Pub Date : 2025-12-01Epub Date: 2025-09-07DOI: 10.1016/j.ccst.2025.100518
Paul de Joannis , Christophe Castel , Mohamed Kanniche , Eric Favre , Olivier Authier
This study investigates a direct air capture (DAC) process using a solid-DAC S-VTSA (steam-assisted vacuum thermal swing adsorption) process. A commercially available sorbent, commonly used in packed bed configurations, is selected as the benchmark sorbent, while a monolithic geometry is also examined to assess its potential performance. The process is modelled using Aspen Adsorption and incorporates physico-chemical data in DAC environmental conditions, including binary isotherms under humid condition. In a reference case comparing the two geometries, the packed bed exhibits higher productivity (2.4 kgCO2/(h.m3)), while the monolith achieves 1.2 kgCO2/(h.m3). However, the monolith allows for a significant reduction in pressure drop and associated fan work by about two orders of magnitude. These findings highlight the trade-off between productivity in favor of packed bed and energy requirement in favor of monolithic design. A sensitivity analysis is then conducted on various environmental and process parameters such as sorbent and bed dimension, air velocity, temperature and humidity, adsorption/desorption loading, mass transfer kinetic, and regeneration pressure, temperature, and steam flowrate. Detailed techno-economic analysis, using Aspen Process Economic Analyzer software for capital cost estimation, is performed at capture scale of 100 ktCO2/yr, with capture costs higher than 1500 €/tCO2.
{"title":"Techno-economic analysis of packed bed and structured adsorbent for direct air capture","authors":"Paul de Joannis , Christophe Castel , Mohamed Kanniche , Eric Favre , Olivier Authier","doi":"10.1016/j.ccst.2025.100518","DOIUrl":"10.1016/j.ccst.2025.100518","url":null,"abstract":"<div><div>This study investigates a direct air capture (DAC) process using a solid-DAC S-VTSA (steam-assisted vacuum thermal swing adsorption) process. A commercially available sorbent, commonly used in packed bed configurations, is selected as the benchmark sorbent, while a monolithic geometry is also examined to assess its potential performance. The process is modelled using Aspen Adsorption and incorporates physico-chemical data in DAC environmental conditions, including binary isotherms under humid condition. In a reference case comparing the two geometries, the packed bed exhibits higher productivity (2.4 kgCO<sub>2</sub>/(h.m<sup>3</sup>)), while the monolith achieves 1.2 kgCO<sub>2</sub>/(h.m<sup>3</sup>). However, the monolith allows for a significant reduction in pressure drop and associated fan work by about two orders of magnitude. These findings highlight the trade-off between productivity in favor of packed bed and energy requirement in favor of monolithic design. A sensitivity analysis is then conducted on various environmental and process parameters such as sorbent and bed dimension, air velocity, temperature and humidity, adsorption/desorption loading, mass transfer kinetic, and regeneration pressure, temperature, and steam flowrate. Detailed techno-economic analysis, using Aspen Process Economic Analyzer software for capital cost estimation, is performed at capture scale of 100 ktCO<sub>2</sub>/yr, with capture costs higher than 1500 €/tCO<sub>2</sub>.</div></div>","PeriodicalId":9387,"journal":{"name":"Carbon Capture Science & Technology","volume":"17 ","pages":"Article 100518"},"PeriodicalIF":0.0,"publicationDate":"2025-12-01","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"145217018","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 : 2025-12-01Epub 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":"2025-12-01","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 : 2025-12-01Epub Date: 2025-09-01DOI: 10.1016/j.ccst.2025.100503
Kamran Aghaee
Given the substantial share of global CO2 emissions attributable to construction materials, especially cement, there is rising interest in harnessing CO2 to enhance cementitious composites and generate value‑added products. Strategic carbon capture, utilization, and storage (CCUS) techniques including CO2 mixing, curing, and mineralization can improve the macro‑mechanical performance and microstructure of cement‑based materials and enable the development of novel binders and construction materials. This article synthesizes current CCUS techniques applicable to construction materials, particularly concrete composites, and elaborates on key parameters affecting their effectiveness. The findings suggest that CO2 mineralization is more effective than CO2 mixing and curing, revealing its considerable potential for producing carbon-sink materials from construction and industrial by-products that support circularity through reuse and closing the loop in construction. However, this approach still faces challenges related to scale-up and economic feasibility. This study compares and identifies the optimal implementation conditions to maximize material performance and production efficiency, while also evaluating the economic and environmental impacts of the technologies, with a focus on advancing circularity in construction.
