Cost-Effective Carbon Dioxide Removal via CaO/Ca(OH)₂-Based Mineralization with Concurrent Recovery of Value-Added Calcite Nanoparticles

Abstract

The rapid rise in atmospheric CO₂ concentrations has intensified the need for scalable, sustainable, and economically viable carbon sequestration technologies. This study introduces a cost-effective CaO/Ca(OH)₂-based mineralization process that not only enables efficient CO₂ removal but also allows the simultaneous recovery of high-purity calcite nanoparticles as value-added products. The process involves hydrating CaO, followed by controlled carbonation under optimized CO₂ flow rates, temperature conditions, and and additive use, yielding nanocrystalline calcite with an average particle size of approximately 100 nm. Comprehensive characterization using X-ray diffraction, transmission electron microscopy, and energy-dispersive X-ray spectroscopy confirmed a polycrystalline structure with exceptional chemical purity (99.9%) and rhombohedral morphology. Techno-economic analysis further demonstrated that coupling CO₂ sequestration with nanoparticle production can markedly improve profitability, particularly when utilizing CaO/Ca(OH)₂-rich industrial residues such as steel slags or lime sludge as feedstock. This hybrid, multi-revenue strategy—integrating carbon credits, nanoparticle sales, and waste valorization—offers a scalable pathway aligned with circular economy principles, enhancing both environmental and economic performance. Moreover, the proposed system can be applied to CO₂-emitting plants and facilities, enabling not only effective carbon dioxide removal and the generation of carbon credits, but also the production of calcite nanoparticles for diverse applications in agriculture, manufacturing, and environmental remediation. These findings highlight the potential of CaO/Ca(OH)₂-based mineralization to evolve from a carbon management technology into a platform for advanced materials manufacturing, thereby contributing to global decarbonization efforts.

1. Introduction

The continuous rise in atmospheric CO₂ concentrations has amplified the global demand for scalable, sustainable, and cost-effective carbon sequestration technologies. Among various strategies, mineralization-based carbon sinks are gaining recognition as practical and long-term solutions for mitigating climate change impacts [1]. From a geological perspective, mineral carbonation—where CO₂ reacts with calcium- or magnesium-rich silicate and ultramafic rocks to form stable carbonate minerals—offers one of the most permanent sequestration pathways, with storage stability over millions of years [2]. In addition, in situ mineralization processes can be integrated with geothermal energy recovery, creating opportunities for co-benefits in both energy generation and carbon management [3]. Economic viability and operational efficiency remain decisive factors for global implementation of carbon capture systems. Methods that immobilize CO₂ in geologically secure forms while producing valuable by-products—such as construction-grade carbonates—can substantially enhance their feasibility [4].

Within mineral carbonation technologies, CaO/Ca(OH)₂-based mineralization has emerged as one of the most promising pathways for CO₂ sequestration, owing to its ability to permanently convert atmospheric or industrial CO₂ emissions into stable calcium carbonate minerals [5]. Unlike other capture techniques requiring costly storage infrastructure or energy-intensive regeneration cycles, CaO/Ca(OH)₂-based processes provide a direct, exothermic reaction pathway with strong thermodynamic favorability [5]. From a mineralogical standpoint, carbonation proceeds through nucleation and growth of crystalline phases—predominantly calcite, along with aragonite and vaterite—whose stability and morphology depend on parameters such as temperature, CO₂ partial pressure, and the presence of aqueous phases [2]. The resulting carbonates exhibit high crystallographic stability, ensuring permanence on geological timescales [1]. Microstructural studies also reveal that the formation of nano- to micro-sized calcite crystals not only enhances CO₂ sequestration efficiency but also yields materials with functional properties suited for high-value industrial applications [6].

