Pub Date : 2025-08-28DOI: 10.1016/j.ccst.2025.100500
Hyeonji Yeom, Yongseok Kim, Woosung Leem, Jongmin Park, Kyungsu Na
The direct hydrogenation of CO2 using green hydrogen offers a sustainable route to produce carbon-neutral liquid hydrocarbons, emerging as a viable alternative to conventional naphtha cracking. Although Fe-based CuAl2O4 catalysts have been widely studied for CO2 hydrogenation, the mechanistic role of hydrogen spillover across dynamic Cu–Fe and associated oxygen vacancies has remained elusive. Here, the structure of FeK/CuAl2O4 catalysts was systematically tailored by controlling the reduction temperature to elucidate the exsolution-driven restructuration of pristine catalyst structure and its influences on the catalytic performance. We investigated the reaction process using in-situ DRIFTS analysis, from which we for the first time observed a cascade mechanism activated by hydrogen spillover, revealing various elementary reaction steps: (i) preferential adsorption of CO2 as carbonate species on oxygen vacancies created by Cu exsolution in CuAl2O4 lattice, (ii) effective formate-mediated reverse water–gas shift (RWGS) reaction via the hydrogen spillover from exsolved Cu, (iii) promoted Fischer–Tropsch synthesis (FTS) reaction on Fe5C2 formed by the facilitated Fe carburization at the exsolved Cu–Fe3O4 interfaces, (iv) rapid desorption of hydrocarbons produced via controlled carbon chain growth. This cooperative interaction enabled the selective production of C5–11 hydrocarbons, achieving the highest C5–11 productivity of 290.7 mL gcat–1 h–1, surpassing our previous work at a CO2 conversion of 36.4%. These findings establish a quantitative structure–performance–mechanism relationship and offer design principles for selectivity control toward desired hydrocarbon ranges in multifunctional CO2 hydrogenation catalysts.
使用绿色氢直接加氢二氧化碳为生产碳中性液态烃提供了一条可持续的途径,成为传统石脑油裂解的可行替代方案。虽然铁基CuAl2O4催化剂在CO2加氢中的应用已经得到了广泛的研究,但氢在Cu-Fe和伴生氧空位上的溢出机制仍然是一个谜。本研究通过控制还原温度,对FeK/CuAl2O4催化剂的结构进行了系统定制,以阐明析出驱动的原始催化剂结构重构及其对催化性能的影响。利用原位DRIFTS分析对反应过程进行了研究,首次观察到氢溢出激活的级联机制,揭示了不同的基本反应步骤:(1) Cu在CuAl2O4晶格中析出形成氧空位,CO2作为碳酸盐优先吸附;(2)通过析出Cu产生的氢溢出,甲酸介导的有效逆水气转换(RWGS)反应;(3)在析出Cu - fe3o4界面上促进Fe渗碳形成Fe5C2,促进了费托合成(FTS)反应;(4)通过控制碳链生长产生的碳氢化合物快速解吸。这种协同作用使C5-11碳氢化合物的选择性生产成为可能,达到了最高的C5-11产能290.7 mL gcat-1 h-1,超过了我们之前工作的36.4%的二氧化碳转化率。这些发现建立了定量的结构-性能-机理关系,并为多功能CO2加氢催化剂的选择性控制提供了设计原则。
{"title":"Mechanistic elucidation of cascade CO2 hydrogenation enabled by Cu–Fe interfaces and oxygen vacancies","authors":"Hyeonji Yeom, Yongseok Kim, Woosung Leem, Jongmin Park, Kyungsu Na","doi":"10.1016/j.ccst.2025.100500","DOIUrl":"10.1016/j.ccst.2025.100500","url":null,"abstract":"<div><div>The direct hydrogenation of CO<sub>2</sub> using green hydrogen offers a sustainable route to produce carbon-neutral liquid hydrocarbons, emerging as a viable alternative to conventional naphtha cracking. Although Fe-based CuAl<sub>2</sub>O<sub>4</sub> catalysts have been widely studied for CO<sub>2</sub> hydrogenation, the mechanistic role of hydrogen spillover across dynamic Cu–Fe and associated oxygen vacancies has remained elusive. Here, the structure of FeK/CuAl<sub>2</sub>O<sub>4</sub> catalysts was systematically tailored by controlling the reduction temperature to elucidate the exsolution-driven restructuration of pristine catalyst structure and its influences on the catalytic performance. We investigated the reaction process using in-situ DRIFTS analysis, from which we for the first time observed a cascade mechanism activated by hydrogen spillover, revealing various elementary reaction steps: (i) preferential adsorption of CO<sub>2</sub> as carbonate species on oxygen vacancies created by Cu exsolution in CuAl<sub>2</sub>O<sub>4</sub> lattice, (ii) effective formate-mediated reverse water–gas shift (RWGS) reaction via the hydrogen spillover from exsolved Cu, (iii) promoted Fischer–Tropsch synthesis (FTS) reaction on Fe<sub>5</sub>C<sub>2</sub> formed by the facilitated Fe carburization at the exsolved Cu–Fe<sub>3</sub>O<sub>4</sub> interfaces, (iv) rapid desorption of hydrocarbons produced via controlled carbon chain growth. This cooperative interaction enabled the selective production of C<sub>5–11</sub> hydrocarbons, achieving the highest C<sub>5–11</sub> productivity of 290.7 mL g<sub>cat</sub><sup>–1</sup> h<sup>–1</sup>, surpassing our previous work at a CO<sub>2</sub> conversion of 36.4%. These findings establish a quantitative structure–performance–mechanism relationship and offer design principles for selectivity control toward desired hydrocarbon ranges in multifunctional CO<sub>2</sub> hydrogenation catalysts.</div></div>","PeriodicalId":9387,"journal":{"name":"Carbon Capture Science & Technology","volume":"17 ","pages":"Article 100500"},"PeriodicalIF":0.0,"publicationDate":"2025-08-28","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"144933166","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":0,"RegionCategory":"","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Pub Date : 2025-08-27DOI: 10.1016/j.ccst.2025.100499
S. Mhlambi , O.E. Eruteya , F.A. Agbor , A. Moscariello , J.M. van Bever Donker , E. Samankassou
