Decarbonization in Shipping Industry: A Review of Research, Technology Development, and Innovation Proposals
Abstract
:1. Introduction
2. Climate Change and the Shipping Industry
2.1. Climate Change
Size of Shipping Industry in Terms of Emissions
2.2. Current Legislation and Incentives to Meet 2050 Emission Targets Set by the International Maritime Organization (IMO)
- To reduce the carbon intensity of international shipping, compared to 2008 levels, by 40% by 2030.
- To increase that reduction to 70% by 2050.
- To reduce the GHG emissions from international shipping, again compared to 2008 levels, by at least 50%, by 2050.
- To achieve zero GHG emissions as soon as possible within this century, i.e., by 2100.
- Hull design,
- Economy of scale,
- Power and propulsion (including energy-saving devices),
- Speed,
- Fuels and alternative energy sources, and
- Weather routing and scheduling
2.2.1. Ship Energy Efficiency Management Plan (SEEMP)
2.2.2. Energy Efficiency Design Index (EEDI)
2.2.3. Energy Efficiency Operational Index (EEOI)
2.2.4. New Short-Term Measures (2018–2023)
2.2.5. Energy Efficiency Existing Ship Index (EEXI)
2.2.6. Carbon Intensity Index (CII)
2.2.7. Medium- (2023–2030) and Long-Term Measures (Beyond 2030)
2.2.8. Market-Based Measures (MBM)
- Economic incentives for the maritime sector to reduce its fuel consumption by investing in more fuel-efficient ships, technologies and operating ships in a more energy efficient way.
- Offsetting in other sectors with growing emissions related to the shipping industry.
2.3. European Green Deal
2.4. International Maritime Research and Development Board (IMRB)
2.5. Existing Pilot Projects
- Safety,
- Environmental impact,
- Economic costs, and
- Generation of knowledge and experience that can be used to further improve technologies. In this way, the overall cost will reduce, a key prerequisite for disseminating and scaling these technologies.
- Hydrogen-fueled ship (C—ZERO Japan H2).
- Super-efficient LNG-fueled ship (C—ZERO Japan LNG and Wind).
- Ammonia-fueled ship (C—ZERO Japan NH3).
- Onboard CO2-capturing ships (C—ZERO Japan Capture).
3. Alternative Fuels for Shipping
- LNG, methanol and LPG are competitive in terms of energy costs, while HVO is significantly more expensive.
- Hydrogen and ammonia are also far more expensive.
- The large cost range indicates a significant uncertainty in terms of pricing.
3.1. Hydrogen
3.1.1. Hydrogen Storage Technologies
- Compressed hydrogen,
- Liquid hydrogen (cooling hydrogen to −252.9 °C),
- Chemical storage
- Ammonia, nitrogen-based storage (via the Haber-Bosch reaction, ammonia can serve as storage medium and a fuel itself),
- CO2-based storage (via carbon capture and storage, producing synthetic fuels such as synthetic diesel, synthetic liquefied synthetic methane—LSM, methanol and formic acid),
- Aromatic Liquid Organic Hydrogen Carriers (LOHCs) (use of aromatic LOHCs and a catalyst to store hydrogen)
- Metal hybrides (store hydrogen within materials).
3.1.2. Hydrogen Safety
3.1.3. Green Hydrogen
3.1.4. Other “Colors” for Hydrogen (Brown, Grey, Yellow, Blue)
3.1.5. Liquid Hydrogen (LH2)
3.2. Ammonia
3.3. Methanol
3.4. Liquefied Natural Gas (LNG)
- Lean-burn spark ignition,
- Low-pressure dual fuel (4- and 2-stroke),
- High-pressure dual fuel and
- Gas turbine.
4. Renewable Energy Sources
4.1. Wind
- Soft-sail,
- Fixed-sail,
- Flettner rotor,
- Kite-sail, and
- Turbine technologies.
4.1.1. Soft-Sails
4.1.2. Fixed-Sails
4.1.3. Flettner Rotors
4.1.4. Kite Sails
4.1.5. Wind Turbines
4.2. Solar
Solar-Hybrid Systems
4.3. Biofuels
- First Generation: “The source of carbon for the biofuel is sugar, lipid or starch directly extracted from a plant. The crop is actually or potentially considered to be in competition with food.”
- Second Generation: “The biofuel carbon is derived from cellulose, hemicellulose, lignin or pectin. For example, this may include agricultural, forestry wastes or residues, or purpose-grown non-food feedstocks (e.g., Short Rotation Coppice, Energy Grasses).”
- Third Generation: “The biofuel carbon is derived from aquatic autotrophic organisms (e.g., algae). Light, carbon dioxide and nutrients are used to produce the feedstock, “extending” the carbon resource available for biofuel production.”
