Prospects of Solar Energy in the Context of Greening Maritime Transport
Abstract
:1. Introduction
2. Literature Review
- Section 3 describes research methodologies and data.
- Section 4 presents an analysis of alternative fuels used on marine vessels.
- Section 5 analyzes technologies that use solar energy in shipping and their technical and economic performance.
- Section 6 analyzes the challenges and trends in the use of solar energy for maritime transport.
- Section 7 discusses the obtained results and proposes future research directions for solar energy use in the maritime sector.
- Section 8 presents conclusions.
3. Description of Research Methodology and Data
- The level of GHG emissions to the environment.
- Energy efficiency.
- Features of production and transportation.
- Features of storage on board ship.
- Economic efficiency.
4. Analysis of Alternative Fuels Used on Marine Vessels
4.1. Liquefied Natural Gas
4.1.1. Environmental Impact of LNG-Powered Vessels
4.1.2. Features of LNG Production and Transportation
- In liquefaction processes, either a mixed or a pure refrigerant is employed. In MR technology, a specially selected blend of hydrocarbons is used to replicate the cooling curve of natural gas. In Cascade technology, several distinct pure refrigerants with cascading boiling points throughout the cycles are utilized. In EXP technology, nitrogen or methane is employed. Owing to the extremely low boiling points of these gases, the liquefaction of natural gas is accomplished in a single cycle. The ranking of the processes by the temperature difference between the refrigerant and natural gas is as follows: MR less Cascade; Cascade less EXP. A reduction in energy consumption is achieved by maintaining a smaller temperature difference. Such a smaller temperature difference can be attained by increasing the heat exchange surface area, which in turn requires greater capital investments. From the above, it follows that the optimization of the gas liquefaction process can be accomplished by balancing the refrigerant zones and the heat exchanger design [65].
- Two primary types of heat exchangers are employed in LNG production: (1) the plate-fin or brazed aluminum type (PFHE) and (2) the spiral-wound heat exchanger type (SWHE). The advantages of PFHE include low pressure drops, versatility in accommodating fluctuations in low-temperature differentials, and a greater number of competitive suppliers. In contrast, the drawbacks of PFHE encompass the necessity for meticulous design and a pronounced susceptibility to physical damage, both of which are inherent to the aluminum construction of PFHE [63]. Among the advantages of SWHE are its higher reliability and ease of operation. However, its disadvantages include a higher cost, limited flexibility with respect to the feed gas composition, and less favorable mass and dimensional characteristics. Moreover, SWHE units are produced by only a few companies. Additionally, SWHE offers a higher maximum capacity (a single PFHE is rated at 1.5 million tons per year, whereas one SWHE can reach up to 4 million tons per year). The benefits and drawbacks of these heat exchanger types ultimately determine their application in various installations. For instance, Cascade and EXP installations employ PFHE, while SWHE is used in large-scale MR installations [65,66].
- Five types of drives and two types of compressors should be considered when analyzing the equipment used in liquefaction processes. The drive and compressor are adapted to the specific technology of the liquefaction process [64].
4.1.3. Features of LNG Storage on Marine Vessels
4.2. Methanol
4.2.1. Environmental Impact of Methanol-Powered Marine Engines
4.2.2. Methanol Production and Transportation Features
4.2.3. Methanol Storage Features on Marine Vessels
4.3. Hydrogen
4.3.1. Parameters of Hydrogen as Fuel for Marine Vessel Engines
4.3.2. Features of Hydrogen Production and Transportation
4.3.3. Features of Hydrogen Storage on Marine Vessels
Hydrogen Usage Onboard
Reactor Development
Hazards of Using Hydrogen Onboard
4.4. Ammonia
4.4.1. Environmental Impact of Ammonia-Powered Marine Engines
4.4.2. Features of Ammonia Production and Transportation
4.4.3. Features of Ammonia Storage on Marine Vessels
4.5. Biofuel
4.5.1. Environmental Impact of Marine Engines Running on Biofuel
4.5.2. Features of Biofuel Manufacturing and Transportation
- Carbohydrate crops.
- Oil crops.
- Lignocellulosic biomass.
- Woody biomass.
- Algal biomass, as well as residues from their production and processing.
