Currently, existing technologies are not yet able to fully address CO₂ emissions, despite significant progress in assessing the feasibility of implementing CCS onboard ships. These systems are designed to capture a significant percentage of CO₂ emitted from fuel combustion thereby mitigating emissions into the atmosphere.

However, current research literature highlights technologies that require the CO₂ liquefaction, onboard storage, and its disposal in ports, posing various challenges as outlined below (Visonà et al., 2024; Sridhar et al., 2024; Hua et al., 2023). In this context, the authors explore an alternative CCS tailored for onboard application, distinct from commonly encountered systems. This system, which eliminates the need for liquefaction and onboard storage, not only overcomes existing challenges but also offers additional advantages.

In fact, this approach signifies a concrete commitment to reducing emissions but also underscores the increasing awareness and urgency surrounding the imperative challenge of achieving decarbonization by 2050.

The amount of reduction achievable with CCS depends on their efficiency, expressed in %, as outlined in Equation 1 (Taipabu et al., 2023).

where CO₂, in represents the total quantity of CO₂ entering the system in a gaseous state, and CO₂, out denotes the amount exiting the system after treatment, also in a gaseous state.

Based on the preliminary studies conducted by the authors (Bortuzzo et al., 2023), achieving a CCS efficiency of 25% appears feasible through retrofitting without compromising onboard space. While higher percentage of CO₂ reductions could be achievable, especially through retrofit approaches involving reallocating space for larger CCS at the expense of other functions like cargo storage, opting for a 25% reduction aims to sidestep the necessity of compromising onboard space and to streamline the retrofit procedure.

Various CCS proposals are currently under research, including those examined by the authors (Bortuzzo et al., 2023), defined as post-combustion systems. These systems intervene after the engine combustion process, focusing on exhaust gas treatment to reduce CO₂ emissions. The technologies explored include:

Following the investigation conducted on the operation of the aforementioned CCS, it has been observed that the output post-CO₂ treatment in the MCFC and Amine systems poses challenges concerning onboard liquefaction of CO₂ and subsequent discharge in ports. These challenges give rise to concerns regarding environmental impact and the development of suitable disposal methods.

The imperative need for an adequate storage facility in ports, capable of maintaining CO₂ in liquid form, necessitates pressurization and freezing systems. Additionally, a robust infrastructure for the secure and reliable transportation of CO₂ is indispensable. Therefore, a well-organized network of pipelines should be instituted to facilitate the conveyance of stored CO₂ from ports to industries or for confinement within geological sites. For shorter distances and smaller quantities, alternative means such as truck or train transport can also be considered (Chen and Morosuk, 2021). It is noteworthy that the transportation of CO₂ requires special attention due to the high pressures and extremely low temperatures involved (International Energy Agency, 2020). The selection of transportation mode is influenced by economic considerations and regulatory frameworks, significantly affecting the decision-making process.

CO₂ could find different applications across various products and services, including direct utilization without chemical alteration and its conversion into valuable products. Presently, approximately 230 million tons of CO₂ are utilized globally each year (International Energy Agency, 2020), predominantly in the fertilizer and oil and gas industries. Emerging technologies present opportunities to exploit CO₂ in sectors such as fuels, chemicals, and construction materials. However, the full realization of these possibilities depends on political support and the reduction of energy costs.

An additional alternative involves the storage of CO₂ by injecting it into a deep underground geological reservoir comprising porous rocks covered by an impermeable layer, sealing the reservoir to prevent CO₂ migration upward and dispersion into the atmosphere. Various types of reservoirs are suitable, including deep saline formations and depleted oil and gas reservoirs with greater capacity. When CO₂ is injected into a reservoir, it spreads through it, occupying porous spaces. Typically, the gas is pre-compressed to increase density and convert it into a liquid state. The reservoir must be at a depth exceeding 800 meters to maintain CO₂ in a dense liquid state (Chen and Morosuk, 2021).

The overall technical capacity for underground CO₂ storage worldwide is uncertain, especially for saline formations where further site characterization and exploration are needed but potentially vast. The total global storage capacity has been estimated between 8,000 and 55,000 gigatons (Gt) (International Energy Agency, 2020). Moreover, the existing offshore potential is substantial, particularly within 300 km from the coast and depths less than 300 meters, with an estimated capacity spanning from 2,000 to 13,000 Gt.