As global efforts to mitigate greenhouse gas emissions intensify, carbon capture and storage (CCS) has emerged as a key strategy for reducing the environmental impact of fossil fuel use. However, geological storage of CO₂ in structurally complex and heterogeneous reservoirs presents a range of issues due to the geological intricacies, with implications for storage capacity estimation, CO₂ injection, migration, and even long-term containment, which pose environmental risks. Therefore, this study assesses the CO₂ storage potential of the depleted F-O Gas Field in the Bredasdorp Basin, offshore South Africa, using a robust modelling approach based on the analysis of a suite of exploration and production datasets from the field. A high degree of structural compartmentalisation with a fault-bounded anticlinal trap characterises the field. The Valanginian-age marine sandstone reservoirs exhibit low to moderate porosity and permeability. In total, a CO₂ storage capacity of 185.3 Mt was determined for the F-O gas field, which reduces to 37.1–74.1 Mt after accounting for reservoir heterogeneity and sweep efficiency. This reduction reflects the impact of the field's complex structural architecture, variable facies distribution, and petrophysical variability, which collectively limit the effective pore volume accessible for CO2 storage. By rigorously integrating the structural architecture of the field, sedimentary processes, facies distribution, and petrophysical variability of the candidate reservoir, this study provides critical insights and strategies into the feasibility of CCS in structurally complex depleted gas fields. Significantly, these findings contribute to ongoing national CCS assessments and support South Africa’s long-term decarbonisation agenda.
{"title":"Assessing CO2 storage potential in a structurally complex depleted gas reservoir, offshore South Africa","authors":"S. Mhlambi , O.E. Eruteya , F.A. Agbor , A. Moscariello , J.M. van Bever Donker , E. Samankassou","doi":"10.1016/j.ccst.2025.100499","DOIUrl":"10.1016/j.ccst.2025.100499","url":null,"abstract":"<div><div>As global efforts to mitigate greenhouse gas emissions intensify, carbon capture and storage (CCS) has emerged as a key strategy for reducing the environmental impact of fossil fuel use. However, geological storage of CO₂ in structurally complex and heterogeneous reservoirs presents a range of issues due to the geological intricacies, with implications for storage capacity estimation, CO₂ injection, migration, and even long-term containment, which pose environmental risks. Therefore, this study assesses the CO₂ storage potential of the depleted F-O Gas Field in the Bredasdorp Basin, offshore South Africa, using a robust modelling approach based on the analysis of a suite of exploration and production datasets from the field. A high degree of structural compartmentalisation with a fault-bounded anticlinal trap characterises the field. The Valanginian-age marine sandstone reservoirs exhibit low to moderate porosity and permeability. In total, a CO₂ storage capacity of 185.3 Mt was determined for the F-O gas field, which reduces to 37.1–74.1 Mt after accounting for reservoir heterogeneity and sweep efficiency. This reduction reflects the impact of the field's complex structural architecture, variable facies distribution, and petrophysical variability, which collectively limit the effective pore volume accessible for CO<sub>2</sub> storage. By rigorously integrating the structural architecture of the field, sedimentary processes, facies distribution, and petrophysical variability of the candidate reservoir, this study provides critical insights and strategies into the feasibility of CCS in structurally complex depleted gas fields. Significantly, these findings contribute to ongoing national CCS assessments and support South Africa’s long-term decarbonisation agenda.</div></div>","PeriodicalId":9387,"journal":{"name":"Carbon Capture Science & Technology","volume":"17 ","pages":"Article 100499"},"PeriodicalIF":0.0,"publicationDate":"2025-08-27","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"145096338","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":0,"RegionCategory":"","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Pub Date : 2025-08-26DOI: 10.1016/j.ccst.2025.100495
Jianqiao Zhang , Liang Zhao , Li Jin , Chen Zhu , Haiou Wang , Lijuan Wang
Rapid mitigation of global climate change demands transformative technological innovations to achieve deep decarbonization. China has pledged the dual carbon goals of peaking carbon emissions by 2030 and achieving carbon neutrality by 2060, underscoring the urgency and scale of the challenge. While Carbon Capture, Utilization, and Storage (CCUS) has emerged as a promising approach, its large-scale implementation in emission-intensive industrial clustered region faces significant infrastructural challenges. Specifically, the optimal layout of regional CCUS clusterization and CO2 transport networks remains unclear, particularly in highly industrialized regions such as China’s Jiangsu Province, where diverse industrial sectors and varied geological formations create complex source-sink matching challenges for CCUS deployment. In this study, we developed the SPATIAL (Strategic Pipeline And Technical Integration Analysis Layout) model that enables the optimization of CCUS deployment in emission-intensive regions from an industrial cluster perspective by integrating data of emissions from major industrial sources and storage potential from geological formations. The model was applied to Jiangsu Province under high, medium, and low emission reduction target scenarios through source-sink matching. Results show significant spatial heterogeneity between emission sources and geological storage resources in Jiangsu Province. For example, southern Jiangsu, characterized by high-intensity CO2 emission clusters, accounts for 63 % of the province’s total emissions while holding only 0.03 % of the province’s geological storage potential. The optimal layout for regional CCUS clusterization deployment under high, medium, and low emission reduction targets achieve total CO2 storage of 1.4, 1.1, and 0.9 Gt, respectively, supported by pipeline networks of 4629, 2513, and 1433 km. These layouts demonstrate economies of scale, with unit emission reduction costs ranging from 93.84 to 179.31 CNY/t CO2. Our findings establish the technical and economic feasibility of achieving significant emission reductions through regional CCUS clusterization deployment and address a critical gap in ignoring the hot spot phenomenon of industrial cluster. This study further emphasizes the importance of inter-regional coordination, regional geological storage resource management, and integrated infrastructure planning in realizing cost-effective CCUS clusterization implementation. This study provides policymakers with actionable insights for formulating CCUS clusterization strategies in emission-intensive industrial regions, contributing to the broader goal of regional carbon neutrality.