4.5.3. Features of Biofuel Storage on Marine Vessels
4.6. The Techno-Economic Analysis of Alternative Fuels for Marine Vessels
4.6.1. Analysis of Technologies
- PEMFCs—Proton Exchange Membrane Fuel Cells.
- AFCs—Alkaline Fuel Cells.
- PAFCs—Phosphoric Acid Fuel Cells.
- MCFCs—Molten Carbonate Fuel Cells.
- SOFCs—Solid Oxide Fuel Cells.
4.6.2. Economic Performance Analysis
5. Innovative Approaches and Challenges of Using Solar Energy in Shipping
5.1. Components of Solar-Powered Marine Vessels
5.1.1. PV Array
5.1.2. DC–DC Converter as a Power Stabilizer
5.1.3. PV MPPT
5.1.4. Electric Motor
5.1.5. Battery Management System
5.2. The Application of Concentrated Solar Energy Systems on Marine Vessels
5.3. Contrasting PV and CSP
5.4. Techno-Economic Analysis of the Use of Battery Storage Systems for Powering Marine Vessel Engines
6. Emerging Trends in Solar Energy for Maritime Transport
6.1. Analysis of the Limitations for the Use of Solar Energy on Marine Vessels
6.2. Trends in the Development of Solar Energy for Marine Transportation
7. Discussion
- Hydrogen is a highly flammable fuel.
- Risks of hydrogen leaks through joints and cracks in any pipelines or storage system.
- Hydrogen disperses easily in the air.
- In high concentrations, hydrogen can displace oxygen in the air, leading to asphyxiation.
- The necessity to avoid explosion risks [85].
- The necessity of appropriate materials capable of withstanding low temperatures to prevent brittleness.
- The necessity to prevent liquid hydrogen spills to avoid asphyxiation and explosion.
8. Conclusions
- The adaptation of concentrated solar power (CSP) systems for marine applications.
- The development of materials and designs for solar panels is specifically intended for the marine environment.
- The development of methods for evaluating the long-term economic benefits of using solar energy on ships.
- The improvement of regulatory frameworks and international standards for the application of solar energy on ships.
Author Contributions
Funding
Institutional Review Board Statement
Informed Consent Statement
Data Availability Statement
Conflicts of Interest
Appendix A
Type of Fuel | Calorific Value (MJ/kg) | Onboard Storage Requirements | Utilization Efficiency | Byproduct of Utilization | Availability of Commercial Utilization Technologies | |
---|---|---|---|---|---|---|
FC (Electrical Efficiency) | ICE (Internal Combustion Engine) | |||||
Liquefied Natural Gas (LNG) | 50–55 | 163° (under pressure or without pressure) | 45–60% (SOFC) 35–45% (PEMFC) | 35–40% | CO2, H2O, NOx (ICE) | ICE: Yes, widely available for commercial use; FC: Underdeveloped, no commercial maritime use |
Hydrogen | 120–140 | 350–700 bar (gaseous), −252.8 °C (liquefied), material-based storage | 50–60% (PEFMC/SOFC) | 30–35% | H2O, NOx (ICE) | ICE: Yes, available for commercial use; FC: Yes, available for commercial use |
Ammonia | 22.5 | 21 °C below 8.8 bar or 33 °C at atmospheric pressure | 30–60% (SOFC) 15–30% (AFC) | 35–40% | H2O, N2, NOx (ICE) | ICE: Underdeveloped; FC: Underdeveloped, no commercial maritime use |
Methanol | 22.7 | Liquid at ambient temperature | 30–50% (SOFC) 20–30% (DFMC) | 40% | CO2, H2O, CO (ICE), NOx (ICE) | ICE: Yes, widely available for commercial use; FC: Underdeveloped, no commercial maritime use |