However, it becomes evident that transferring CO₂ to the storage site requires additional energy, leading to increased pollutant emissions associated with this operation, alongside the environmental concerns already highlighted. Moreover, the investments required to develop CO₂ confinement infrastructures demand significant resources, including those allocated for economic studies conducted by governments and stakeholders in the maritime and other relevant sectors.

Due to the problems highlighted above, the CCSs based on molten carbonate fuel cells and amine present a difficult implementation on-board ship and may not give origin to effective carbon capture in terms of reduced pollutant emissions.

On the other hand, the third CCS under consideration, involving Calcium Hydroxide, has the advantage of not encountering the challenge of CO₂ liquefaction and thus avoids the aforementioned consequences. This system presents potential environmental benefits, which will be examined by the authors in the subsequent section.

The operational principle of a CCS utilizing the Calcium Hydroxide is represented in Figure 3 .

Specifically, the engine exhaust gas treatment unit is where exhaust gases are directed into an SO_X scrubber. These gases then undergo a process where 25% are diverted to the CCS unit while the remainder is released into the funnel and into the atmosphere. Once the gases reach the CCS unit, they undergo a process outlined in the following steps (Bortuzzo et al., 2023):

1. initially, a quantity of calcium oxide (CaO), also known as quicklime, which is found in a solid state as a very fine powder, is extracted from a dedicated tank and reacted with H₂O to form calcium hydroxide (Ca(OH)₂):

This reaction occurs at specific temperatures that determine the purity of the produced Ca(OH)₂. Studies indicate that the optimal temperature for the carbonation of Ca(OH)₂ is approximately 200°C (Costagliola et al., 2022), ensuring better performance in absorbing CO₂ in the subsequent reaction. The H₂O used in this process is the same as that utilized in the SO_X scrubber system.

2. Secondly, Ca(OH)₂ is transferred to the designated scrubber for carbonation with CO₂. Exhaust gases, including CO₂, from the onboard engines are directed into this scrubber, and together with Ca(OH)₂, they enable the capture of CO₂ present in the gas stream. The product of carbonation is an inert inorganic compound, a suspension of CaCO₃, which is a primary constituent of mollusk shells, along with water as a byproduct.

The choice to use slaking with Ca(OH)₂ in onboard carbon capture systems, rather than direct injection of stack emissions into a CaO fluidized bed, involves several technical considerations. Slaking CaO to form Ca(OH)₂ increases the surface area and reactivity of the sorbent, enhancing the capture efficiency of CO₂ compared to using CaO directly (Ge et al., 2022). Additionally, the slaking process occurs at lower temperatures, which can be easier to manage onboard ships. Direct injection into a CaO fluidized bed requires maintaining high temperatures (around 650°C for carbonation and 950°C for calcination), which can be challenging in the variable conditions at sea. Using Ca(OH)₂ also allows for more flexible operation, as the slaked lime can be stored and used as needed, whereas maintaining a fluidized bed requires continuous operation and precise control of gas flow and temperature (Valverde, 2018). However, the effectiveness of capturing CO₂ can be influenced by temperature fluctuations, kinetics of the reactions, and impurities (Morse and Mackenzie, 1990; Zeebe and Wolf-Gladrow, 2001). Impurities like SO_X and NO_X can form stable compounds with calcium-based sorbents, decreasing their availability for CO₂ capture and creating unwanted by-products (Lerman and Mackenzie, 2018). To mitigate the impact of impurities, the engine’s exhaust gas treatment unit includes an SOx scrubber capable of achieving a 98% reduction in sulfur oxides, placed upstream of the CO₂ scrubber (Bortuzzo et al., 2024). As for NOx emissions, the lower combustion temperatures of a 2-stroke engine typically used onboard cargo ships minimize the risk of NOx interference with the CO₂ scrubber, which is why the supplier does not include a Selective Catalytic Reduction (SCR) unit in the design. However, for other engine types where NOx emissions could pose a challenge, incorporating an SCR unit could be considered a viable solution to reduce NOx levels. These practices ensure that the CaCO₃ formed is not impure and can potentially be discharged into the sea without causing pollution. In addition, reaction kinetics are affected by factors such as particle size, gas flow rates, and the partial pressure of CO₂. Smaller particle sizes increase the surface area for reactions, enhancing capture efficiency, but maintaining optimal conditions for these variables can be challenging onboard ships. Stable operation of fluidized bed reactors is essential because variations in gas flow rates and temperature can lead to channeling or particle agglomeration, which reduces process efficiency (Zeebe and Wolf-Gladrow, 2001).