4.3.1. Liquid Biofuels
4.3.2. Biogas
Engine Type | Manufacturer | Engine Model |
---|---|---|
Four-stroke | Anglo Belgian Corporation (Gent, Belgium) | VDZC Series; DL36 Series |
Akasaka diesels (Tokyo, Japan) | AX 28 Series | |
Caterpillar Inc (Deerfield, MA, USA) | 3500 Series; 3600 Series | |
MaK Motoren GmbH and Co. (Peoria, IL, USA) | M601; M20C, M25C, M32C and M43C Series | |
Daihatsu Motor Co. Ltd. (Ikeda, Japan) | DK-28 Series; DC-17Ae Series | |
Deutz AG (Cologne, Germany) | TCD 2015 V Series | |
Doosan Engine Co. Ltd. (Changwon, Korea) | V222TI; L136TI Series | |
Hanshin Diesel (Kobe City, Japan) | LA 30; LA 34 Series | |
Hyundai Heavy Industries Co. Ltd. (Ulsan, Korea) | HiMSEN Series H17/28; H21/32; H32/40 | |
MAN Diesel and Turbo SE (Augsburg, Germany) | L23/30; L16/24; L21/31; L27/38; L32/40; L40/54; L48/60 CR; L58/64; L32/44 CR; D2876 | |
Mitsui and Co. Ltd. (Tokyo, Japan) | ADD30V | |
MTU Friedrichschafen GmbH (Friedrichshafen, Germany) | MTU V 4000 | |
Paxman (Colchester, UK) | VP185 | |
Rolls-Royce Group Plc (London, UK) | B32:40R; C25:33L | |
Ruston and Hornsby (Lincoln, UK) | RK 270; RK 280 | |
Pielstick (Augsburg, Germany) | S.E.M.T. Pielstick series PC2.6B | |
Sulzer Brothers Ltd. (Winterthur, Switzerland) | Z40; ZA40S | |
Wärtsilä NSD (Helsinki, Finland) | L20; L/V32C; L/V46C; 64C | |
Yanmar Co. Ltd. (Osaka, Japan) | 6N21; EY18L; EY26L; AYM | |
Gas four-stroke | MAN Diesel and Turbo SE (Augsburg, Germany) | V35/44G |
Mitsubishi Heavy Industries (Tokyo, Japan) | KU30G | |
Rolls-Royce Bergen (Hordvik, Norway) | C26:33LPG | |
Gas-diesel dual-fuel four-stroke | MAN Diesel and Turbo SE (Augsburg, Germany) | 35/44DF |
Caterpillar Inc (Deerfield, MA, USA) | M46DF | |
Wärtsilä NSD (Helsinki, Finland) | L50DF | |
Two-stroke ship low-speed crosshead | MAN Diesel and Turbo SE (Augsburg, Germany) | MC, MC-C, ME, ME-C and ME-B series |
Mitsubishi Heavy Industries (Tokyo, Japan) | UEC LSH-Eso; LSE-Eco | |
Wärtsilä-Sulzer (Helsinki, Finland) | RTA; RT-Flex Series | |
WinGD (Winterthur, Switzerland) | W-X Series | |
Gas diesel two-stroke ship low-speed (low pressure) | WinGD (Winterthur, Switzerland) | X-DF Series |
Gas diesel two-stroke ship low-speed (high pressure) | MAN Diesel and Turbo SE (Augsburg, Germany) | ME-GI Series |
5. Maturity of Technologies
5.1. Internal Combustion Engines (ICE)
5.1.1. Types of Engines Used in Shipping
Four-Stroke Engines
Two-Stroke Engines
- Fuel (in the gas phase) enters the combustion cylinder after the exhaust valve is closed at the initial stage of the compression stroke under relatively low pressure; hence, such systems are called low-pressure supply systems.
- Fuel (in the gas phase) with the ignition fuel enters the combustion cylinder at the end of the compression stroke which is at high pressure; hence, such systems are called high-pressure supply systems or direct gas injection (GD).
Gas and Gas-Diesel (Dual Fuel) Engines
- (1)
- Convert diesel engines to operate according to the Otto cycle, i.e., mix the air-fuel externally to the combustion cylinder and ignite the air-fuel mixture with electric spark ignition.
- (2)
- Mix the air-fuel externally to the combustion chamber and ignite the air-fuel mixture with electric spark ignition combined with liquid fuel injection into the combustion cylinder: DF engine.
- (3)
- Mix the air-fuel in the combustion chamber and ignite the air-fuel mixture with electric spark ignition combined with liquid fuel injection into the combustion: DF engine.