Recent research highlights the dual benefits of CaO/Ca(OH)₂-based mineralization: efficient CO₂ capture and simultaneous production of high-value by-products. These systems demonstrate rapid carbonation kinetics, high CO₂ uptake efficiency, and compatibility with industrial waste streams (e.g., slags, fly ash), making them well-suited for large-scale deployment [7]. Furthermore, there is increasing interest in optimizing carbonation conditions to selectively synthesize nano-sized calcite particles with high surface area, tunable morphology, and chemical stability. Such properties enable diverse applications in biomedicine (e.g., drug delivery, bone tissue engineering), polymer and paper industries, coatings, and environmental remediation [8,9,10,11]. At the nanoscale, calcite offers superior dispersion, mechanical integration, and reactivity in composite materials, reducing reliance on costly synthetic fillers and improving commercial competitiveness [6,12].

Integrating calcite nanoparticle recovery into CaO/Ca(OH)₂-based mineralization represents a paradigm shift from waste-focused sequestration toward resource-oriented valorization. This approach aligns with circular economy principles, transforming CO₂ from an emission challenge into a feedstock for sustainable material production [1,13]. Against this backdrop, the present study seeks to develop a cost-effective and scalable CaO/Ca(OH)₂-based CO₂ sequestration process that achieves both efficient carbon capture and recovery of high-purity calcite nanoparticles. Specifically, the research aims to: (1) Optimize carbonation parameters—such as temperature, CO₂ flow rate, and CaO particle size—to maximize CO₂ fixation efficiency; (2) Characterize the physicochemical properties of calcite nanoparticles, including morphology, crystallinity, and surface area; (3) Assess the economic and application potential of recovered nanoparticles in industrial sectors. By coupling CO₂ sequestration with nanomaterial synthesis, this study aims to propose a sustainable and economically viable pathway for carbon management that contributes to climate change mitigation while enabling circular resource utilization.

2. Materials and Methods

2.1. Process Description for CO₂ Mineralization and Byproduct Valorization

The proposed system for carbon dioxide removal and by-product valorization employs a multi-stage CaO/Ca(OH)₂-based mineralization process designed to maximize CO₂ capture efficiency while enabling the synthesis of high-value calcium carbonate nanoparticles. The CaO used in this study was purchased from Sigma-Aldrich (≥98% purity, particle size < 75 μm). High-purity CO₂ gas (99.5%) was supplied by Linde Korea(Gyeonggi-do, Republic of Korea) and used without any further purification. The methodology integrates a sequence of physical and chemical unit operations to optimize reaction kinetics, control particle morphology, and ensure consistent product quality (Figure 1).

The process begins with the preparation of calcium oxide (CaO, quicklime), which may undergo preliminary crushing to achieve an optimal particle size distribution for rapid hydration and carbonation reactions. The prepared CaO is introduced into a mixing tank equipped with a mechanical agitator, where it is combined with water to form calcium hydroxide (Ca(OH)₂) slurry via an exothermic hydration reaction:

CaO + H₂O → Ca(OH)₂

(1)

The particle size and hydration conditions in this stage directly influence the surface area and reactivity of the resulting Ca(OH)₂. Following hydration, the slurry is transferred to a buffer tank for secondary agitation and pH stabilization. To facilitate the formation of uniform colloidal seed particles, an additive such as sodium glutamate, sugar, or a mixture is introduced at 0.1–2.0 parts by weight per 100 parts Ca(OH)₂. These additives act as crystal growth modifiers, influencing nucleation and controlling particle morphology at the nanoscale. This step also ensures complete hydration, thereby preparing the slurry for efficient CO₂ absorption. The conditioned slurry is pumped into a reaction chamber, where CO₂ gas is sparged through a gas ejector system. A controlled flow rate of 50–150 L/min per kg of Ca(OH)₂ promotes the formation of colloidal CaCO₃ seed particles with a cubic crystal habit and an average particle size of approximately 100 nm. Particle size and morphology can be adjusted by controlling the CO₂ flow rate and reaction time. The carbonation reaction proceeds as follows:

Ca(OH)₂ + CO₂ → CaCO₃ + H₂O

(2)

Direct gas–liquid contact ensures high mass transfer rates and rapid mineralization, resulting in high conversion efficiency. The aqueous CaCO₃ slurry produced in the reactor is collected in a storage tank and can be used directly in liquid form.