{"title":"Carbon capture, utilization, and storage for sustainable construction: Insights into CO2 mixing, curing, and mineralization","authors":"Kamran Aghaee","doi":"10.1016/j.ccst.2025.100503","DOIUrl":"10.1016/j.ccst.2025.100503","url":null,"abstract":"<div><div>Given the substantial share of global CO<sub>2</sub> emissions attributable to construction materials, especially cement, there is rising interest in harnessing CO<sub>2</sub> to enhance cementitious composites and generate value‑added products. Strategic carbon capture, utilization, and storage (CCUS) techniques including CO<sub>2</sub> mixing, curing, and mineralization can improve the macro‑mechanical performance and microstructure of cement‑based materials and enable the development of novel binders and construction materials. This article synthesizes current CCUS techniques applicable to construction materials, particularly concrete composites, and elaborates on key parameters affecting their effectiveness. The findings suggest that CO<sub>2</sub> mineralization is more effective than CO<sub>2</sub> mixing and curing, revealing its considerable potential for producing carbon-sink materials from construction and industrial by-products that support circularity through reuse and closing the loop in construction. However, this approach still faces challenges related to scale-up and economic feasibility. This study compares and identifies the optimal implementation conditions to maximize material performance and production efficiency, while also evaluating the economic and environmental impacts of the technologies, with a focus on advancing circularity in construction.</div></div>","PeriodicalId":9387,"journal":{"name":"Carbon Capture Science & Technology","volume":"17 ","pages":"Article 100503"},"PeriodicalIF":0.0,"publicationDate":"2025-12-01","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"145096442","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 : 2025-12-01Epub Date: 2025-11-15DOI: 10.1016/j.ccst.2025.100542
Nadia Hartini Suhaimi , Norwahyu Jusoh , Boon Kar Yap , Mohammad Nur-E-Alam , Nonni Soraya Sambudi , Li Sze Lai , Amir Izzuddin Adnan
Polymer-filler incompatibility and interface defects are key challenges faced in hybrid membranes, hindering the effective separation performance in CO2 separation applications. Ligand modification on the metal-organic framework (MOF)-based filler is a beneficial approach to overcome these challenges by creating hydrogen bonding, which positively impacts the interfacial compatibility. This review aims to elucidate the role of amine-functionalization (-NH2) by discussing available synthesis techniques, its influence on the physicochemical properties of modified fillers, and macroscopic separation performance. Additionally, this review specifically highlights the NH2 group interactions at the filler-polymer-gas interface, which contribute to positive CO2 separation performance. Besides, the key challenges associated with adding amine-functionalized MOF-based filler within hybrid membranes are outlined, along with adaptive measures proposed in tackling these challenges. Overall, this review highlights the role of –NH₂ ligand modification in amine-functionalized MOF-based hybrid membranes, emphasizing current progress and outlining future potential to advance research in CO₂ separation technologies.