Biodiesel | 38–46 | Liquid at ambient temperature | 10–30% (AFC) | 10–30% (AFC), Varies | CO2, H2O, CO (ICE), NOx (ICE) | ICE: Yes, widely available for commercial use; FC: Underdeveloped, no commercial maritime use |
Electricity | - | High energy density battery systems such as NMC, LFP, NCA, and solid-state batteries | - | - | - | Currently available only for small shore-based vessels |
Fuel | Material for Fuel Production | Fuel Production Costs/Import Price, USD/MJ | Fossil Fuel Price, USD/MJ | Total Price |
---|---|---|---|---|
LNG | Natural gas | 0.0022–0.0092 | 0.014 | 0.16–0.66 |
LBG | Biomass | 0.0081–0.032 | 0.57–2.29 | |
Biodiesel | Soybean, palm oil, rapeseed | 0.013–0.027 | 0.92–1.93 | |
Methanol | Biomass | 0.021–0.037 | 1.50–2.64 | |
Methanol | Natural gas | 0.006–0.022 | 0.43–1.57 | |
Hydrogen SMR | Wind power, water | 0.0063–0.035 | 0.45–2.5 | |
Hydrogen electrolysis | Wind power, water | 0.025–0.08 | 1.78–5.71 | |
Hydrogen electrolysis | Nuclear energy, water | 0.019–0.045 | 1.36–3.21 | |
Ammonia | Natural gas | 0.0093–0.036 | 0.66–2.57 | |
Ammonia | Wind power | 0.021–0.037 | 1.50–2.64 |
Component | Capital Investments for Vessel Modernization, USD/kW | Capital Expenditures for Construction of New Vessels (Four-Stroke Engine/Two-Stroke Engine), USD/kW | Life Cycle |
---|---|---|---|
Propulsion system | |||
ICE diesel, biodiesel | - | 240/460 | 30 years |
ICE, methanol | 328 | 265/505 | 30 years |
ICE, ammonia | - | 370/600 | 30 years |
ICE, LNG, LBG, hydrogen | 900 | 387/850 | 30 years |
Fuel cell, SOFC | - | 4000–9000 | 7–12 years |
Fuel cell, PEMFC | - | 730–2860 | 7–12 years |
Electrical and generator, LNG, LBG, hydrogen | - | 400 | 30 years |
Electric motor | - | 250 | 30 years |
Fuel storage system | |||
Gas supply system + tank, LNG, LBG, USD/kg | 270–420 | 270–420 | 30 years |
Gas supply system + high-pressure tank (700 bar), Hydrogen, USD/kg | - | 576–868 | 30 years |
Criteria | PV | CSP |
---|---|---|
Storage and intermittency | It generates electricity immediately, making storage difficult, and batteries are economically unfeasible for large installations. Intermittency is the main drawback of PV. | Overcoming interruptions and maintaining supply at night, TES (Thermal Energy Storage) is an attractive feature of CSP, making it dispatchable and increasing CSP’s penetration in energy sectors. |
Efficiency | Maximum efficiency 10–28%, with productivity decreasing over time. | Average efficiency 41%, efficiency increases with temperature. |
Capacity factor | 10–35% | With TES 29–33%, without TES 28–29%. |
Equipment | Direct current must be converted to alternating current using inverters. | Output is alternating current combined with feeding cycles; therefore, an inverter is not needed. |
Solar Irradiance | Uses Global Horizontal Irradiance (GHI) and can operate in diffuse light. | CSP uses only Direct Normal Irradiance (DNI), which varies from 65 to 85% of total GHI. |
Control System | Advantages | Disadvantages |
---|---|---|
FOC | 1. Lower torque pulsation coefficient on the motor shaft. 2. Better speed control quality at speeds higher than the rated value. | 1. Less energy efficiency. 2. Worse torque control quality. |