The CaCO₃ obtained can be managed in two ways:

In the first scenario, a dedicated tank could be installed onboard for collecting CaCO₃, which could then be disposed at ports for potential resale, thus creating a circular economy.

Indeed, the system described relies on CaO, which is stored on board in a dedicated tank. The production of CaO is attained through a process known as calcination. This essential thermochemical process consists in:

Therefore, in this context, the initial step regarding raw material procurement could potentially change, considering the possibility of establishing circularity of the CaCO₃ produced onboard the vessel through CCS with the producers of CaO, rather than sourcing it from quarries or limestone mines.

In the second scenario, releasing CaCO₃ directly overboard, into the sea water, could potentially mitigate the increase in water acidity. In recent years, studies conducted on marine ecosystems have highlighted the repercussions of increased CO₂ on the marine environment, leading to a phenomenon known as acidification (Hönisch et al., 2012). This process is caused by the absorption of atmospheric CO₂ into seawater, where it reacts to form carbonic acid, thereby reducing the water’s pH. Marine acidification poses a serious threat to marine ecosystems, jeopardizing the survival of organisms such as corals and numerous fish species, as it can impede the formation of CaCO₃ shells and other skeletal structures.

In this framework, the direct discharge of CaCO₃ suspension, into water not only addresses pollution emission problems but also offers potential benefits, as it could help counteract the effects of ocean acidification, thus supporting marine ecosystems (Zhang et al., 2023). Some marine organisms can benefit from this process, as CaCO₃ is utilized by many species to form and strengthen their shells or skeletons. This shell-building process involves the conversion of calcium carbonate into a solid structure through biological reactions (Rau, 2011). According to (Dupont and Pörtner, 2013), ocean acidification has already started and has the potential to significantly impact marine ecosystems. However, it is also essential to investigate how entire ecosystems will respond to acidification over long timescales.

(Rau and Caldeira, 1999) suggested a comparable approach where dissolving CaCO₃ in seawater mixed with CO₂ from industrial flue gases could increase ocean alkalinity. However, a significant drawback of this approach is the large volume of seawater needed, with thousands of tons required for each ton of CO₂ captured (Renforth and Henderson, 2017). Additionally, there is a need for careful management of ocean alkalinity enhancement processes to maximize CO₂ removal while minimizing unintended environmental impacts. For instance, as highlighted by (Moras et al., 2024), smaller grain sizes of Mg(OH)₂ dissolve more quickly but also promote faster CaCO₃ precipitation, which can reduce CO₂ capture efficiency by causing CO₂ outgassing.

Overall, implementing a CCS onboard a ship using calcium hydroxide involves the release of several tons of calcium carbonate in the form of suspension into the ocean. CaCO₃ as a suspension form, poses no identified hazards. According to the IBC Code for bulk transport, it is classified as OS, and as Group C under the IMSBC Code for solid bulk transport. Since it is not listed among the prohibited wastes in Annex I and II of the London Convention, the disposal of a suspension of CaCO₃ in the sea could be considered analogous to geological CO₂ storage, resulting in an inert, non-toxic inorganic substance either suspended or deposited on the seabed. This could potentially be allowed based on the assessment outlined in Annex III of the same convention (RINA, 2023).

Once dispersed in the sea, CaCO₃ suspension dissolves, helping to reduce water acidity (Harvey, 2008). The dissolution reaction is:

Currently, there are already practices of releasing CaCO₃, for example, in various locations in the deep ocean, like in the northern Atlantic and near the Southern Ocean, where deep waters are rich in anthropogenic CO₂ (Sulpis et al., 2021). Furthermore, CaCO₃ dissolves more efficiently in water under higher pressure and lower temperature conditions and these factors vary considerably with the season and location in the surface layers (Caserini et al., 2021b).