{"title":"Amine-functionalized MOF-based hybrid membranes for CO₂ separation: Molecular interactions and separation performance","authors":"Nadia Hartini Suhaimi , Norwahyu Jusoh , Boon Kar Yap , Mohammad Nur-E-Alam , Nonni Soraya Sambudi , Li Sze Lai , Amir Izzuddin Adnan","doi":"10.1016/j.ccst.2025.100542","DOIUrl":"10.1016/j.ccst.2025.100542","url":null,"abstract":"<div><div>Polymer-filler incompatibility and interface defects are key challenges faced in hybrid membranes, hindering the effective separation performance in CO<sub>2</sub> separation applications. Ligand modification on the metal-organic framework (MOF)-based filler is a beneficial approach to overcome these challenges by creating hydrogen bonding, which positively impacts the interfacial compatibility. This review aims to elucidate the role of amine-functionalization (-NH<sub>2</sub>) by discussing available synthesis techniques, its influence on the physicochemical properties of modified fillers, and macroscopic separation performance. Additionally, this review specifically highlights the NH<sub>2</sub> group interactions at the filler-polymer-gas interface, which contribute to positive CO<sub>2</sub> separation performance. Besides, the key challenges associated with adding amine-functionalized MOF-based filler within hybrid membranes are outlined, along with adaptive measures proposed in tackling these challenges. Overall, this review highlights the role of –NH₂ ligand modification in amine-functionalized MOF-based hybrid membranes, emphasizing current progress and outlining future potential to advance research in CO₂ separation technologies.</div></div>","PeriodicalId":9387,"journal":{"name":"Carbon Capture Science & Technology","volume":"17 ","pages":"Article 100542"},"PeriodicalIF":0.0,"publicationDate":"2025-12-01","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"145568350","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 : 2025-12-01Epub Date: 2025-11-13DOI: 10.1016/j.ccst.2025.100540
Shihang Yu , Cong Li , Li Lyu , Rongsheng Cai , Lifeng Xiao , Yilai Jiao , Huanhao Chen , Xiaoxia Ou , Xiaoyang Wei , Xaiolei Fan
Experimental studies of dry reforming of methane (DRM) under bubbling regime in the thermal fluidized bed reactors (FBRs) remain limited. In this study, a thermal FBR was developed, and catalytic DRM was systematically evaluated. Nickel-supported catalysts (Ni/FCC) were prepared via a wet impregnation method using commercial fluid catalytic cracking (FCC) particles, and their physicochemical properties were comprehensively characterized. Detailed fluidization behaviour was investigated using pressure drop fluctuations and discrete wavelet transformation (DWT), revealing a transition velocity (Uc) between bubbling and turbulent regimes in the FBR (under the conditions relevant to DRM), which was found to decrease with increasing temperature. DRM performance of Ni/FCC was assessed under various reaction temperatures (600–800 °C), gas velocities (0.1–0.2 m/s), and preheating conditions. Optimal operation in the bubbling regime (800 °C, 0.1 m/s) enabled CO2 and CH4 conversions of 57% and 41%, respectively, with an H2/CO ratio of 0.67. Comparative studies demonstrated that the packed bed reactor (PBR) achieved higher conversions and better H2/CO ratios (∼0.96), attributed to its plug flow characteristics, whereas the FBR exhibited lower conversions due to gas back mixing and reactant bypassing. Nevertheless, the Ni/FCC catalyst exhibited good thermal stability and negligible deactivation in both reactor configurations during 20 h of continuous operation. These findings provide practical insights into the design, operation, and catalytic behaviour of FBR systems for industrial DRM applications.