DTC | 1. Better energy efficiency. 2. Better torque control quality. | 1. Higher torque pulsation coefficient on the motor shaft. 2. Lower speed control quality at speeds greater than the rated value. |
Filtration Type | Advantages | Disadvantages |
---|---|---|
Frequency domain | 1. Higher filtering accuracy | 1. More time of unstable operation of the compensator. 2. More complex algorithm for obtaining the desired signals of phase currents of the stator phase currents of the induction motor. |
Time domain | 1. Less time of unstable operation of compensator. 2. Simpler algorithm to obtain the desired signals of induction motor stator phase currents. | 1. Less accurate filtering. |
Battery Type | Advantages |
---|---|
Gel battery | 1. No maintenance required. 2. No leaks. 3. Can be submerged in water. 4. Spill-proof. 5. Eliminated gas emission. 6. Can be safely used near sensitive electronics and in public areas. |
Pure lead thin film | 1. Can withstand higher charge power. 2. Charges quickly. 3. 400 cycles of charge and discharge. |
Lithium-manganese | 1. Can withstand higher charge power. 2. Charges quickly. 3. 400 cycles of charge and discharge. |
With absorbed glass mat | 1. Good starting power. 2. Deep cycle capability. |
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Fuel Type | LNG | HFO | |
---|---|---|---|
Main engine type | Low-speed high-pressure dual-fuel engines (LS-HPDF) | Low-speed low-pressure dual-fuel engines (LS-LPDF) | Low-speed diesel cycle engines (LSD) |
Engine model: | 6G50ME-GI | 6X-52DF | 6G50ME |
Average main engine load at sea and operating days | 72.5%/250 days | ||
Engine thermal efficiency (%) at 72.5% MCR | 55.30 | 50.20 | 53.9 |
SFC (g/kWh) at 72.5% MCR (Primary/Pilot Fuel) | 126.85/3.9 | 141.75/1.95 | 147.24/ - |
Lower heating value (LHV), MJ/kg | 49.2 | 49.2 | 40.2 |
Emission factor (GHG t/t of Fuel) | |||
CO2 | 2.75 | 2.75 | 3.144 |
CH4 | 0.001449 | 0.017086 | 0.00006 |
N2O | 0.000217 | 0.000137 | 0.00016 |
Fuel Type | LNG | HFO |
---|---|---|
Type of auxiliary engine | Medium-speed high-pressure dual-fuel engines (MS-LPDF) | Medium-speed diesel cycle engines (MSD) |
SFOC (g/kWh) | 152 | 195 |
Emission factor (GHG t/t of Fuel) | ||
CO2 | 2.75 | 3.144 |
CH4 | 0.036 | 0.00006 |
N2O | 0.000131 | 0.00025 |
Load (%) | LS-HPDF | LS-LPDF | ||
---|---|---|---|---|
SFOS | SPOS | SFOS | SPOS | |
10 | 141.4 | 12.5 | 156.8 | 4.7 |
20 | 137.1 | 10.1 | 152.6 | 4.1 |
30 | 133.8 | 8.0 | 149.1 | 3.5 |
40 | 131.4 | 6.3 | 146.3 | 2.9 |
50 | 129.8 | 5.0 | 144.1 | 2.5 |
60 | 129.2 | 4.1 | 142.6 | 2.1 |
70 | 129.4 | 3.5 | 141.7 | 1.8 |
80 | 130.6 | 3.3 | 141.5 | 1.6 |
90 | 132.7 | 3.5 | 142.0 | 1.5 |
100 | 135.6 | 4.1 | 143.1 | 1.4 |
Indicator | Cascade | MR | EXP |
---|---|---|---|
Application | LS Onshore | LS Onshore, SS, and Offshore | SS Onshore and Offshore |
Energy efficiency | H | M to H | L |
Equipment quantity | H | L to M | L |
Heat transfer surface area | M | H | L |
Operational simplicity | L | L to M | H |
Ease of startup and adjustment | M | L | H |
Feed gas composition adaptability | H | M | H |
Vessel motion sensitivity | H | M to H | L |
Space requirements | H | M | L |
Hydrocarbon refrigerant storage | H | M to H | None |