Therefore, excluding some special restrictions that might be enforced in port or coastal areas, it can be reasonably expected that releasing CaCO₃ into sea during navigation will be permitted or even incentivized by international bodies.

In summary, while innovative CCS solutions for onboard vessel applications are still under research, the use of calcium hydroxide for CO₂ capture shows promise. This system avoids challenges like CO₂ liquefaction and offers environmental benefits, including potential contributions to mitigating ocean acidification, while also addressing logistical and operational concerns for maritime emissions reduction.

Given the absolute novelty of CCS with Calcium Hydroxide to be installed onboard a ship, its effective implementation is jeopardized by the lack of technical data coming from an actual case study. For such reason, the authors aim to provide a sound methodology that can allow sizing the system based on the chemical reactions, in order also to provide some reference data potentially useful for further technology developments.

The analyzed CCS is governed by the reaction Equations 2 and 3. To determine the quantities of CaO required for onboard storage on the vessel and thereby reduce CO₂ emissions, a stoichiometric approach is utilized.

Equation 3 presents the stoichiometric ratio of the reactants as 1:1, indicating that the reactants act in equivalent molar quantities. By determining the amount of CO₂ to be captured by the CCS, the number of moles of CO₂ ( n C O 2 ) can be calculated using the following equation:

where m C O 2 is the amount of CO₂ (g/s), and P M C O 2 is the molecular weight of CO₂ (g/mol).

Subsequently, the number of moles of calcium carbonate ( n C a C O 3 ) and calcium hydroxide ( n C a ( O H ) 2 ) are calculated based on 1:1 stoichiometric ratio. The amount of calcium hydroxide ( m C a ( O H ) 2   ) and calcium carbonate ( m C a C O 3 ) are calculated:

Following the same procedure, the amount of CaO ( m C a O ) and H₂O ( m H 2 O ) is determined starting from Equation 2. Since the reaction between CaO and H₂O has a 1:1 stoichiometric ratio, the same number of moles calculated for CaO can be used to determine the amount of H₂O used.

The values of the molecular weights (PM) for each reagent type are reported in Table 1 .

Based on previous considerations, the process developed by the authors to perform the sizing of a Calcium Hydroxide based CCS for an existing vessel is outlined in the following.

Firstly, it is imperative to consider the main characteristics of the vessel upon which the system is to be sized in order to identify available space and physical constraints for the installation of CCS. These characteristics include Deadweight tonnage (DWT), Length overall, Breadth, Depth, Draft, Main Engine and Auxiliary Engine specifications.

Secondly, the routes undertaken by the vessel have to be examined and the one necessitating the longest duration of navigation under loaded conditions should be selected. This ensures that the CCS is appropriately sized to effectively manage the most demanding voyage in terms of operation time of the CCS, thus assuring continuous capture of CO₂ emitted by the vessels during its operations.

Based on the chosen route and real data extrapolated from the vessel under consideration, the total voyage distance in nm, the vessel average speed in kts and the total days of navigation (days), must be collected. following parameters must be collected.

With the aim of estimating the quantities of the elements required for the CCS with Calcium Hydroxide to react with CO₂ and prevent its release into the atmosphere, the starting point is to understand the amount of CO₂ that needs to be treated.

To accurately determine the system’s size, it’s crucial to calculate the CO₂ emissions for the chosen voyage.

Based on total days of navigation and the vessel engine specifications at the selected average speed the daily fuel consumption (Cg), in tons/day, must be calculated as the sum of main engine fuel consumption (Cg_ME) and auxiliary engines fuel consumption (Cg_AE).

where SFOC is the Specific Fuel Oil Consumption in g/kWh and P_D is the delivered power in kW, for both Main Engine (ME) and Auxiliary Engines (AE), respectively.

From Cg, the Total Fuel Consumption for the selected voyage (Cg_TOT) can be derived and the total CO₂ produced during the selected voyage (CO_2Voyage) is calculated:

where C_F is the Carbon Factor of the fuel in tonsCO₂/tonsFuel.

From the CO_2Voyage the CO₂ flow rate production ( C O 2 Flow ), in g/s, can be calculated, along with the CO₂ flow rate captured by CCS system, in g/s ( CCS CO 2 Flow ).

