物的熔融混合物(CaO + CaCl2, COC),因为它解决了一些替代方法的关键问题,包括热稳定性和捕获效率。通过建立一个简单的动力学模型和确定不同条件下的动力学常数,研究了COC柱中CO2的吸收动力学。该模型强调了氧化阴离子(O2−)浓度和CO2分压在驱动吸收率中的重要性。将该模型应用于已报道的不同熔盐高度或熔融CaCl2中CaO wt%的CO2吸收实验数据,得到了高精度的动力学常数值。熔盐高度为15 cm时,吸收速率最快,速率常数为0.00313 L mol−1 min−1。相反,在CaCl2中,当CaO浓度为20%时,反应速率最低,为0.00062 L mol−1 min−1。与传统的胺基CO2捕获系统的比较分析表明,熔盐的吸收率较慢。尽管如此,要与胺系进行全面比较,还需要进一步探索一些因素,例如解吸动力学或吸收能力。这加强了对熔盐吸收动力学的进一步研究的必要性,以获得对该技术的更全面的理解,并为进一步评估当前和未来工艺中熔盐基CO2捕获的可行性和可扩展性提供最佳工艺设计。最终,这将促进碳捕获技术的采用,在工业中培养更可持续的做法。
Advancing carbon dioxide capture: investigation into the kinetics and efficiency of absorption in molten calcium oxide–chloride†
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.