Capital expenditure | H | L to M | L |
Fuel Type | Methanol | HFO |
---|---|---|
Main Engine Type | LSD | LSD |
Engine manufacturer model | 6G50ME-LGIM | 6G50ME |
Thermal efficiency (%) at 72.5% MCR | 53.9 | 53.9 |
SFC (g/kWh) at 72.5% of MCR (methanol/HFO) | 307.5/13.1 | 147.24/- |
Lower heating value (LHV), MJ/kg | 19.9 | 40.2 |
Emission Factor (GNG t/ton of fuel) | ||
CO2 | 1.375 | 3.144 |
CH4 | 0.000006 | 0.00006 |
N2O | 0.00016 | 0.00016 |
Fuel Type | Methanol | HFO |
---|---|---|
Auxiliary engine type | MSD | MSD |
SFOC (g/kWh) | 370 | 195 |
Emission factor (GHG t/t fuel) | ||
CO2 | 1.375 | 3.144 |
CH4 | 0.00006 | 0.00006 |
N2O | 0.00025 | 0.00025 |
Engine Load (%) | HFO | Methanol |
---|---|---|
10 | 141.4 | 45.9 |
20 | 137.1 | 33.3 |
30 | 133.8 | 25.1 |
40 | 131.4 | 20.8 |
50 | 129.8 | 19.7 |
60 | 129.2 | 21.3 |
70 | 129.4 | 24.8 |
80 | 130.6 | 29.9 |
90 | 132.7 | 35.8 |
100 | 135.6 | 41.9 |
Parameter | Units | Hydrogen | Methane |
---|---|---|---|
Gas density at standard conditions (ISO) | kg/m3 | 0.0905 | 0.716 |
Relative gas density (air = 1) | relative units | 0.07 | 0.554 |
Relative density, liquid (water = 1) | relative units | 0.071 | 0.44–0.48 |
Lower heating value | MJ/kg | 119.96 | 50 |
Critical temperature | °C | −240 | −82.45 |
Boiling point | °C | −253 | −161.48 |
Melting point | °C | −259 | −187.6 |
Combustibility range | % (v/v) | 4–77 | 5–14 |
Maximum combustion velocity | m/s | 2.91 | 0.37 |
Autoignition temperature | °C | 585 | 537 |
UN number | 1954 | 1971 | |
Additional information | Burns with an invisible flame, extremely flammable gas | Asphyxiating |
Technology | Energy Consumption (kWh/kg(H2)) | Operating Temperature (°C) | Hydrogen Pressure (MPa) | Stack Lifetime (hours) | Deployment Scale (kW) |
---|---|---|---|---|---|
Alkaline | 53.4 | 80 | 0.7 | 90,000 | >100,000 |
PEM | 54.6 | 80 | 0.5 | 50,000 | >100,000 |
SOFC | 36.14 | >800 | 0.1 | 23,000 | 7.5 |
Membraneless | 54.34 | <50 | 0/1 | - | ~10 |
Engine Type | Fuel | CO2 | CH4 | CO2-eq (CH4) | N2O | CO2-eq (N2O) | CO2-eq (Total) |
---|---|---|---|---|---|---|---|
Two-stroke slow-speed main engine (ME) with diesel cycle | MGO | 3.21 | 6.53 × 10−5 | 1.83 × 10−3 | 2.22 × 10−4 | 5.88 × 10−2 | 3.27 |
LNG | 2.75 | 1.64 × 10−3 | 4.58 × 10−2 | 2.45 × 10−4 | 6.51 × 10−2 | 2.86 | |
Methanol | 1.38 | 3.34 × 10−5 | 9.35 × 10−4 | 1.00 × 10−5 | 2.65 × 10−3 | 1.38 | |
Ammonia | 0 | 0 | 0 | 5.42 × 10−4 | 1.44 × 10−1 | 0.14 | |
Four-stroke medium-speed auxiliary engine with Otto cycle | MGO | 3.21 | 5.35 × 10−5 | 1.50 × 10−3 | 1.60 × 10−4 | 4.25 × 10−2 | 3.25 |
LNG | 2.75 | 3.54 × 10−2 | 9.92 × 10−1 | 1.29 × 10−4 | 3.41 × 10−2 | 3.78 | |
Methanol | 1.38 | 2.53 × 10−5 | 7.09 × 10−4 | 7.59 × 10−6 | 2.01 × 10−3 | 1.38 | |
Ammonia | 0 | 0 | 0 | 5.02 × 10−3 | 1.33 | 1.33 |
Fuel Property | Ammonia | Diesel |
---|---|---|
Liquid density, kg/m3 | 602.8 | 832 |
Heat of combustion, MJ/kg | 18.8 | 42.7 |
Octane number | 110 | 30 |
Cetane number | 5–7 | 40–55 |
Ignition temperature, °C | 651 | 254–285 |
Laminar flame speed, m/s | 0.07–0.14 | 0.87 |
Stoichiometric air-to-fuel ratio | 6.06 | 14.5 |
Heat of vaporization, kJ/kg | 1370 | 232 |
Operating Mode | Mode 1 | Mode 2 | Mode 3 | Mode 4 | Mode 5 |
---|---|---|---|---|---|