In this study, the carbonation reactor was a stainless-steel cylindrical vessel with an internal volume corresponding to a diameter of 1.5 m and a height of 2 m. For each experiment, 20 kg of Ca(OH)₂ slurry was prepared by hydrating CaO with deionized water to form a homogeneous suspension. Carbon dioxide was continuously injected through a gas ejector system at a controlled flow rate of 100 L·min⁻¹ per kilogram of Ca(OH)₂. The carbonation reaction was conducted for 6 h to achieve complete conversion, while pH and temperature were monitored throughout the process to track reaction progress. The slurry dehydration and drying processes were conducted at room temperature under ambient laboratory conditions, and no external heating was applied.

For applications requiring solid or semi-solid products, the slurry undergoes mechanical dewatering using a filtration unit to produce a gel-like paste. This paste is then dried—preferably using microwave-assisted drying to preserve particle morphology—resulting in granular solids. The dried material can be milled into a fine powder to meet the specifications of various industrial applications, such as polymer fillers, paper coatings, biomedical products, and advanced composite materials.

2.2. Characterization

Characterization of the synthesized nano-calcium carbonate was performed at the Mineralogy and Mineral Resources Laboratory, Department of Earth and Environmental Sciences, Chungbuk National University (CBNU), and the CBNU Central Instrumentation Facility. Powder X-ray diffraction (XRD) analysis was carried out using a Rigaku Miniflex 600 (Tokyo, Japan) powder X-ray diffractometer equipped with a Cu Kα radiation source (λ = 1.5406 Å) operated at 40 kV and 15 mA. Data were collected over the 2θ range of 5–80°, with a step size of 0.1° and a scan rate of 3°·min⁻¹ to ensure adequate peak resolution. Prior to measurement, the instrument was calibrated using a standard silicon reference material to correct systematic errors.

Morphological observations and elemental analyses were conducted using a JEOL JSM-IT510 (Tokyo, Japan) scanning electron microscope (SEM) operated at an accelerating voltage of 10–15 kV, under high-vacuum mode, and equipped with an Oxford Instruments (Abingdon, UK) energy-dispersive X-ray spectroscopy (EDS) system for qualitative and semi-quantitative elemental analysis. High-resolution imaging and structural analysis were conducted using a spherical aberration (Cs)-corrected transmission electron microscope (JEM-ARM200F, NEOARM; JEOL Ltd., Tokyo, Japan) operated at an accelerating voltage of 200 kV. Lattice-resolved images and Fast Fourier Transform (FFT) patterns were obtained to investigate the crystal structure at the nanoscale. TEM specimens were prepared by dispersing the powder sample in ethanol, followed by ultrasonication for 10 min to prevent particle agglomeration. A drop of the suspension was then deposited onto copper carbon lacey grids and dried under ambient conditions prior to analysis.

3. Results

3.1. Powder X-Ray Diffraction

XRD analysis was conducted to examine the phase composition, crystallinity, and structural characteristics of the synthesized calcium carbonate byproduct, with the objective of confirming the formation of the calcite polymorph. The diffraction pattern exhibited a series of sharp and intense peaks, characteristic of a well-ordered crystalline material (Figure 2). Peak positions and relative intensities showed complete agreement with reference data [14,15] for rhombohedral calcite (space group R$\overline{3}$c). Prominent reflections, including the (10$\overline{2}$), (104), (110), (1$\overline{2}$3), and (202) planes, were consistent with the standard pattern, indicating the exclusive presence of calcite. No diffraction signals attributable to alternative CaCO₃ polymorphs, such as aragonite or vaterite, were detected, confirming the high phase purity of the synthesized product. The nanocrystalline nature of the calcite was further confirmed by estimating the average crystallite size using the Scherrer Equation (3), applied to the full width at half maximum of the dominant reflections.

$$D=\mathrm{K}\mathsf{\lambda }/\mathsf{\beta }\mathrm{c}\mathrm{o}\mathrm{s}\mathsf{\theta }$$