{"title":"Optimizing regional CCUS clusterization deployment for multi-industrial sectors: A carbon neutrality pathway for emission-intensive region","authors":"Jianqiao Zhang , Liang Zhao , Li Jin , Chen Zhu , Haiou Wang , Lijuan Wang","doi":"10.1016/j.ccst.2025.100495","DOIUrl":"10.1016/j.ccst.2025.100495","url":null,"abstract":"<div><div>Rapid mitigation of global climate change demands transformative technological innovations to achieve deep decarbonization. China has pledged the dual carbon goals of peaking carbon emissions by 2030 and achieving carbon neutrality by 2060, underscoring the urgency and scale of the challenge. While Carbon Capture, Utilization, and Storage (CCUS) has emerged as a promising approach, its large-scale implementation in emission-intensive industrial clustered region faces significant infrastructural challenges. Specifically, the optimal layout of regional CCUS clusterization and CO<sub>2</sub> transport networks remains unclear, particularly in highly industrialized regions such as China’s Jiangsu Province, where diverse industrial sectors and varied geological formations create complex source-sink matching challenges for CCUS deployment. In this study, we developed the SPATIAL (Strategic Pipeline And Technical Integration Analysis Layout) model that enables the optimization of CCUS deployment in emission-intensive regions from an industrial cluster perspective by integrating data of emissions from major industrial sources and storage potential from geological formations. The model was applied to Jiangsu Province under high, medium, and low emission reduction target scenarios through source-sink matching. Results show significant spatial heterogeneity between emission sources and geological storage resources in Jiangsu Province. For example, southern Jiangsu, characterized by high-intensity CO<sub>2</sub> emission clusters, accounts for 63 % of the province’s total emissions while holding only 0.03 % of the province’s geological storage potential. The optimal layout for regional CCUS clusterization deployment under high, medium, and low emission reduction targets achieve total CO<sub>2</sub> storage of 1.4, 1.1, and 0.9 Gt, respectively, supported by pipeline networks of 4629, 2513, and 1433 km. These layouts demonstrate economies of scale, with unit emission reduction costs ranging from 93.84 to 179.31 CNY/t CO<sub>2</sub>. Our findings establish the technical and economic feasibility of achieving significant emission reductions through regional CCUS clusterization deployment and address a critical gap in ignoring the hot spot phenomenon of industrial cluster. This study further emphasizes the importance of inter-regional coordination, regional geological storage resource management, and integrated infrastructure planning in realizing cost-effective CCUS clusterization implementation. This study provides policymakers with actionable insights for formulating CCUS clusterization strategies in emission-intensive industrial regions, contributing to the broader goal of regional carbon neutrality.</div></div>","PeriodicalId":9387,"journal":{"name":"Carbon Capture Science & Technology","volume":"17 ","pages":"Article 100495"},"PeriodicalIF":0.0,"publicationDate":"2025-08-26","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"145020149","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":0,"RegionCategory":"","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Pub Date : 2025-08-24DOI: 10.1016/j.ccst.2025.100493
Ye-Sub Son , Shaukat Ali Mazari , Min-Kyeong Oh , Gwan Hong Min , Hyung Jin Park , Sunghoon Lee , Il-Hyun Baek , Chang-Ha Lee , Jong-Ho Moon , Sung-Chan Nam
The contribution of solvent regeneration energy to amine-based CO2 capture processes is a major hurdle to their large-scale economic viability. It is important to develop solvents that reduce CO2 capture cost without compromising the process performance or operations. To reduce regeneration energy, this study focuses on the development of aqueous blends of piperazine (PZ) and 3-dimethylamino-1-propanol (3DMA1P) as an energy-efficient absorbent for CO2 capture. The study relies on rigorous modeling, supported by experimental data. The experimental data from this study and the literature includes CO2 solubility, NMR speciation, heat of absorption, and physical properties. To determine the potential application of PZ-3DMA1P blend for CO2 capture, their equilibrium CO2 solubility, cyclic capacity, heat of absorption, and, more importantly, solvent regeneration energy was investigated. Regeneration energy is calculated and evaluated under the influence of various operating parameters such as absorber temperature (313.15–343.15 K), stripper temperature (373.15–403.15 K), CO2 partial pressure (1–30 kPa), stripper total pressure (200–400 kPa), CO2 recovery (80–95 %), amine blending ratio (PZ:3DMA1P, 0–10:40–30 wt.%) and water concentration (60–90 wt.%). The results were compared with those obtained under the same operating conditions using monoethanolamine (MEA) 30 and 40 wt.%, and CESAR-1, the benchmark solvents. Results of the current study for blends of PZ and 3DMA1P are promising, and the solvent system exhibits higher CO2 absorption capacity and lower regeneration energy compared to MEA and CESAR-1. A comprehensive parametric analysis of regeneration energy enhances the applicability of the results across a diverse range of industries.