{"title":"Development of a fluidized bed reactor for catalytic dry reforming of methane with CO2","authors":"Shihang Yu , Cong Li , Li Lyu , Rongsheng Cai , Lifeng Xiao , Yilai Jiao , Huanhao Chen , Xiaoxia Ou , Xiaoyang Wei , Xaiolei Fan","doi":"10.1016/j.ccst.2025.100540","DOIUrl":"10.1016/j.ccst.2025.100540","url":null,"abstract":"<div><div>Experimental studies of dry reforming of methane (DRM) under bubbling regime in the thermal fluidized bed reactors (FBRs) remain limited. In this study, a thermal FBR was developed, and catalytic DRM was systematically evaluated. Nickel-supported catalysts (Ni/FCC) were prepared via a wet impregnation method using commercial fluid catalytic cracking (FCC) particles, and their physicochemical properties were comprehensively characterized. Detailed fluidization behaviour was investigated using pressure drop fluctuations and discrete wavelet transformation (DWT), revealing a transition velocity (Uc) between bubbling and turbulent regimes in the FBR (under the conditions relevant to DRM), which was found to decrease with increasing temperature. DRM performance of Ni/FCC was assessed under various reaction temperatures (600–800 °C), gas velocities (0.1–0.2 m/s), and preheating conditions. Optimal operation in the bubbling regime (800 °C, 0.1 m/s) enabled CO<sub>2</sub> and CH<sub>4</sub> conversions of 57% and 41%, respectively, with an H<sub>2</sub>/CO ratio of 0.67. Comparative studies demonstrated that the packed bed reactor (PBR) achieved higher conversions and better H<sub>2</sub>/CO ratios (∼0.96), attributed to its plug flow characteristics, whereas the FBR exhibited lower conversions due to gas back mixing and reactant bypassing. Nevertheless, the Ni/FCC catalyst exhibited good thermal stability and negligible deactivation in both reactor configurations during 20 h of continuous operation. These findings provide practical insights into the design, operation, and catalytic behaviour of FBR systems for industrial DRM applications.</div></div>","PeriodicalId":9387,"journal":{"name":"Carbon Capture Science & Technology","volume":"17 ","pages":"Article 100540"},"PeriodicalIF":0.0,"publicationDate":"2025-12-01","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"145568415","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 : 2025-12-01Epub Date: 2025-11-26DOI: 10.1016/j.ccst.2025.100551
Aaqib Ali , Arshad Raza , Mubashir Aziz , Mohamed Mahmoud , Umair Ali , Ammar Mohammed Alshammari
Accelerated soil carbonation (ASC) is a rapidly advancing carbon capture and storage technique which provides a dual benefit of permanent CO2 sequestration and geotechnical soil stabilization. This paper presents a comprehensive review of soil carbonation processes, emphasizing the mechanisms, quantification methods, and engineering performance improvements achieved through MgO and CaO-based binders and industrial by-products. The carbonation process transforms reactive oxides into stable carbonate minerals, enhancing soil strength, stiffness, and durability while reducing moisture content and porosity. A systematic analysis of the impact of carbonation on physical, chemical, mechanical, and microstructural behavior is presented, together with quantification approaches such as thermogravimetric analysis, calcimetry, and gas-balance techniques. The techno-economic evaluation highlights that optimized magnesia-lime-slag systems can offset up to 70 % of embodied emissions, offering a cost-effective and scalable pathway for carbon-negative ground improvement. Despite these advances, the field faces challenges related to reaction uniformity, long-term durability, and standardization of quantification and field protocols. The study identifies key research directions to establish ASC as a reliable, sustainable, and verifiable carbon sequestration strategy in geotechnical engineering.
{"title":"Advanced soil carbonation strategies: insights into quantification, performance, and scalable carbon capture","authors":"Aaqib Ali , Arshad Raza , Mubashir Aziz , Mohamed Mahmoud , Umair Ali , Ammar Mohammed Alshammari","doi":"10.1016/j.ccst.2025.100551","DOIUrl":"10.1016/j.ccst.2025.100551","url":null,"abstract":"<div><div>Accelerated soil carbonation (ASC) is a rapidly advancing carbon capture and storage technique which provides a dual benefit of permanent CO<sub>2</sub> sequestration and geotechnical soil stabilization. This paper presents a comprehensive review of soil carbonation processes, emphasizing the mechanisms, quantification methods, and engineering performance improvements achieved through MgO and CaO-based binders and industrial by-products. The carbonation process transforms reactive oxides into stable carbonate minerals, enhancing soil strength, stiffness, and durability while reducing moisture content and porosity. A systematic analysis of