Song Zhou, Graeme Puxty, William Conway, Liang Li, Fanghua Li, Paul Feron, Hai Yu
{"title":"替代综合捕集-矿化(AICM)用于低反应性富镁废物的低能碳化","authors":"Song Zhou, Graeme Puxty, William Conway, Liang Li, Fanghua Li, Paul Feron, Hai Yu","doi":"10.1016/j.cej.2025.159236","DOIUrl":null,"url":null,"abstract":"Efficient carbon capture and utilization are vital for a low-carbon economy. Unlike traditional CO<sub>2</sub> capture methods that are energy-intensive or amine-based mineralization methods that are limited to calcium-rich wastes, this study presents an aqueous amine-based integrated CO<sub>2</sub> capture and mineralization process (AICM). AICM enables simultaneous CO<sub>2</sub> capture and stable fixation using low-reactivity, magnesium-rich feedstocks, which typically need high temperatures and pressures. A notable advantage of AICM is its ability to regenerate the absorbent by simply adding lime kiln dust (LKD), an abundant waste of lime production. Optimal conditions for CO<sub>2</sub> carbonation with magnesium were achieved with a 4.0 M monoethanolamine (MEA) solution at 60 °C, reaching an 87 % carbonation efficiency. Interestingly, the formation of magnesium carbonate was observed under weakly alkaline conditions, even at pH conditions below 8 where the concentration of free carbonate ions (CO<sub>3</sub><sup>2−</sup>) is negligible. This phenomenon can be attributed to the availability of carbamate, which was potentially reacting with magnesium ions (Mg<sup>2+</sup>) to form magnesium carbonate, thereby facilitating CO<sub>2</sub> desorption in the solution. The carbamate-rich environment was more pronounced at higher MEA concentrations and temperatures investigated here. Following CO<sub>2</sub> desorption, the reactivity of spent MEA solutions has diminished due to consumption of free reactive amine groups by protons released during carbonation. However, LKD can restore these groups by neutralizing protons, allowing regenerated MEA to regain near-full reactivity and CO<sub>2</sub> capture capacity comparable to fresh MEA. Producing valuable magnesium carbonate further enhances the process’s economic viability. This study provides valuable insight into new methods to improve traditional thermal regeneration CO<sub>2</sub> capture processes and to reduce the consumption of alkalis compared to conventional pH-swing mineralisation processes, which require significant amounts of strong non-regenerable bases.","PeriodicalId":270,"journal":{"name":"Chemical Engineering Journal","volume":"20 1","pages":""},"PeriodicalIF":13.2000,"publicationDate":"2025-01-03","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":"{\"title\":\"Alternative integrated capture − Mineralisation (AICM) for low-energy carbonation of low-reactivity magnesium-rich wastes\",\"authors\":\"Song Zhou, Graeme Puxty, William Conway, Liang Li, Fanghua Li, Paul Feron, Hai Yu\",\"doi\":\"10.1016/j.cej.2025.159236\",\"DOIUrl\":null,\"url\":null,\"abstract\":\"Efficient carbon capture and utilization are vital for a low-carbon economy. Unlike traditional CO<sub>2</sub> capture methods that are energy-intensive or amine-based mineralization methods that are limited to calcium-rich wastes, this study presents an aqueous amine-based integrated CO<sub>2</sub> capture and mineralization process (AICM). AICM enables simultaneous CO<sub>2</sub> capture and stable fixation using low-reactivity, magnesium-rich feedstocks, which typically need high temperatures and pressures. A notable advantage of AICM is its ability to regenerate the absorbent by simply adding lime kiln dust (LKD), an abundant waste of lime production. Optimal conditions for CO<sub>2</sub> carbonation with magnesium were achieved with a 4.0 M monoethanolamine (MEA) solution at 60 °C, reaching an 87 % carbonation efficiency. Interestingly, the formation of magnesium carbonate was observed under weakly alkaline conditions, even at pH conditions below 8 where the concentration of free carbonate ions (CO<sub>3</sub><sup>2−</sup>) is negligible. This phenomenon can be attributed to the availability of carbamate, which was potentially reacting with magnesium ions (Mg<sup>2+</sup>) to form magnesium carbonate, thereby facilitating CO<sub>2</sub> desorption in the solution. The carbamate-rich environment was more pronounced at higher MEA concentrations and temperatures investigated here. Following CO<sub>2</sub> desorption, the reactivity of spent MEA solutions has diminished due to consumption of free reactive amine groups by protons released during carbonation. However, LKD can restore these groups by neutralizing protons, allowing regenerated MEA to regain near-full reactivity and CO<sub>2</sub> capture capacity comparable to fresh MEA. Producing valuable magnesium carbonate further enhances the process’s economic viability. 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Alternative integrated capture − Mineralisation (AICM) for low-energy carbonation of low-reactivity magnesium-rich wastes
Efficient carbon capture and utilization are vital for a low-carbon economy. Unlike traditional CO2 capture methods that are energy-intensive or amine-based mineralization methods that are limited to calcium-rich wastes, this study presents an aqueous amine-based integrated CO2 capture and mineralization process (AICM). AICM enables simultaneous CO2 capture and stable fixation using low-reactivity, magnesium-rich feedstocks, which typically need high temperatures and pressures. A notable advantage of AICM is its ability to regenerate the absorbent by simply adding lime kiln dust (LKD), an abundant waste of lime production. Optimal conditions for CO2 carbonation with magnesium were achieved with a 4.0 M monoethanolamine (MEA) solution at 60 °C, reaching an 87 % carbonation efficiency. Interestingly, the formation of magnesium carbonate was observed under weakly alkaline conditions, even at pH conditions below 8 where the concentration of free carbonate ions (CO32−) is negligible. This phenomenon can be attributed to the availability of carbamate, which was potentially reacting with magnesium ions (Mg2+) to form magnesium carbonate, thereby facilitating CO2 desorption in the solution. The carbamate-rich environment was more pronounced at higher MEA concentrations and temperatures investigated here. Following CO2 desorption, the reactivity of spent MEA solutions has diminished due to consumption of free reactive amine groups by protons released during carbonation. However, LKD can restore these groups by neutralizing protons, allowing regenerated MEA to regain near-full reactivity and CO2 capture capacity comparable to fresh MEA. Producing valuable magnesium carbonate further enhances the process’s economic viability. This study provides valuable insight into new methods to improve traditional thermal regeneration CO2 capture processes and to reduce the consumption of alkalis compared to conventional pH-swing mineralisation processes, which require significant amounts of strong non-regenerable bases.
期刊介绍:
The Chemical Engineering Journal is an international research journal that invites contributions of original and novel fundamental research. It aims to provide an international platform for presenting original fundamental research, interpretative reviews, and discussions on new developments in chemical engineering. The journal welcomes papers that describe novel theory and its practical application, as well as those that demonstrate the transfer of techniques from other disciplines. It also welcomes reports on carefully conducted experimental work that is soundly interpreted. The main focus of the journal is on original and rigorous research results that have broad significance. The Catalysis section within the Chemical Engineering Journal focuses specifically on Experimental and Theoretical studies in the fields of heterogeneous catalysis, molecular catalysis, and biocatalysis. These studies have industrial impact on various sectors such as chemicals, energy, materials, foods, healthcare, and environmental protection.