(3)

where D is the crystallite size (nm), K is the shape factor (0.9), λ is the X-ray wavelength of the Cu Kα radiation (1.5406 Å), β is the full width at half maximum (FWHM) of the diffraction peak (radians), and θ is the Bragg diffraction angle (degrees). The calculated crystallite size was approximately 86 nm, indicating its nanocrystalline nature. The narrow and symmetric diffraction peaks also suggest minimal lattice strain and a uniform crystallite distribution. These results demonstrate that the synthesis process successfully produced a phase-pure nanocrystalline calcite without detectable secondary calcium carbonate polymorphs.

3.2. Transmission Electron Microscopy

To elucidate the morphology and size characteristics of the synthesized byproduct, a multi-modal electron microscopy approach was employed. Initial SEM imaging was insufficient to resolve individual primary particles due to nanoscale resolution limitations. Consequently, TEM was utilized to obtain high-resolution images, which revealed discrete nanoparticles exhibiting a well-defined rhombohedral habit (Figure 3a,b). This morphology is consistent with the rhombohedral crystal structure of calcite confirmed by XRD analysis. A statistical size analysis was conducted by measuring a total of 536 nanoparticles from TEM micrographs (Figure 3c). The particle size distribution, determined using a 10 nm bin width, ranged from 60 to 200 nm and exhibited a unimodal but positively skewed profile. The majority of particles fell within the 70–110 nm range, with a mean size of approximately 105 nm. The narrow, dominant peak indicates that the reaction conditions promoted stable, well-controlled nucleation and growth, while the extended right-hand tail suggests the presence of a minor population of larger particles, likely formed via partial irreversible agglomeration or Ostwald ripening. Such size distribution characteristics are critical, as particle size and monodispersity directly influence the functional performance of nanomaterials in applications such as catalysis, composite reinforcement, and optical systems. TEM coupled with EDS confirmed the high chemical purity of the nanoparticles, detecting only calcium, carbon, and oxygen, with no other elemental impurities (Figure 3d). The estimated purity of 99.9% is attributed to the use of high-grade CaO precursors in the synthesis. This compositional purity is a key requirement for high-value applications.

High-resolution TEM (HRTEM) imaging revealed well-defined lattice fringes, indicative of high local crystallinity (Figure 4). FFT analysis of the HRTEM images yielded diffraction spot patterns that were indexed to the rhombohedral calcite structure, showing excellent agreement with simulated electron diffraction patterns along major crystallographic orientations, including the b-axis and c-axis. Notably, HRTEM observations demonstrated that, particularly along the c-axis, the Ca-O coordination polyhedra at the boundaries of the a- and b-axes are in contact with a distinct lattice mismatch (Figure 5). This interfacial misfit is clearly manifested in the corresponding FFT patterns. Closer inspection revealed that the particles are nanocrystalline aggregates composed of multiple nanodomains with varied orientations, rather than single crystals. While each domain is a coherent crystalline unit, inter-domain misorientation restricts long-range order. The preserved rhombohedral morphology together with surface roughness, grain boundaries, and nanodomain arrangement suggests a non-classical growth pathway, likely via oriented attachment of primary nanocrystals.

4. Discussion

4.1. Process Control for Calcite Nanoparticle Formation

A central challenge—and a decisive success factor—in CaO/Ca(OH)₂-based CO₂ mineralization lies in achieving simultaneous optimization of carbon fixation efficiency and nanoparticle quality control [2]. The physicochemical attributes of the final calcite nanoparticles—particularly size, crystallinity, morphology, and purity—are highly sensitive to process parameters, all of which must be precisely tuned to deliver products suited for high-value applications [6,16]. From an economic perspective, the rationale for producing calcite nanoparticles rather than micron-scale calcite is compelling [16,17]. Micron-sized particles have limited market value and constrained applicability in advanced functional materials [18]. In contrast, nanoscale calcite offers markedly higher surface area, enhanced reactivity, and tunable optical properties, making it highly attractive for applications such as biomedical fillers, advanced composites, and photonic materials. By implementing well-designed process control strategies, it is possible not only to consistently produce nanoparticles but also to selectively tailor particle size distributions—enabling the targeted manufacture of specific size fractions to match diverse industrial requirements and thereby improving commercial viability.