the impact of carbonation on physical, chemical, mechanical, and microstructural behavior is presented, together with quantification approaches such as thermogravimetric analysis, calcimetry, and gas-balance techniques. The techno-economic evaluation highlights that optimized magnesia-lime-slag systems can offset up to 70 % of embodied emissions, offering a cost-effective and scalable pathway for carbon-negative ground improvement. Despite these advances, the field faces challenges related to reaction uniformity, long-term durability, and standardization of quantification and field protocols. The study identifies key research directions to establish ASC as a reliable, sustainable, and verifiable carbon sequestration strategy in geotechnical engineering.</div></div>","PeriodicalId":9387,"journal":{"name":"Carbon Capture Science & Technology","volume":"17 ","pages":"Article 100551"},"PeriodicalIF":0.0,"publicationDate":"2025-12-01","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"145680888","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 : 2025-12-01Epub Date: 2025-09-16DOI: 10.1016/j.ccst.2025.100516
Milad Shakouri Kalfati, Ahmed Abdulla
Averting the worst consequences of climate change requires decarbonizing the global energy system and deploying carbon dioxide removal technologies, including the direct air capture of CO. To estimate the cost and performance of the latter technologies, climate and energy system analysts need numerical process models that are validated with experimental data. Existing process models often limit reconfiguration that accommodates different design choices or restrict modelling to steady-state conditions. However, ambient environmental conditions like temperature, humidity, pressure, and inlet CO concentration vary, affecting capture. This study develops an open-source process model for direct air capture using solid sorbents. Starting from first principles, this model allows users to select facility sizes, sorbents, other design parameters, and locations to simulate the capture performance of a solid sorbent direct air capture plant. More importantly, users can incorporate climate data to determine site-specific performance. Here, model validation is presented for two cold-climate sorbents that are being proposed for nations in northern latitudes. Results for climatically different cities are presented, highlighting the importance of sorbent choice and ambient environmental conditions on the overall capture performance and energy requirement of a direct air capture facility. The model can be employed by engineers, investors, and energy system analysts to undertake design optimization research, siting analyses, and improved studies that integrate high-fidelity process models into energy system optimization.
{"title":"An open-source dynamic model for direct air capture of carbon dioxide using solid sorbents","authors":"Milad Shakouri Kalfati, Ahmed Abdulla","doi":"10.1016/j.ccst.2025.100516","DOIUrl":"10.1016/j.ccst.2025.100516","url":null,"abstract":"<div><div>Averting the worst consequences of climate change requires decarbonizing the global energy system and deploying carbon dioxide removal technologies, including the direct air capture of CO<span><math><msub><mrow></mrow><mn>2</mn></msub></math></span>. To estimate the cost and performance of the latter technologies, climate and energy system analysts need numerical process models that are validated with experimental data. Existing process models often limit reconfiguration that accommodates different design choices or restrict modelling to steady-state conditions. However, ambient environmental conditions like temperature, humidity, pressure, and inlet CO<span><math><msub><mrow></mrow><mn>2</mn></msub></math></span> concentration vary, affecting capture. This study develops an open-source process model for direct air capture using solid sorbents. Starting from first principles, this model allows users to select facility sizes, sorbents, other design parameters, and locations to simulate the capture performance of a solid sorbent direct air capture plant. More importantly, users can incorporate climate data to determine site-specific performance. Here, model validation is presented for two cold-climate sorbents that are being proposed for nations in northern latitudes. Results for climatically different cities are presented, highlighting the importance of sorbent choice and ambient environmental conditions on the overall capture performance and energy requirement of a direct air capture facility. The model can be employed by engineers, investors, and energy system analysts to undertake design optimization research, siting analyses, and improved studies that integrate high-fidelity process models into energy system optimization.</div></div>","PeriodicalId":9387,"journal":{"name":"Carbon Capture Science & Technology","volume":"17 ","pages":"Article 100516"},"PeriodicalIF":0.0,"publicationDate":"2025-12-01","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"145262668","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 : 2025-12-01Epub Date: 2025-10-20DOI: 10.1016/j.ccst.2025.100533
