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Mechanistic elucidation of cascade CO2 hydrogenation enabled by Cu–Fe interfaces and oxygen vacancies Cu-Fe界面和氧空位导致CO2级联加氢的机理研究
Pub Date : 2025-08-28 DOI: 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。
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引用次数: 0
Assessing CO2 storage potential in a structurally complex depleted gas reservoir, offshore South Africa 评估南非海上一个结构复杂的枯竭气藏的二氧化碳储存潜力
Pub Date : 2025-08-27 DOI: 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.
随着全球减少温室气体排放的努力不断加强,碳捕获与封存(CCS)已成为减少化石燃料使用对环境影响的关键战略。然而,由于地质的复杂性,在结构复杂和非均质储层中,CO 2的地质储存带来了一系列问题,包括存储容量估算、CO 2注入、迁移甚至长期遏制,这带来了环境风险。因此,本研究基于对油田勘探和生产数据集的分析,采用了一种强大的建模方法,评估了南非近海Bredasdorp盆地枯竭的F-O气田的CO₂储存潜力。该油田具有高度的构造分区化和断层为界的背斜圈闭特征。瓦兰吉尼期海相砂岩储层具有低—中等孔渗特征。总的来说,F-O气田的CO₂储存量为1853 Mt,考虑到储层非均质性和波及效率,其储存量减少到37.1-74.1 Mt。这种减少反映了油田复杂的结构结构、多变的相分布和岩石物性变化的影响,这些因素共同限制了二氧化碳储存的有效孔隙体积。通过严格整合油田的构造结构、沉积过程、相分布和候选储层的岩石物理变异性,本研究为结构复杂的枯竭气田CCS的可行性提供了重要的见解和策略。重要的是,这些发现有助于正在进行的国家CCS评估,并支持南非的长期脱碳议程。
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引用次数: 0
Optimizing regional CCUS clusterization deployment for multi-industrial sectors: A carbon neutrality pathway for emission-intensive region 多产业区域CCUS集群布局优化:排放密集型区域的碳中和路径
Pub Date : 2025-08-26 DOI: 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.
快速减缓全球气候变化需要变革性技术创新,以实现深度脱碳。中国已承诺到2030年达到碳排放峰值和到2060年实现碳中和的双重碳目标,强调了这一挑战的紧迫性和规模。虽然碳捕集、利用与封存(CCUS)已成为一种有前景的方法,但其在排放密集型工业集群地区的大规模实施面临着重大的基础设施挑战。具体而言,区域CCUS集群和二氧化碳运输网络的最佳布局尚不清楚,特别是在中国江苏省等高度工业化地区,不同的工业部门和不同的地质构造为CCUS的部署带来了复杂的源汇匹配挑战。在本研究中,我们开发了空间(战略管道和技术集成分析布局)模型,通过整合主要工业源的排放数据和地质构造的储存潜力,从产业集群的角度优化CCUS在排放密集型地区的部署。通过源汇匹配,将模型应用于江苏省高、中、低三种减排目标情景。结果表明:江苏省排放源与地质储存资源之间存在显著的空间异质性。以苏南地区为例,该地区的二氧化碳排放强度较大,占全省总排放量的63%,而其地质储存量仅占全省的0.03%。高、中、低减排目标下区域CCUS集群部署的最优布局分别实现了1.4、1.1和0.9 Gt的CO2总储存量,管网长度分别为4629、2513和1433 km。这些布局具有规模经济效益,单位减排成本在93.84 - 179.31元/吨CO2之间。研究结果确立了通过区域CCUS集群化部署实现显著减排的技术和经济可行性,解决了忽视产业集群热点现象的关键空白。本研究进一步强调了区域间协调、区域地质存储资源管理和综合基础设施规划对实现CCUS集群经济效益的重要性。本研究为政策制定者在排放密集型工业地区制定CCUS集群战略提供了可操作的见解,有助于实现区域碳中和的更广泛目标。
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引用次数: 0
Energy-efficient CO2 capture with piperazine and 3-dimethylamino-1-propanol blends: Modeling, experimental validation, and regeneration energy optimization 哌嗪和3-二甲氨基-1-丙醇混合物的节能CO2捕集:建模、实验验证和再生能源优化
Pub Date : 2025-08-24 DOI: 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.