Among the most critical operational parameters are reaction temperature, CO₂ gas injection rate, pH control, and CaO precursor characteristics (particle size, surface area, and purity). Elevated temperatures (>50 °C) can accelerate carbonation by enhancing reaction kinetics and decreasing CO₂ solubility in the aqueous phase [19]. However, such thermal conditions also promote uncontrolled crystal growth, leading to particle coarsening and a broader size distribution—undesirable for applications requiring monodispersity [20,21]. The CO₂ injection rate governs gas–liquid mass transfer efficiency and local supersaturation. As previously reported, high flow rates can significantly increase nucleation rates but may also cause localized pH gradients and rapid precipitation, resulting in amorphous or poorly crystalline phases and particle agglomeration. Excessively high injection rates can overwhelm the system’s buffering capacity, further amplifying variability in particle size and morphology [18,19,20]

pH control emerges as an equally important, yet often underemphasized, factor in nanoparticle synthesis. The saturation state of carbonate species and the stability of intermediate phases (e.g., amorphous calcium carbonate) are pH-dependent, directly influencing nucleation kinetics, crystal habit, and final particle size [22]. Maintaining a controlled pH window during carbonation—particularly in the range that stabilizes critical nuclei while suppressing rapid, uncontrolled precipitation—can yield narrower size distributions and higher monodispersity [23]. Conversely, uncontrolled pH fluctuations can trigger premature aggregation or phase transformations, undermining particle uniformity and functional performance [21,22].

The CaO precursor also plays a decisive role. Nanoscale CaO particles provide abundant reactive sites but are prone to early-stage agglomeration during hydration and carbonation, which can reduce dispersion quality [24,25]. Impurities or secondary mineral phases in the precursor can disrupt controlled nucleation and growth pathways. High-resolution TEM observations reveal that the synthesized calcite nanoparticles exhibit a polycrystalline structure, consistent with a non-classical crystallization pathway. Rather than forming solely through stepwise monomer addition, the particles appear to develop via oriented attachment (OA) of primary nanocrystalline domains, followed by Ostwald ripening—where larger, more stable particles grow at the expense of smaller ones. These mechanisms, widely recognized in biomineralization and synthetic systems, are governed by the interplay of kinetic and thermodynamic factors that dictate phase selection, particle aggregation, and morphological evolution [26,27].

In prolonged reactions or under sustained CO₂ saturation, OA-driven growth and secondary ripening are more pronounced, often producing irregular aggregates and broader size distributions [27]. Thus, integrated control—combining CO₂ dosing profiles, temperature management, pH stabilization, and the use of crystal growth modifiers—is essential to suppress undesirable growth pathways. Additives such as sugar derivatives or amino acids can selectively inhibit particle fusion and regulate crystal habits, further enhancing monodispersity and functional performance. The economic imperative for producing calcite nanoparticles, combined with the ability to precisely tune particle size Via temperature, CO₂ flow, pH, and precursor engineering, underscores the importance of mastering both classical and non-classical growth mechanisms (

Table 1. Key process parameters influencing CaCO₃ nanoparticle synthesis, including their primary roles, optimal operating conditions, and potential adverse effects when deviated from the optimal range.