{"title":"Energy-efficient CO2 capture with piperazine and 3-dimethylamino-1-propanol blends: Modeling, experimental validation, and regeneration energy optimization","authors":"Ye-Sub Son , Shaukat Ali Mazari , Min-Kyeong Oh , Gwan Hong Min , Hyung Jin Park , Sunghoon Lee , Il-Hyun Baek , Chang-Ha Lee , Jong-Ho Moon , Sung-Chan Nam","doi":"10.1016/j.ccst.2025.100493","DOIUrl":"10.1016/j.ccst.2025.100493","url":null,"abstract":"<div><div>The contribution of solvent regeneration energy to amine-based CO<sub>2</sub> capture processes is a major hurdle to their large-scale economic viability. It is important to develop solvents that reduce CO<sub>2</sub> capture cost without compromising the process performance or operations. To reduce regeneration energy, this study focuses on the development of aqueous blends of piperazine (PZ) and 3-dimethylamino-1-propanol (3DMA1P) as an energy-efficient absorbent for CO<sub>2</sub> capture. The study relies on rigorous modeling, supported by experimental data. The experimental data from this study and the literature includes CO<sub>2</sub> solubility, NMR speciation, heat of absorption, and physical properties. To determine the potential application of PZ-3DMA1P blend for CO<sub>2</sub> capture, their equilibrium CO<sub>2</sub> solubility, cyclic capacity, heat of absorption, and, more importantly, solvent regeneration energy was investigated. Regeneration energy is calculated and evaluated under the influence of various operating parameters such as absorber temperature (313.15–343.15 K), stripper temperature (373.15–403.15 K), CO<sub>2</sub> partial pressure (1–30 kPa), stripper total pressure (200–400 kPa), CO<sub>2</sub> recovery (80–95 %), amine blending ratio (PZ:3DMA1P, 0–10:40–30 wt.%) and water concentration (60–90 wt.%). The results were compared with those obtained under the same operating conditions using monoethanolamine (MEA) 30 and 40 wt.%, and CESAR-1, the benchmark solvents. Results of the current study for blends of PZ and 3DMA1P are promising, and the solvent system exhibits higher CO<sub>2</sub> absorption capacity and lower regeneration energy compared to MEA and CESAR-1. A comprehensive parametric analysis of regeneration energy enhances the applicability of the results across a diverse range of industries.</div></div>","PeriodicalId":9387,"journal":{"name":"Carbon Capture Science & Technology","volume":"16 ","pages":"Article 100493"},"PeriodicalIF":0.0,"publicationDate":"2025-08-24","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"144913238","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":0,"RegionCategory":"","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Pub Date : 2025-08-24DOI: 10.1016/j.ccst.2025.100496
Yakubu Adekunle Alli , Onome Ejeromedoghene , Tendai O. Dembaremba , Amer Adawi , Oyekunle Azeez Alimi , Teckla Njei , Abayomi Bamisaye , Alex Kofi , Uche Quincy Anene , Adekola Monsuru Adewale , Zainab Temitope Yaqub , Motunrayo Eniola Oladele , Lateefat Jimoh , Samuel Oluwadadepo Oni , Adeniyi Sunday Ogunlaja , Ben Bin Xu
The rapid rise in atmospheric carbon dioxide (CO₂) concentrations continues to threaten global climate stability, underscoring the urgent need for scalable, economically viable, and sustainable CO₂ mitigation strategies. Among emerging solutions, CO₂ conversion technologies offer a transformative pathway by enabling the utilization of CO₂ as a renewable carbon feedstock for the production of fuels, chemicals, and materials, thereby promoting a circular carbon economy. The review begins by exploring foundational CO₂ capture and pre-treatment methods, emphasizing advanced materials, as well as integration strategies that directly couple capture with conversion processes as a gateway to improved CO2 conversion. Recent advancements in CO₂ conversion technologies, spanning thermochemical, electrochemical, photochemical, and biological domains are then covered. The integration of CO₂ conversion systems with renewable energy and industrial infrastructures is explored through case studies and commercialization efforts, highlighting opportunities for sector-wide decarbonization. Furthermore, the increasing role of artificial intelligence (AI) and machine learning (ML) in predictive modeling, catalyst design, and process optimization, as well as the techno-economic analyses that frame the practical deployment of these technologies is also presented. Persistent challenges including energy efficiency, long-term stability, product selectivity, and regulatory constraints are critically analyzed, and emerging solutions are proposed. The review concludes by outlining future research directions, including the development of next-generation technologies and strategies to promote interdisciplinary collaboration and public-private partnerships. By synthesizing cutting-edge advancements and identifying key barriers and opportunities, this work provides a roadmap for accelerating the global deployment of CO₂ conversion technologies toward a sustainable and decarbonized future.