The methodology described in Section 3.2 is applied to calculate, as a flow rate (g/s), the quantities of products necessary to achieve the desired % reduction in CO₂ emissions compared to the capture plant’s efficiency assessing the information as Ca ( OH ) 2 Flow , CaC O 3 Flow , CaO Flow , H 2 O Flow .

These results can be correlated with the number of navigation days of the ship along the selected route to obtain the quantities of products, in tons, required for the selected voyage.

Given the quantities of CaO essential for CO₂ capture during navigation, the volumes of reactants required on board the ship can be calculated. The estimation of the volume containing the necessary amounts of reactants can be accomplished using the Equation 22:

Where ρ represents the density for each reagent, defined as:

Total volume of CaO, H₂O and CaCO₃, that need to be stored onboard can be calculated.

Having established all the requisite quantities and volumes of substances essential for the operation of the CCS on board, the assessment of system installation can be conducted.

To underline the major advantages of the developed methodology, it outlines a stoichiometric approach for sizing a Calcium Hydroxide-based CCS for ships, determining the necessary quantities of reactants and assessing the feasibility of onboard installation based on vessel characteristics, voyage data, and emission calculations.

Analyzing the available records, the most demanding voyage is the route from Ruwais (Abu Dhabi, UAE) and reaching the terminal in Rio de Janeiro (Brazil) ( Figure 5 ). Hence, this route has been selected to size the CSS.

Based on real data extrapolated from the ship’s case study, Table 4 presents the voyage characteristics.

A mentioned, initial research suggests that CCS could achieve a carbon capture efficiency (%) leading to a 25% reduction in CO₂ emissions (Bortuzzo et al., 2023). This value has been assumed to further proceed.

The calculation of the CO₂ produced in the selected voyage is conducted as reported in Table 5 .

The quantities of reagents, necessary to achieve a 25% reduction in carbon dioxide emissions compared to the capture plant’s efficiency are calculated and reported in Table 6 .

These results are correlated with the number of navigation days of the vessel along the selected route as reported in Table 7 .

The volume containing the necessary amounts of reactants are calculated considering an allowance of approximately 2% and reported in Table 8 .

Having all the requisite quantities and volumes of substances to operate the CCS on board, the authors proceeded to conduct an assessment of its installation.

Two lime (CaO) tanks were positioned on the main deck in a location where they do not potentially interfere with loading and unloading operations. However, the presence of a centrally located crane restricts the placement of the lime tanks further forward due to the maneuvering space required by the crane arm. The decision to install only two tanks onboard was made to expedite lime loading operations that could occur in port. Additionally, the choice was made not to incorporate tanks inside the ship from the early design stages, as this would have necessitated numerous modifications to the ship’s compartments, making the refitting complex and economically unsustainable.

Each tank’s characteristics are detailed as follows and depicted in Figure 6A : length equals to 15.9 m, width equals to 6 m, height equals to 3.5 and total capacity of 520 tons.

The total volume of CaO required to operate the system in order to capture 25% of CO₂ produced during the selected voyage, which is the most demanding undertaken by the vessel, is quantified at 318 m³. This indicates that with this quantity, the ship will be able to undertake almost all other voyages, whose voyage length is less than one considered.

The height of 3.5 meters includes the support structure of the tanks and allows for sufficient space to enable a sloped configuration at the bottom of the tank, optimizing lime flow downwards through gravitational effects. Given the considerable length of the tanks, it is advisable to install a longitudinal bulkhead to limit load oscillations during rolling. Since CaO is a hygroscopic substance, the tanks housing must be equipped with insulation and a ventilation system to ensure a dry and well-ventilated internal environment.

The transfer of lime from the tanks to the CCS is managed through a system of volumetric pumps, with lime flow pipelines that can be positioned along the main deck.

The connection between the exhaust gas collector and the CCS is made through a duct originating from the ship’s funnel. To facilitate the transfer of exhaust gases from the duct inside the funnel to the one of CCS, an exhaust gas fan is installed, positioned downstream of the SO_X scrubber. This arrangement ensures that the exhaust gas that flows into the carbon capture unit is free of sulfur and nitrogen oxides.