Parameter	Primary Influence	Optimal Condition	Potential Negative Effects
Reaction temperature	Controls carbonation kinetics & CO2 solubility; affects nucleation rate	30–50 °C → balanced kinetics & controlled crystal growth	High T → uncontrolled growth and particle coarsening; Low T→ slow reaction
CO2 injection rate	Governs gas–liquid mass transfer & local supersaturation	Moderate flow → efficient nucleation without uncontrolled precipitation	High rate → pH gradients, amorphous phases, agglomeration
pH control	Regulates carbonate speciation & stability of intermediate phases	pH 8.5–9.5 → stabilizes nuclei & controls growth	Large pH swings → premature aggregation, phase transformation
CaO precursor characteristics	Determines reactive surface area & nucleation sites	Fine particle size, high surface area, high purity	Impurities → disrupt nucleation; ultrafine particles→ prone to early agglomeration

). Such process mastery not only enhances product performance in high-end applications but also enables the creation of market-differentiated nanoparticle products with optimized size, purity, and functionality, thereby bridging carbon capture with advanced materials manufacturing [24].

4.2. Characteristics and High-Value Application Potential of Synthesized Calcite Nanoparticles

The calcite nanoparticles synthesized in this process—averaging approximately 100 nm in size—are not merely a medium for CO₂ storage, but constitute a high-value product in their own right. At this scale, calcite exhibits physicochemical characteristics that fundamentally distinguish it from bulk calcium carbonate, including a high specific surface area, uniform rhombohedral morphology, and intrinsic biocompatibility [28]. These attributes confer enhanced reactivity, excellent dispersibility, and superior interfacial performance, making nanoscale calcite highly sought after in a range of high-performance industrial and biomedical applications [29,30].

In the biomedical sector, approximately 100 nm calcite particles have been investigated as core materials for drug delivery, gene transfection, and bone tissue engineering [9,11,31]. Their pH-responsive solubility in acidic microenvironments—such as those present in tumor tissues—enables controlled and targeted therapeutic release [32]. Furthermore, their crystallographic and chemical similarity to natural bone minerals promotes osteogenic activity and biointegration when incorporated into orthopedic scaffolds [9]. In the polymer and composite industries, calcite nanoparticles serve as a highly efficient functional filler, significantly improving tensile strength, impact resistance, and thermal stability [6,17]. Due to their nanoscale dimensions and superior dispersion, these particles can achieve equivalent or greater performance enhancements at much lower loadings compared to conventional micron-sized fillers. This yields a favorable cost-to-performance ratio, making them advantageous for demanding sectors such as automotive components, high-barrier packaging films, and biodegradable plastics [6].

The 100 nm calcite nanoparticles produced in this study—characterized by confirmed phase purity, high crystallinity, and minimal agglomeration—align closely with the stringent specifications of these high-value markets. Moreover, the process developed here offers flexibility in tuning particle size and morphology to match specific market demands. By adjusting process parameters such as temperature, CO₂ injection rate, pH, and additive type, it is feasible to produce tailored morphologies, including whisker-shaped calcite nanoparticles (Table 1). Such whisker-type particles have already been demonstrated as high-performance fillers in specialty paper manufacturing, enhancing mechanical strength, opacity, and printability [33]. This adaptability indicates that the present method can be extended beyond calcite nanoparticles to produce application-specific morphologies, further broadening its industrial applicability and market potential [31,33].

4.3. Integrated Techno-Economic Assessment: Building a Multi-Revenue Model

Theoretically, 1 kg of CaO can capture up to 784.77 g of CO₂, corresponding to a stoichiometric CO₂ uptake capacity of approximately 78.5%, indicating high sequestration potential [24]. However, when assessed solely on the basis of carbon credit revenues, the economic feasibility remains limited. Industrial-grade CaO costs approximately $0.15 per kg, while the average market value of CO₂ credits—depending on regional pricing—translates to only $0.039–$0.078 per kg of CaO reacted [34]. This disparity indicates that a model relying solely on carbon credits is insufficient to achieve profitability, especially when operational costs for CO₂ capture, slurry preparation, and post-processing are taken into account (Figure 6).

A viable solution lies in the co-recovery and commercialization of high-value calcite nanoparticles as a additional revenue stream. Conventional bulk CaCO₃ sells for only $30–$80 per ton, whereas high-purity nano-calcite—particularly in the 50–200 nm range—can command $300 to >$1000 per ton, depending on morphological uniformity, surface properties, and application sector [34,35]. Given that 1 kg of CaO yields approximately 1.78 kg of CaCO₃, and assuming 60–70% recovery as nano-grade material, revenues from material sales alone could exceed raw material and processing costs substantially—effectively transforming the process from a cost center into a net revenue generator.