{"title":"Perspectives on the status and future of sustainable CO2 conversion processes and their implementation","authors":"Yakubu Adekunle Alli , Onome Ejeromedoghene , Tendai O. Dembaremba , Amer Adawi , Oyekunle Azeez Alimi , Teckla Njei , Abayomi Bamisaye , Alex Kofi , Uche Quincy Anene , Adekola Monsuru Adewale , Zainab Temitope Yaqub , Motunrayo Eniola Oladele , Lateefat Jimoh , Samuel Oluwadadepo Oni , Adeniyi Sunday Ogunlaja , Ben Bin Xu","doi":"10.1016/j.ccst.2025.100496","DOIUrl":"10.1016/j.ccst.2025.100496","url":null,"abstract":"<div><div>The rapid rise in atmospheric carbon dioxide (CO₂) concentrations continues to threaten global climate stability, underscoring the urgent need for scalable, economically viable, and sustainable CO₂ mitigation strategies. Among emerging solutions, CO₂ conversion technologies offer a transformative pathway by enabling the utilization of CO₂ as a renewable carbon feedstock for the production of fuels, chemicals, and materials, thereby promoting a circular carbon economy. The review begins by exploring foundational CO₂ capture and pre-treatment methods, emphasizing advanced materials, as well as integration strategies that directly couple capture with conversion processes as a gateway to improved CO<sub>2</sub> conversion. Recent advancements in CO₂ conversion technologies, spanning thermochemical, electrochemical, photochemical, and biological domains are then covered. The integration of CO₂ conversion systems with renewable energy and industrial infrastructures is explored through case studies and commercialization efforts, highlighting opportunities for sector-wide decarbonization. Furthermore, the increasing role of artificial intelligence (AI) and machine learning (ML) in predictive modeling, catalyst design, and process optimization, as well as the techno-economic analyses that frame the practical deployment of these technologies is also presented. Persistent challenges including energy efficiency, long-term stability, product selectivity, and regulatory constraints are critically analyzed, and emerging solutions are proposed. The review concludes by outlining future research directions, including the development of next-generation technologies and strategies to promote interdisciplinary collaboration and public-private partnerships. By synthesizing cutting-edge advancements and identifying key barriers and opportunities, this work provides a roadmap for accelerating the global deployment of CO₂ conversion technologies toward a sustainable and decarbonized future.</div></div>","PeriodicalId":9387,"journal":{"name":"Carbon Capture Science & Technology","volume":"16 ","pages":"Article 100496"},"PeriodicalIF":0.0,"publicationDate":"2025-08-24","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"144913319","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":0,"RegionCategory":"","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Pub Date : 2025-08-24DOI: 10.1016/j.ccst.2025.100494
Jin Kim , Seokyoon Moon , Dongjae Kim
The importance of carbon capture, utilization, and storage (CCUS) for achieving carbon neutrality is increasingly recognized. Carbonate minerals are currently being manufactured from the abundant calcium-containing wastes and minerals that are generated by carbon mineralization technology in industry. Among these, calcium carbonate, which is highly versatile, generally exists in three crystal forms (vaterite, aragonite, and calcite). These three crystal forms must be freely controllable to increase the value and range of use of calcium carbonate. In this study, the variables of concentration, temperature, pH, stirring speed, and stirring time were changed during the reaction of calcium raw material (i.e., CaCl2) and carbon raw material (i.e., K2CO3). In addition, the phase composition ratios were determined by Rietveld refinement analysis using X-ray diffraction (XRD) patterns. Drawing on an extensive set of experimental data, we constructed data-driven predictive models by training and evaluating multilayer perceptron (MLP), support vector machine (SVM), random forest (RF), and decision tree (DT) algorithms. The best-performing model, selected by k-fold cross-validation, was then applied to determine the optimal operating conditions to control crystallinity. This study provides comprehensive knowledge about a system that allows industries to select, manufacture, and produce calcium carbonate in the crystal form they need. It is anticipated that using carbon mineralization technology, which is part of CCUS technology, will contribute to carbon neutrality, while alleviating waste environmental treatment costs.