Within the necessary refitting operation to install the CCS, it enables the accommodation of all required machinery without substantial alteration to existing spaces on board the ship. The structure of the system extends approximately three superstructure decks in height and is supported by beams positioned on the main deck ( Figure 6 ).

Additionally, the installation and operation of the CCS must consider the harsh marine environment, where factors such as humidity and salt exposure can accelerate corrosion and material degradation, affecting the system’s durability. To ensure long-term performance and reliable operation, insights from marine scrubber systems emphasize the importance of using durable, corrosion-resistant materials that can withstand high operational temperatures and energy demands. Regular maintenance is essential to maintain efficiency and address impurity buildup over time.

The main results are summed up as a 25% reduction in CO₂ emissions achievable for the selected demanding voyage between Ruwais (UAE) and Rio de Janeiro (Brazil). The necessary reagents, system components, and tank design have been optimized for this reduction, ensuring system feasibility without substantial modifications to the ship. The installation plan takes into account operational constraints, including space limitations and environmental conditions, while maintaining durability and efficiency in a marine setting.

The feasibility study on the implementation of a CCS using Calcium Hydroxide onboard the real case-ship has demonstrated that its components and the subsequent impact of their installation do not require complex procedures. Therefore, it is feasible to implement such systems even on older vessels, which may emit more pollutants compared to new buildings, without necessitating extensive modifications. Particularly noteworthy is the fact that there is no need to sacrifice space intended for cargo or other purposes, making retrofitting achievable within a short timeframe without significant structural alterations.

Regarding the stability of the vessel with the implementation of CCS onboard, future assessments will be essential, especially if the realistic implementation of this system on ships is considered. However, preliminary stability studies on vessels with different CCS implementations indicate that stability remains within acceptable limits with the original design (MMMCZCS, 2022). For the specific CCS under consideration, the additional installation of CaO tanks must be evaluated not only for its impact on overall stability but also from a structural perspective. It is important to assess the integration of the hull’s longitudinal strength and verify the support elements for the CaO tanks to prevent adverse effects on the vessel’s stability and safety. The CaO tanks should also undergo certification to ensure compliance with safety and security guidelines, given the material’s potential to cause hazardous reactions.

As evidenced by the case study, the system would be capable of reducing CO₂ emissions from a ship’s voyage by approximately 25%. Given that the system has been sized for the most demanding voyage, it highlights the potential for emissions reduction across all voyages undertaken by the vessel. This undoubtedly offers significant and immediate benefits in addressing the global emissions challenge faced by the maritime sector.

In this study, no storage tank for the product discharged from the CCS, namely CaCO₃, was designed onboard. This decision not only saved additional space onboard but also adopted a more environmentally sustainable approach by directly discharging the CaCO₃ product overboard, mitigating ocean acidification.

Taking into account the potential adoption of this system throughout the global merchant fleet, which, as per the study conducted at the close of March 2022 (https://www.atlas-mag.net/en/category/tags/focus/the-world-merchant-fleet), encompasses approximately 57,000 merchant ships navigating voyages worldwide, the profound implications of this innovation cannot be overlooked. Even if only a portion of these vessels were to integrate this technology, the resultant production of CaCO₃ could yield a dual benefit: mitigating CO₂ emissions and promoting the health of our oceans and marine life.

However, this does not preclude the possibility of considering future onboard CaCO₃ storage tanks, whether it involves all the produced CaCO₃ or just a portion that is not discharged overboard. This substance could be disposed of in ports, to initiate a circular economy. This approach would necessitate the development of a green transport network for product distribution from the port to the utilization industry. This consideration applies even if other CCS, which require the discharge of liquefied CO₂ into ports, were to be implemented.

Being the CaCO₃ the substance from which CaO is produced, and the CaCO₃ discharged by ships could potentially be utilized instead of sourcing it from quarries or limestone mines. Moreover, since the process of producing CaO generates CO₂ emissions itself, this might be performed in an industry where CCS is already implemented. Given the widespread availability of CCS in land industries, which are already operational, highly efficient, and industrially established, this approach is promising.

Such integration could pave the way for a circular economy, as illustrated in Figure 7 .