Further economic and environmental benefits can be realized by substituting commercial CaO with CaO-rich industrial residues, such as lime sludge from water treatment plants, demolished concrete fines, or steelmaking slags [13,18]. This substitution not only reduces feedstock costs to near zero but also eliminates the environmental burden of quarrying and calcining limestone, while diverting alkaline wastes from landfills—thereby achieving waste valorization and aligning with circular economy principles. Moreover, many waste-derived CaO sources exhibit high reactivity due to their fine particle size and elevated surface area, potentially enhancing carbonation kinetics [36].

From a techno-economic standpoint (Figure 6), integrating these strategies yields a multi-revenue business model with three primary income streams: (1) CO₂ sequestration credits—monetizing verified emission reductions; (2) production and sale of high-margin calcite nanoparticles for premium markets in biomedicine, polymers, and coatings; (3) valorization of CaO/Ca(OH)₂-bearing industrial residues—generating added value from materials that would otherwise be disposal liabilities. This integrated approach not only strengthens process economics but also enhances the life-cycle sustainability profile of CaO/Ca(OH)₂-based mineralization technologies [19]. By coupling carbon mitigation with advanced material manufacturing, the system achieves higher returns on investment, greater scalability, and stronger alignment with global decarbonization and resource efficiency objectives [36].

5. Conclusions

This study demonstrates that CaO/Ca(OH)₂-based CO₂ mineralization, when integrated with the concurrent recovery of high-purity calcite nanoparticles, can transform from a conventional carbon capture strategy into a value-generating, resource-oriented industrial process with added economic value. Under optimized reaction conditions, the process yielded calcite nanoparticles with an average size of about 100 nm, high crystallinity, phase purity, and minimal agglomeration—properties that align with the stringent specifications required in advanced applications such as biomedicine, polymer composites, and specialty coatings. From an economic perspective, a model relying solely on carbon credits is insufficient to offset raw material and processing costs. In contrast, incorporating the sale of high-margin nano-calcite—priced significantly above bulk calcium carbonate—enables the process to achieve profitability. Additional gains can be realized by replacing commercial CaO with CaO-rich industrial residues, thereby lowering raw material costs, reducing waste disposal burdens, and advancing circular economy objectives. Techno-economic analysis confirms that a multi-revenue model—combining (1) CO₂ sequestration credits, (2) high-value nano-calcite sales, and (3) valorization of CaO-bearing industrial residues—substantially improves both profitability and sustainability. This integrated approach not only addresses the urgent need for scalable, cost-effective carbon removal but also contributes to the production of next-generation functional materials, positioning CaO/Ca(OH)₂-based mineralization as a strategic platform technology for climate change mitigation and sustainable manufacturing. Moreover, the proposed system can be readily applied to CO₂-emitting plants and industrial facilities, providing an effective pathway for large-scale carbon dioxide removal. In addition to generating carbon credits, the process enables the concurrent production of calcite nanoparticles as a value-added product. These nanoparticles hold broad application potential across agriculture, manufacturing, and environmental remediation, thereby extending both the economic and societal benefits of the technology.

Future work should focus on refining process control strategies to tailor particle size, morphology, and surface chemistry to meet specific market requirements, as well as conduct long-term pilot-scale demonstrations to validate economic performance under real industrial conditions. Nanominerals exhibit diverse characteristics depending on their size, and we plan to further investigate these aspects in future work [30]. In addition, owing to their extremely small particle dimensions, we intend to conduct more detailed analyses using synchrotron radiation techniques and high-resolution TEM to gain deeper insights into their structural and morphological features [37]. With these advancements, CaO/Ca(OH)₂-based CO₂ mineralization has the potential to become a pivotal component of global decarbonization strategies, delivering tangible economic, environmental, and technological co-benefits.