{"title":"Artificial Intelligence Prediction of Carbonate Crystallinity of Carbon Mineralization","authors":"Jin Kim , Seokyoon Moon , Dongjae Kim","doi":"10.1016/j.ccst.2025.100494","DOIUrl":"10.1016/j.ccst.2025.100494","url":null,"abstract":"<div><div>The importance of carbon capture, utilization, and storage (CCUS) for achieving carbon neutrality is increasingly recognized. Carbonate minerals are currently being manufactured from the abundant calcium-containing wastes and minerals that are generated by carbon mineralization technology in industry. Among these, calcium carbonate, which is highly versatile, generally exists in three crystal forms (vaterite, aragonite, and calcite). These three crystal forms must be freely controllable to increase the value and range of use of calcium carbonate. In this study, the variables of concentration, temperature, pH, stirring speed, and stirring time were changed during the reaction of calcium raw material (i.e., CaCl<sub>2</sub>) and carbon raw material (i.e., K<sub>2</sub>CO<sub>3</sub>). In addition, the phase composition ratios were determined by Rietveld refinement analysis using X-ray diffraction (XRD) patterns. Drawing on an extensive set of experimental data, we constructed data-driven predictive models by training and evaluating multilayer perceptron (MLP), support vector machine (SVM), random forest (RF), and decision tree (DT) algorithms. The best-performing model, selected by k-fold cross-validation, was then applied to determine the optimal operating conditions to control crystallinity. This study provides comprehensive knowledge about a system that allows industries to select, manufacture, and produce calcium carbonate in the crystal form they need. It is anticipated that using carbon mineralization technology, which is part of CCUS technology, will contribute to carbon neutrality, while alleviating waste environmental treatment costs.</div></div>","PeriodicalId":9387,"journal":{"name":"Carbon Capture Science & Technology","volume":"16 ","pages":"Article 100494"},"PeriodicalIF":0.0,"publicationDate":"2025-08-24","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"144913318","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":0,"RegionCategory":"","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Pub Date : 2025-08-24DOI: 10.1016/j.ccst.2025.100497
Baljeet Singh, Zahra Eshaghi Gorji, Luc Charbonneau, Timo Repo
Direct Air Capture (DAC) and Post-Combustion CO2 capture (PCC) using liquid and solid amine sorbents, received enormous attention due to worsening weather and climate change. Enhancing the efficiency of CO2 capture and removal technologies is crucial, with a primary focus on reducing the energy demand for continuous capture-release cycles. Low-energy CO2 removal strategies offer promising durability and low operational costs, and a low levelized cost per ton of CO2 removal is preferred for large-scale implementation. This review highlights low-energy CO2 removal approaches, such as moisture/humidity swing sorbents. This discussion covers the influence of structural and molecular characteristics, the effect of counter anions on CO2 removal efficiency and kinetics, the impact of different operational factors on performance, and the long-term stability of these materials. Continuous exploration and optimization of these materials and methods are vital for advancing the moisture swing method, contributing to global efforts to combat climate change and promoting environmental sustainability. Finally, recommendations are provided for the design of innovative materials.
{"title":"Harnessing humidity for direct air capture: Moisture-swing sorbent design and mechanisms","authors":"Baljeet Singh, Zahra Eshaghi Gorji, Luc Charbonneau, Timo Repo","doi":"10.1016/j.ccst.2025.100497","DOIUrl":"10.1016/j.ccst.2025.100497","url":null,"abstract":"<div><div>Direct Air Capture (DAC) and Post-Combustion CO<sub>2</sub> capture (PCC) using liquid and solid amine sorbents, received enormous attention due to worsening weather and climate change. Enhancing the efficiency of CO<sub>2</sub> capture and removal technologies is crucial, with a primary focus on reducing the energy demand for continuous capture-release cycles. Low-energy CO<sub>2</sub> removal strategies offer promising durability and low operational costs, and a low levelized cost per ton of CO<sub>2</sub> removal is preferred for large-scale implementation. This review highlights low-energy CO<sub>2</sub> removal approaches, such as moisture/humidity swing sorbents. This discussion covers the influence of structural and molecular characteristics, the effect of counter anions on CO<sub>2</sub> removal efficiency and kinetics, the impact of different operational factors on performance, and the long-term stability of these materials. Continuous exploration and optimization of these materials and methods are vital for advancing the moisture swing method, contributing to global efforts to combat climate change and promoting environmental sustainability. Finally, recommendations are provided for the design of innovative materials.</div></div>","PeriodicalId":9387,"journal":{"name":"Carbon Capture Science & Technology","volume":"17 ","pages":"Article 100497"},"PeriodicalIF":0.0,"publicationDate":"2025-08-24","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"145096441","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":0,"RegionCategory":"","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Pub Date : 2025-08-20DOI: 10.1016/j.ccst.2025.100491
Shun Wang, Mengyin Xie, Shujuan Wang, Yuqun Zhuo
The increasing CO2 concentration in atmosphere leads to significant ecological changes, and the control of CO2 emissions has been a major concern worldwide. Amine-functionalized adsorbents are promising because they have high CO2 adsorption capacity, moderate adsorption heat and strong water resistance. Adsorption kinetics is a key performance parameter and facilitates the cognizance of microscopic CO2 adsorption process. A novel kinetic model was proposed, which categorized the amines of solid amine adsorbents into two regions: the open amine region and the closed amine region. Different from the open amine region, CO2 adsorption by amines in the closed amine region was significantly influenced by diffusion. The model could elucidate the effect of amine loading and temperature on CO2 adsorption. When amine loading was below the theoretical maximum loading, the CO2 adsorption capacity and the N efficiency gradually increased with the rise of amine loading. Nevertheless, as the amine loading further increased, the adsorption capacity decreased instead. CO2 adsorption by solid amines was not affected by external diffusion, but was significantly affected by internal diffusion. The percentage of closed amine region of adsorbents with high amine loading was large, CO2 needed to diffuse slowly into this region, leading to a small CO2 adsorption capacity at low temperature. When the amine loading was less than 0.5, the CO2 adsorption rate stayed almost the same. The model is instructive for the targeted preparation of solid amine adsorbents with fast adsorption rates.