Another issue that could be addressed by implementing CCS onboard ships is certainly emissions of SO_X and CO₂ in ports. While the broader issue in ports includes more than just CO₂ emissions, reducing these emissions could effectively mitigate the problem of large quantities of pollutants released especially in urban areas. Vessels that cannot use cold ironing could rely on CCS to achieve this goal.

Once further developments of the system are made, it will also be necessary to assess the additional amount of fuel required to operate the system as well as the associated operational expenses, including maintenance and materials such as CaO. However, in the absence of a CO₂ liquefaction unit and the additional energy required for its operation, the extra energy demand typically needed for this unit in other types of CCSs is avoided (Bortuzzo et al., 2023; Hua et al., 2023).

However, it is worth noting that even if these costs are significant, these will be offset by savings from EU ETS or future pricing mechanisms, as well as tangible benefits for compliance with CII, EEXI, EEDI and GHG intensity regulations. In this framework, although various technologies can increase a ship’s energy efficiency and reduce CO₂ emissions, such as wind-assist systems, air lubrication technology, and energy-saving devices like waste heat recovery systems, these are unlikely to achieve the same level of reduction as CCS. Consequently, CCS is expected to result in greater savings within carbon pricing mechanisms like the EU ETS.

This study introduces a new framework to tackle challenges in marine environments and climate change mitigation. Future research could focus on detailed sensitivity analyses to validate assumptions about CCS efficiency and energy demands. These analyses would clarify the most influential variables and ensure the approach’s robustness under different conditions.

Building upon the insights gained from sensitivity analyses, further technical investigations could focus on enhancing the operational efficiency of the calcium looping process. This would involve addressing challenges such as optimizing CO₂ capture under diverse operating conditions and minimizing associated risks. Pilot studies in real-world marine environments would also be invaluable for assessing the feasibility of the technology at scale and identifying practical barriers to implementation. Moreover, the implications related to the need to introduce new training activities for on-board personnel to operate with the novel technology must be foreseen.

Economic considerations represent another critical aspect for future exploration. By leveraging findings from sensitivity and technical analyses, a high-level economic evaluation could be conducted by analyzing costs related to equipment, maintenance, and energy use that are still not available due to the lack of full-scale systems installed onboard ships. This evaluation should aim to identify cost-reduction strategies and the potential financial benefits of the proposed approach. This evaluation would include projected savings from emissions credits and could inform decision-making for both policymakers and industry stakeholders.

Another essential area for future research lies in the ecological assessment of CaCO₃ discharge and its potential impacts on marine ecosystems. Detailed studies should examine changes to biodiversity and water chemistry across various environments, complemented by predictive ecological modelling to forecast long-term consequences. These efforts should be coupled with the development of robust regulatory and monitoring frameworks capable of tracking direct and indirect impacts over time. Incorporating feedback mechanisms into such frameworks would help mitigate any unintended adverse effects, ensuring the sustainability of the intervention. Compared to other CCSs, this system eliminates the need for CO₂ liquefaction, simplifying onboard operations and enhancing its life cycle assessment. By avoiding the complexities of discharging liquefied CO₂ offshore, developing specialized port infrastructure, and transporting CO₂ to underground storage sites, it offers a more streamlined and sustainable solution. However, for the system under study future research could explore innovative ship designs that integrate onboard CaCO₃ storage tanks, enabling closed-loop solutions for future deployments. This approach would allow for the partial or complete containment of generated CaCO₃ onboard, with subsequent disposal at ports to support a circular economy. Evaluating the feasibility of repurposing collected CaCO₃ for industrial applications could further promote a sustainable green transport network by facilitating its distribution from ports to industries. These initiatives would address challenges related to onboard space constraints and land-based infrastructure, creating a comprehensive and sustainable strategy for CaCO₃ management.

Additionally, CaCO₃ is not listed among the prohibited wastes in Annex I and II of the London Convention, as outlined in this study. However, future research should consider new ecological insights and assess whether this approach aligns with existing regulatory frameworks or necessitates updates to international guidelines to accommodate novel strategies for climate mitigation.

Together, these avenues for further research provide a comprehensive roadmap for advancing the current study’s findings. They highlight the need for an interdisciplinary approach that integrates technical, economic, ecological and legal perspectives to maximize the potential of the proposed solution while addressing its limitations.