Heidi Kirppu, Miika Rämä, Esa Pursiheimo, Kati Koponen, Tomi J. Lindroos
Achieving Paris Agreement targets for climate change mitigation requires an urgent shift away from fossil fuels. In addition, negative emissions by permanently removing carbon dioxide from the atmosphere are required. Both targets require substantial amounts of carbon neutral electricity and heat production. While electricity can be produced and transferred over long distances, the heat production needs to be local. This study investigates an energy system integrating both carbon neutral heat production and carbon dioxide removal from the atmosphere. The system is modelled using the Backbone energy system modelling framework. The carbon neutral heat production in the study is based on small modular nuclear reactors (SMRs), large-scale thermal energy storages (TES), heat pumps (HPs) and electric boilers (EBs), and the carbon removal is implemented by direct air capture (DAC) combined with permanent geological storage. The studied technologies are integrated into a specific large-scale district heating system located in Northern Europe. The impact of outdoor temperature for the efficiency of the DAC process is considered, and the system integration potential with the district heating system is evaluated. The results show that high 70–90 % utilisation rates for both SMR and DAC units can be reached but depending on the case year and corresponding profiles for demand, outdoor temperature, electricity and carbon prices, a large variation in utilisation rates is observed. The variable CO2 capture costs were between 115–126 €/t CO2 in the modelled scenarios, and with higher OPEX values at the range 152–163€/tCO2, and the limit price for economic viability considering the investment was calculated to be in the range of 209–223 €/tCO2, with lower, and 233–246 €/tCO2 with higher adsorbent costs. When not accounting the biogenic CO2 emissions, the carbon negativity can be reached in the system in all the scenarios where the CO2 price is over 150€/t and the number of DAC modules is at least 400. When accounting the biogenic CO2 emissions, the carbon negativity can be reached only in scenarios with DAC capacity at 900 modules and CO2 price at 180–200€/t.
{"title":"District heating with negative emissions – direct air carbon capture and storage combined with small modular reactors","authors":"Heidi Kirppu, Miika Rämä, Esa Pursiheimo, Kati Koponen, Tomi J. Lindroos","doi":"10.1016/j.ccst.2025.100533","DOIUrl":"10.1016/j.ccst.2025.100533","url":null,"abstract":"<div><div>Achieving Paris Agreement targets for climate change mitigation requires an urgent shift away from fossil fuels. In addition, negative emissions by permanently removing carbon dioxide from the atmosphere are required. Both targets require substantial amounts of carbon neutral electricity and heat production. While electricity can be produced and transferred over long distances, the heat production needs to be local. This study investigates an energy system integrating both carbon neutral heat production and carbon dioxide removal from the atmosphere. The system is modelled using the Backbone energy system modelling framework. The carbon neutral heat production in the study is based on small modular nuclear reactors (SMRs), large-scale thermal energy storages (TES), heat pumps (HPs) and electric boilers (EBs), and the carbon removal is implemented by direct air capture (DAC) combined with permanent geological storage. The studied technologies are integrated into a specific large-scale district heating system located in Northern Europe. The impact of outdoor temperature for the efficiency of the DAC process is considered, and the system integration potential with the district heating system is evaluated. The results show that high 70–90 % utilisation rates for both SMR and DAC units can be reached but depending on the case year and corresponding profiles for demand, outdoor temperature, electricity and carbon prices, a large variation in utilisation rates is observed. The variable CO<sub>2</sub> capture costs were between 115–126 €/t CO<sub>2</sub> in the modelled scenarios, and with higher OPEX values at the range 152–163€/tCO<sub>2</sub>, and the limit price for economic viability considering the investment was calculated to be in the range of 209–223 €/tCO<sub>2,</sub> with lower, and 233–246 €/tCO<sub>2</sub> with higher adsorbent costs. When not accounting the biogenic CO<sub>2</sub> emissions, the carbon negativity can be reached in the system in all the scenarios where the CO<sub>2</sub> price is over 150€/t and the number of DAC modules is at least 400. When accounting the biogenic CO<sub>2</sub> emissions, the carbon negativity can be reached only in scenarios with DAC capacity at 900 modules and CO<sub>2</sub> price at 180–200€/t.</div></div>","PeriodicalId":9387,"journal":{"name":"Carbon Capture Science & Technology","volume":"17 ","pages":"Article 100533"},"PeriodicalIF":0.0,"publicationDate":"2025-12-01","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"145412812","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 : 2025-12-01Epub Date: 2025-09-22DOI: 10.1016/j.ccst.2025.100523