{"title":"Kinetic model describing the effect of amine loading and temperature on CO2 capture by solid amine adsorbent","authors":"Shun Wang, Mengyin Xie, Shujuan Wang, Yuqun Zhuo","doi":"10.1016/j.ccst.2025.100491","DOIUrl":"10.1016/j.ccst.2025.100491","url":null,"abstract":"<div><div>The increasing CO<sub>2</sub> concentration in atmosphere leads to significant ecological changes, and the control of CO<sub>2</sub> emissions has been a major concern worldwide. Amine-functionalized adsorbents are promising because they have high CO<sub>2</sub> adsorption capacity, moderate adsorption heat and strong water resistance. Adsorption kinetics is a key performance parameter and facilitates the cognizance of microscopic CO<sub>2</sub> adsorption process. A novel kinetic model was proposed, which categorized the amines of solid amine adsorbents into two regions: the open amine region and the closed amine region. Different from the open amine region, CO<sub>2</sub> adsorption by amines in the closed amine region was significantly influenced by diffusion. The model could elucidate the effect of amine loading and temperature on CO<sub>2</sub> adsorption. When amine loading was below the theoretical maximum loading, the CO<sub>2</sub> adsorption capacity and the N efficiency gradually increased with the rise of amine loading. Nevertheless, as the amine loading further increased, the adsorption capacity decreased instead. CO<sub>2</sub> adsorption by solid amines was not affected by external diffusion, but was significantly affected by internal diffusion. The percentage of closed amine region of adsorbents with high amine loading was large, CO<sub>2</sub> needed to diffuse slowly into this region, leading to a small CO<sub>2</sub> adsorption capacity at low temperature. When the amine loading was less than 0.5, the CO<sub>2</sub> adsorption rate stayed almost the same. The model is instructive for the targeted preparation of solid amine adsorbents with fast adsorption rates.</div></div>","PeriodicalId":9387,"journal":{"name":"Carbon Capture Science & Technology","volume":"17 ","pages":"Article 100491"},"PeriodicalIF":0.0,"publicationDate":"2025-08-20","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"144913466","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":0,"RegionCategory":"","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Flowback and produced water (FPW) from hydraulic fracturing operations of tight hydrocarbon reservoirs has attracted significant research interest, particularly regarding its treatment and the recovery of valuable minerals. In this study, a simple and sustainable method was developed to precipitate calcium (Ca), magnesium (Mg), and strontium (Sr) carbonates from a high salinity FPW using NH3 or NaOH and CO2-containing flue gas. The precipitated solids and the treated FPW solution were subjected to various characterization techniques to evaluate the properties of the solids and the efficiency of the precipitation method. The precipitated carbonate minerals were further investigated as sorbents for CO2 capture in the calcium looping process, demonstrating a substantial carbon capture capacity of approximately 0.3 kg CO2/kg solid sample. Moreover, a series of detailed process simulations and economic analysis were performed to further evaluate the potential of using solid precipitates from FPW in the calcium looping process. Two different operating modes and multiple cases of calcium looping using solid sorbents from FPW, integrated with renewable energy, were thoroughly studied. The economic analysis of this integrated technology showed a relatively comparable levelized cost of carbon capture, at less than $200 per tonne of CO2 captured. The techno-economic analysis of the overall process demonstrated the potential of the calcium looping process with carbonate precipitates from produced water as a possible approach for decarbonization and energy transition in the oil and gas industry.
致密油气储层水力压裂返排和采出水(FPW)引起了人们极大的研究兴趣,特别是在其处理和有价值矿物的回收方面。在本研究中,开发了一种简单且可持续的方法,利用NH3或NaOH和含二氧化碳的烟气从高盐度FPW中沉淀钙(Ca)、镁(Mg)和锶(Sr)碳酸盐。对沉淀固体和处理后的FPW溶液进行了各种表征技术,以评估固体的性质和沉淀方法的效率。进一步研究了沉淀的碳酸盐矿物作为钙环过程中二氧化碳捕获的吸附剂,证明了大约0.3 kg CO2/kg固体样品的可观碳捕获能力。此外,还进行了一系列详细的过程模拟和经济分析,以进一步评估在钙循环过程中使用FPW固体沉淀物的潜力。对FPW固体吸附剂与可再生能源相结合的两种不同操作模式和多例钙循环进行了深入研究。对这一综合技术的经济分析表明,碳捕获的成本相对相当,每捕获一吨二氧化碳不到200美元。对整个过程的技术经济分析表明,利用采出水中的碳酸盐沉淀物进行钙环工艺的潜力,可能是石油和天然气行业脱碳和能源转型的一种方法。
{"title":"Experimental investigation and techno-economic assessment of oilfield brine-derived carbonates for calcium looping CO2 capture","authors":"Rufan Zhou , Chunqing Jiang , Rafal Gieleciak , Lava Kumar Pillari , Lukas Bichler","doi":"10.1016/j.ccst.2025.100489","DOIUrl":"10.1016/j.ccst.2025.100489","url":null,"abstract":"<div><div>Flowback and produced water (FPW) from hydraulic fracturing operations of tight hydrocarbon reservoirs has attracted significant research interest, particularly regarding its treatment and the recovery of valuable minerals. In this study, a simple and sustainable method was developed to precipitate calcium (Ca), magnesium (Mg), and strontium (Sr) carbonates from a high salinity FPW using NH<sub>3</sub> or NaOH and CO<sub>2</sub>-containing flue gas. The precipitated solids and the treated FPW solution were subjected to various characterization techniques to evaluate the