Weighting Factor | 0.05 | 0.05 | 0.25 | 0.50 | 0.15 |
Engine Conditions Using Biofuel Mixture | |||||
Engine Load (%) | 20 | 32 and 37 | 41 | 61 and 63 | 90 |
Engine Speed, rpm | 37 | 55 and 66 | 63 | 79 | 90 |
Power (kWh) | 1986 | 3178 and 3675 | 4072 | 6058 and 6257 | 8939 |
Fuel Consumption (kg·h−1) | 280 | 561 and 825 | 736 | 1179 and 1215 | 1780 |
Specific Fuel Consumption (g·kWh−1·h−1) | 141 | 177 and 224 | 181 | 195 and 194 | 199 |
Engine Conditions Using LSMGO | |||||
Engine Load (%) | 23 | 37 | 44 | 67 | 90 |
Engine Speed, rpm | 36 | 55 | 63 | 79 | 87 |
Power (kWh) | 2284 | 3675 | 4370 | 6654 | 8939 |
Fuel Consumption (kg·h−1) | 304 | 587 | 762 | 1245 | 1703 |
Specific Fuel Consumption (g·kWh−1·h−1) | 133 | 160 | 174 | 187 | 191 |
Renewable Carrier | Production Technology |
---|---|
LBG/LNG | Anaerobic digestion |
Gasification and cat. reaction (Sabatier process) | |
Ethanol | Fermentation from sugars |
Fermentation from lignocellulosic waste | |
Methanol | Anaerobic production of methane and dehydration |
Gasification from solid biomass | |
DME (dimethyl ether) | Gasification |
Dehydration of bio-methanol | |
SVO (straight vegetable oil) | Extraction from plants |
FAME (fatty acid methyl esters) | Transesterification of vegetable oils |
HVO (hydrotreated vegetable oil) | Hydrogenation of vegetable oils |
Renewable diesel | FT, HTL, pyrolysis, HVO |
Lignin diesel oil | Solvolysis |
Fuel | LHV (MJ/kg) | HHV (MJ/kg) | Energy Density (MJ/L) |
---|---|---|---|
HFO | 39 | 42 | 39 |
ULS MDO (Ultra-Low Sufhur Marine Diesel Oil) | 43 | 46 | 36 |
Petrol | 43 | 47 | 32 |
LBG | 48 | 55 | 21 |
Biomethanol | 20 | 23 | 16 |
Bioethanol | 27 | 30 | 21 |
SVO | 37 | 40 | 34 |
FAME | 38 | 40 | 34 |
HVO | 43 | 47 | 33 |
FT diesel (Fischer–Tropsch diesel fuel) | 44 | – | 34 |
UPO (Upgraded Pyrolysis Oil) | 43 | 47 | 36 |
Lignin oil | 33 | 35 | – |
HTL biocrude (Hydrothermal Liquefaction Biocrude) | 34–38 | – | – |
Component | Capital Investments for the Construction of New Ships (Four-Stroke Engine/Two-Stroke Engine), USD/kW | Life Cycle |
---|---|---|
Propulsion system | ||
Electric motor | 400 | 30 years |
Fuel storage system | ||
Battery, NMC, USD/kWh | 400–1000 and expected to fall to 124 in 2030 | 8–11 years |
Battery, LPF, USD/kWh | 210–1000 and expected to fall to 70 in 2030 | 7–13 years |
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Petrychenko, O.; Levinskyi, M.; Goolak, S.; Lukoševičius, V. Prospects of Solar Energy in the Context of Greening Maritime Transport. Sustainability 2025, 17, 2141. https://doi.org/10.3390/su17052141
Petrychenko O, Levinskyi M, Goolak S, Lukoševičius V. Prospects of Solar Energy in the Context of Greening Maritime Transport. Sustainability. 2025; 17(5):2141. https://doi.org/10.3390/su17052141
Chicago/Turabian StylePetrychenko, Olga, Maksym Levinskyi, Sergey Goolak, and Vaidas Lukoševičius. 2025. "Prospects of Solar Energy in the Context of Greening Maritime Transport" Sustainability 17, no. 5: 2141. https://doi.org/10.3390/su17052141
APA StylePetrychenko, O., Levinskyi, M., Goolak, S., & Lukoševičius, V. (2025). Prospects of Solar Energy in the Context of Greening Maritime Transport. Sustainability, 17(5), 2141. https://doi.org/10.3390/su17052141