Kayode Adesina Adegoke, Potlaki Foster Tseki
The CO2 reduction reactions present a viable approach to addressing the challenges of energy scarcity and the pressing concerns of global warming. To enhance their kinetically sluggish processes, developing highly stable, cost-effective, selective, and energy-efficient catalysts is essential. Graphene-based metal-organic frameworks (MOFs) composite exhibits characteristics such as outstanding conductivity, structural tunability, and excellent surface chemistry and sustainability, positioning them as innovative competitors for both CO2 conversion to fuels and chemicals. In this study, we present recent developments in graphene-based MOF catalysts for CO2 reduction reactions (CO2RR). Before discussing the evaluation of the approaches for graphene-based MOFs, rational, structural, and electronic synergies of graphene/MOF nanocomposites were addressed. Various synthetic techniques, a comprehensive review of characterization techniques, associated challenges, and the relation between graphene-based MOF structures and their conductivity are examined. A detailed breakthrough in both photocatalytic and electrocatalytic performance for CO2RR is examined. The concluding remarks emphasized the knowledge gaps, related deficiencies, and strengths, with significant viewpoints and concepts for enhancing graphene-based MOFs for CO2RR in accordance with pragmatic industry expectations. This study offers the scientific community a thorough insight into the present research emphasis and the significance of creating more efficient and environmentally sustainable graphene-based MOFs for clean energy conversion. This is essential for tackling the difficulties of reducing greenhouse gas emissions and alleviating the global energy deficit.
{"title":"Graphene-based metal-organic framework nanocomposites for CO2 reduction reactions","authors":"Kayode Adesina Adegoke, Potlaki Foster Tseki","doi":"10.1016/j.ccst.2025.100523","DOIUrl":"10.1016/j.ccst.2025.100523","url":null,"abstract":"<div><div>The CO<sub>2</sub> reduction reactions present a viable approach to addressing the challenges of energy scarcity and the pressing concerns of global warming. To enhance their kinetically sluggish processes, developing highly stable, cost-effective, selective, and energy-efficient catalysts is essential. Graphene-based metal-organic frameworks (MOFs) composite exhibits characteristics such as outstanding conductivity, structural tunability, and excellent surface chemistry and sustainability, positioning them as innovative competitors for both CO<sub>2</sub> conversion to fuels and chemicals. In this study, we present recent developments in graphene-based MOF catalysts for CO<sub>2</sub> reduction reactions (CO<sub>2</sub>RR). Before discussing the evaluation of the approaches for graphene-based MOFs, rational, structural, and electronic synergies of graphene/MOF nanocomposites were addressed. Various synthetic techniques, a comprehensive review of characterization techniques, associated challenges, and the relation between graphene-based MOF structures and their conductivity are examined. A detailed breakthrough in both photocatalytic and electrocatalytic performance for CO<sub>2</sub>RR is examined. The concluding remarks emphasized the knowledge gaps, related deficiencies, and strengths, with significant viewpoints and concepts for enhancing graphene-based MOFs for CO<sub>2</sub>RR in accordance with pragmatic industry expectations. This study offers the scientific community a thorough insight into the present research emphasis and the significance of creating more efficient and environmentally sustainable graphene-based MOFs for clean energy conversion. This is essential for tackling the difficulties of reducing greenhouse gas emissions and alleviating the global energy deficit.</div></div>","PeriodicalId":9387,"journal":{"name":"Carbon Capture Science & Technology","volume":"17 ","pages":"Article 100523"},"PeriodicalIF":0.0,"publicationDate":"2025-12-01","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"145320913","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}