properties of the solids and the efficiency of the precipitation method. The precipitated carbonate minerals were further investigated as sorbents for CO<sub>2</sub> capture in the calcium looping process, demonstrating a substantial carbon capture capacity of approximately 0.3 kg CO<sub>2</sub>/kg solid sample. Moreover, a series of detailed process simulations and economic analysis were performed to further evaluate the potential of using solid precipitates from FPW in the calcium looping process. Two different operating modes and multiple cases of calcium looping using solid sorbents from FPW, integrated with renewable energy, were thoroughly studied. The economic analysis of this integrated technology showed a relatively comparable levelized cost of carbon capture, at less than $200 per tonne of CO<sub>2</sub> captured. The techno-economic analysis of the overall process demonstrated the potential of the calcium looping process with carbonate precipitates from produced water as a possible approach for decarbonization and energy transition in the oil and gas industry.</div></div>","PeriodicalId":9387,"journal":{"name":"Carbon Capture Science & Technology","volume":"16 ","pages":"Article 100489"},"PeriodicalIF":0.0,"publicationDate":"2025-08-19","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"144889727","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":0,"RegionCategory":"","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Pub Date : 2025-08-19DOI: 10.1016/j.ccst.2025.100486
Maximilian Krödel, Dominic Spescha, Agnieszka Kierzkowska, Felix Donat, Christoph R. Müller
Morphological changes of natural limestone-based CO2 sorbents during the cyclic transition between CaO and CaCO3 affect their carbonation rate and cyclic CO2 uptake. We examine the evolution of the pore structure of Havelock limestone during carbonation in the ranges (I) 2–100 nm, (II) 200–3000 nm and (III) > 3000 nm with unprecedented detail, and correlate morphological changes with the observed carbonation rate. Pores of region (I) are fully filled with CaCO3 at a CaO conversion > 60 % (1st cycle), leading to a loss of ∼ 90 % of the total surface area of the sorbent, whereas pores of region (II) are only partially filled, and pores of region (III) remain largely unaffected. Throughout the carbonation reaction in the 1st and 10th cycle, the observed carbonation rate decreases linearly with the decreasing total surface area of the sorbent. Supported by kinetic and morphological modelling, our findings challenge the widely used concept of a CaCO3 product layer of critical thickness limiting CO2 diffusion to CaO, implying that the reaction is limited by diffusion as soon as the surface of CaO is fully covered with CaCO3 crystallites. Our results further provide a perspective on the design of efficient CaO-based sorbents by tuning their pore diameter to be larger than > 100 nm, such that the pore volume (and the respective surface area) can be largely regenerated over cycling, in turn yielding a high cyclic CO2 uptake.
{"title":"Experimental and numerical investigation of the morphological changes of a natural limestone-based CO2 sorbent over repeated carbonation-calcination cycles","authors":"Maximilian Krödel, Dominic Spescha, Agnieszka Kierzkowska, Felix Donat, Christoph R. Müller","doi":"10.1016/j.ccst.2025.100486","DOIUrl":"10.1016/j.ccst.2025.100486","url":null,"abstract":"<div><div>Morphological changes of natural limestone-based CO<sub>2</sub> sorbents during the cyclic transition between CaO and CaCO<sub>3</sub> affect their carbonation rate and cyclic CO<sub>2</sub> uptake. We examine the evolution of the pore structure of Havelock limestone during carbonation in the ranges (I) 2–100 nm, (II) 200–3000 nm and (III) > 3000 nm with unprecedented detail, and correlate morphological changes with the observed carbonation rate. Pores of region (I) are fully filled with CaCO<sub>3</sub> at a CaO conversion > 60 % (1st cycle), leading to a loss of ∼ 90 % of the total surface area of the sorbent, whereas pores of region (II) are only partially filled, and pores of region (III) remain largely unaffected. Throughout the carbonation reaction in the 1st and 10th cycle, the observed carbonation rate decreases linearly with the decreasing total surface area of the sorbent. Supported by kinetic and morphological modelling, our findings challenge the widely used concept of a CaCO<sub>3</sub> product layer of critical thickness limiting CO<sub>2</sub> diffusion to CaO, implying that the reaction is limited by diffusion as soon as the surface of CaO is fully covered with CaCO<sub>3</sub> crystallites. Our results further provide a perspective on the design of efficient CaO-based sorbents by tuning their pore diameter to be larger than > 100 nm, such that the pore volume (and the respective surface area) can be largely regenerated over cycling, in turn yielding a high cyclic CO<sub>2</sub> uptake.</div></div>","PeriodicalId":9387,"journal":{"name":"Carbon Capture Science & Technology","volume":"16 ","pages":"Article 100486"},"PeriodicalIF":0.0,"publicationDate":"2025-08-19","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"144879249","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":0,"RegionCategory":"","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}