溶剂再生能源对胺基CO2捕集工艺的贡献是其大规模经济可行性的主要障碍。在不影响工艺性能或操作的情况下,开发降低二氧化碳捕获成本的溶剂非常重要。为了降低再生能量,本研究重点研究了哌嗪(PZ)和3-二甲氨基-1-丙醇(3DMA1P)的水共混物作为CO2捕获的节能吸收剂的开发。这项研究依赖于严格的建模,并得到实验数据的支持。本研究和文献的实验数据包括CO2溶解度、核磁共振形态、吸收热和物理性质。为了确定PZ-3DMA1P共混物在CO2捕集方面的潜在应用,研究了它们的平衡CO2溶解度、循环容量、吸收热,以及更重要的溶剂再生能量。在吸收塔温度(313.15 ~ 343.15 K)、汽提塔温度(373.15 ~ 403.15 K)、CO2分压(1 ~ 30 kPa)、汽提塔总压(200 ~ 400 kPa)、CO2回收率(80 ~ 95%)、胺混合比(PZ:3DMA1P, 0 ~ 10:40 ~ 30 wt.%)和水浓度(60 ~ 90 wt.%)等操作参数的影响下,对再生能进行了计算和评价。在相同的操作条件下,以30%和40% wt.%的单乙醇胺(MEA)和CESAR-1为基准溶剂,得到的结果进行了比较。目前对PZ和3DMA1P共混物的研究结果表明,与MEA和CESAR-1相比,溶剂体系具有更高的CO2吸收能力和更低的再生能量。再生能源的综合参数分析增强了结果在不同行业范围内的适用性。
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引用次数: 0
Perspectives on the status and future of sustainable CO2 conversion processes and their implementation 对可持续二氧化碳转化过程及其实施的现状和未来的看法
Pub Date : 2025-08-24 DOI: 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.
大气中二氧化碳(CO 2)浓度的快速上升继续威胁着全球气候的稳定,因此迫切需要可扩展的、经济上可行的和可持续的CO 2减缓战略。在新兴的解决方案中,二氧化碳转化技术提供了一种变革性的途径,使二氧化碳成为可再生的碳原料,用于生产燃料、化学品和材料,从而促进循环碳经济。本文首先探讨了基本的二氧化碳捕获和预处理方法,强调了先进的材料,以及直接将捕获与转化过程结合起来的集成策略,作为改善二氧化碳转化的门户。在CO₂转化技术的最新进展,跨越热化学,电化学,光化学和生物领域,然后涵盖。通过案例研究和商业化努力,探讨了二氧化碳转换系统与可再生能源和工业基础设施的整合,强调了全行业脱碳的机会。此外,还介绍了人工智能(AI)和机器学习(ML)在预测建模、催化剂设计和过程优化方面日益重要的作用,以及为这些技术的实际部署提供框架的技术经济分析。对能源效率、长期稳定性、产品选择性和监管约束等持续存在的挑战进行了批判性分析,并提出了新兴的解决方案。报告最后概述了未来的研究方向,包括下一代技术的发展以及促进跨学科合作和公私伙伴关系的战略。通过综合最新进展,确定关键障碍和机会,这项工作为加速全球部署二氧化碳转换技术,走向可持续和脱碳的未来提供了路线图。
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引用次数: 0
Artificial Intelligence Prediction of Carbonate Crystallinity of Carbon Mineralization 碳矿化碳酸盐结晶度的人工智能预测
Pub Date : 2025-08-24 DOI: 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.
碳捕获、利用和封存(CCUS)对实现碳中和的重要性日益得到认识。碳酸盐矿物是目前工业上利用碳矿化技术产生的大量含钙废物和矿物制造的。其中,用途广泛的碳酸钙,一般以三种晶体形式存在(水晶石、文石和方解石)。这三种晶型必须是自由可控的,以增加碳酸钙的价值和使用范围。在本研究中,改变了钙原料(即CaCl2)和碳原料(即K2CO3)在反应过程中的浓度、温度、pH、搅拌速度和搅拌时间等变量。此外,采用x射线衍射(XRD)图,通过Rietveld细化分析确定了相组成比。利用大量的实验数据,我们通过训练和评估多层感知器(MLP)、支持向量机(SVM)、随机森林(RF)和决策树(DT)算法,构建了数据驱动的预测模型。然后通过k-fold交叉验证选择最佳模型,以确定控制结晶度的最佳操作条件。这项研究提供了一个系统的全面知识,允许工业选择,制造和生产碳酸钙的晶体形式,他们需要。预计使用碳矿化技术(CCUS技术的一部分)将有助于碳中和,同时降低废物环境处理成本。
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引用次数: 0
Harnessing humidity for direct air capture: Moisture-swing sorbent design and mechanisms 利用湿度进行直接空气捕获:变湿吸附剂的设计和机制
Pub Date : 2025-08-24 DOI: 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.
由于天气和气候的不断恶化,使用液态和固态胺吸附剂的直接空气捕集(DAC)和燃烧后二氧化碳捕集(PCC)受到了极大的关注。提高二氧化碳捕获和去除技术的效率至关重要,其主要重点是减少连续捕获-释放循环的能源需求。低能耗CO2去除策略具有良好的耐久性和低运营成本,每吨CO2去除的低水平成本是大规模实施的首选。本综述重点介绍了低能耗的CO2去除方法,如湿/湿摆动吸附剂。讨论了结构和分子特性的影响,反阴离子对CO2去除效率和动力学的影响,不同操作因素对性能的影响,以及这些材料的长期稳定性。对这些材料和方法的不断探索和优化对于推进水分摇摆法,为全球应对气候变化和促进环境可持续性做出贡献至关重要。最后,对创新材料的设计提出了建议。
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引用次数: 0
Kinetic model describing the effect of amine loading and temperature on CO2 capture by solid amine adsorbent 描述胺负载和温度对固体胺吸附剂捕获CO2影响的动力学模型
Pub Date : 2025-08-20 DOI: 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.
大气中CO2浓度的增加导致了重大的生态变化,CO2排放的控制一直是世界各国关注的焦点。胺功能化吸附剂具有高的CO2吸附能力、适中的吸附热和较强的耐水性等优点,具有广阔的应用前景。吸附动力学是一个关键的性能参数,有利于微观CO2吸附过程的认识。提出了一种新的动力学模型,将固体胺吸附剂中的胺分为两个区域:开放胺区和封闭胺区。与开放胺区不同,封闭胺区对CO2的吸附受扩散的影响较大。该模型能较好地阐明胺的负载和温度对CO2吸附的影响。当胺负荷低于理论最大负荷时,随着胺负荷的增加,CO2吸附量和氮效率逐渐增加。然而,随着胺负荷的进一步增加,吸附量反而下降。固体胺对CO2的吸附不受外部扩散的影响,但受内部扩散的影响较大。高胺负荷吸附剂封闭胺区所占比例大,CO2需要缓慢扩散到该区域,导致低温下CO2吸附量小。当载胺量小于0.5时,CO2吸附率基本保持不变。该模型对定向制备快速吸附的固体胺吸附剂具有指导意义。
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引用次数: 0
Experimental investigation and techno-economic assessment of oilfield brine-derived carbonates for calcium looping CO2 capture 油田卤水碳酸盐捕集钙环CO2的实验研究及技术经济评价
Pub Date : 2025-08-19 DOI: 10.1016/j.ccst.2025.100489
Rufan Zhou , Chunqing Jiang , Rafal Gieleciak , Lava Kumar Pillari , Lukas Bichler
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。
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引用次数: 0
Experimental and numerical investigation of the morphological changes of a natural limestone-based CO2 sorbent over repeated carbonation-calcination cycles 天然石灰石基CO2吸附剂在重复碳化-煅烧循环中形态变化的实验和数值研究
Pub Date : 2025-08-19 DOI: 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.
天然石灰石基CO2吸附剂在CaO与CaCO3循环过渡过程中的形态变化影响其碳化速率和循环CO2吸收量。我们以前所未有的细节研究了Havelock灰岩在(I) 2-100 nm、(II) 200-3000 nm和(III) 3000 nm范围内碳酸化过程中孔隙结构的演化,并将形态变化与观测到的碳酸化速率联系起来。区域(I)的孔隙被CaCO3完全填充,CaO转化率为>; 60%(第1循环),导致吸附剂总表面积损失约90%,而区域(II)的孔隙仅被部分填充,而区域(III)的孔隙基本不受影响。在第1和第10个循环的碳化反应中,观察到的碳化速率随着吸附剂总表面积的减小而线性减小。在动力学和形态学模型的支持下,我们的发现挑战了广泛使用的CaCO3产物层的临界厚度限制CO2向CaO扩散的概念,这意味着一旦CaO表面完全被CaCO3晶体覆盖,反应就会受到扩散的限制。我们的研究结果进一步为设计高效的cao基吸附剂提供了一个视角,将其孔径调整到大于100 nm,这样孔隙体积(和相应的表面积)可以在循环过程中大量再生,从而产生高循环二氧化碳吸收率。
{"title":"Experimental and numerical investigation of the morphological changes of a natural limestone-based CO2 sorbent over repeated carbonation-calcination cycles","authors":"Maximilian Krödel,&nbsp;Dominic Spescha,&nbsp;Agnieszka Kierzkowska,&nbsp;Felix Donat,&nbsp;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) &gt; 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 &gt; 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 &gt; 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}
引用次数: 0
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Carbon Capture Science & Technology
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