- Effective lubrication (and the varying degree of sulfur level) because of the use of different fuels. The knocking margin due to alkali and other compounds depositing on the cylinder walls, hence it will be difficult to select a suitable lubricant that satisfies operation in diesel or gas mode.
- Different characteristics of natural gas at different bunkering stations (varying degree of humidity, CO2, etc.) which may cause knocking.
5.1.2. Combustion of Alternative Fuels in ICE
LNG in ICE
Hydrogen in ICE
Ammonia in ICE
- Poor ignition and very slow flame propagation speed compared to other fuels, see Table 4 for minimum ignition energy and laminar flame speed.
- Toxic and corrosive, thus the requirement of sustainable safety and storage solutions.
- Higher NOx emissions, unless controlled either by after-treatment or by optimizing the combustion process.
- Regulations/policies will need to be developed for its use as a marine fuel.
Methanol in ICE
5.1.3. After-Treatment Technologies in ICE
Direct Water Injection (DWI)
Intake Air Humidification
Water-in-Fuel Emulsion
Non-Thermal Plasma (NTP)
Selective Catalytic Reduction (SCR)
- Ammonia SCR after-treatment
- Hydrocarbon SCR after-treatment
- Carbon monoxide SCR after-treatment
- Hydrogen SCR after-treatment
- Alcohol SCR after-treatment
NOx Trap After-Treatment
Exhaust Gas Recirculation (EGR)
Control of Particulate Matter (PM) Emissions
De-SOx After-Treatment Technologies
5.2. Fuel Cells
5.2.1. Fuel Cell Types
- Alkaline fuel cell (AFC),
- Low- and high-temperature polymer electrolyte membrane fuel cell (LT/HT-PEMFC),
- Phosphoric acid fuel cell (PAFC),
- Molten Carbonate fuel cell (MCFC),
- Direct Methanol fuel cell (DMFC) and
- Solid oxide fuel cell (SOFC).
5.2.2. Hydrogen as Fuel for Fuel Cells
5.2.3. Ammonia as Fuel for Fuel Cells
5.3. Electric/Hybrid Propulsion
- Batteries,
- Flywheels, and
- Supercapacitors.
5.4. Batteries and Supercapacitors
5.5. Gas Turbines
5.6. Nuclear
5.7. Carbon Capture and Storage (CCS)
6. Reduction of Fuel Consumption via Technical and Operational Measures
6.1. Vessel Speed
- Full speed: 23–25 knots (44 km/h).
- Slow steaming: 20–22 knots (39 km/h).
- Extra slow steaming: 17–19 knots (33 km/h).
- Super slow steaming: 15 knots (28 km/h).
6.2. Reduction of Hull Resistance
6.2.1. Cleaning
6.2.2. Paints and Low-Resistance Coatings
6.2.3. Vessel Design
Reduced Ballast Operation
Lightweight Construction
Optimum Hull Dimensions
Low-Profile Hull Openings
Interceptor Trim Plates
Skeg Shape/Trailing Edge
Bulbous Bow
6.2.4. Propeller Design
- Wing thrusters (<10% improvement),
- Counter rotating propellers (<12% improvement),
- Optimization of propeller–hull interaction (<4% improvement),
- Propeller–rudder interactions (<4%),
- Advanced propeller blade sections (<2%),
- Propeller tip winglets (<4%), propeller nozzle (<5%),
- Constant vs. variable speed operation (<5%),
- Pulling thruster (<10%), and
- Propeller efficiency management (<2%).
6.3. Air Lubrication
- Bubble Drag Reduction (BDR),
- Air Layer Drag Reduction (ALDR), and
- Partial Cavity Drag Reduction (PCDR).
6.3.1. Bubble Drag Reduction
6.3.2. Air Layer Drag Reduction
6.3.3. Partial Cavity Drag Reduction
6.4. Waste Heat Recovery
- Rankine Cycle (RC):
- ○
- Steam/conventional Rankine Cycle
- ○
- Organic Rankine Cycle (ORC)
- ○
- Super-Critical Rankine Cycle
- Kalina Cycle (KC)
- Exhaust gas turbine system:
- ○
- Hybrid turbocharger
- ○
- Mechanical turbo-compound system
- ○
- Hydraulic turbo-compound system
- ○
- Electric turbo-compound system
- Thermoelectric generation (TEG) systems
- There is no optimal WHR solution for maritime applications. One has to consider the trade-offs of costs, working fluid characteristics, size and safety.
- As a rule of thumb:
- Steam RC in combination with a power turbine for marine engines “with power output greater than 25 MW is more likely to be used due to high efficiency and technology maturity”.
- ORC technologies are recommended for relatively small size ships due to high efficiency and flexibility in recovering waste heat from different sources.
- The CO2-based power cycles are “more appealing where the system size is of particular importance”.
- KC has found use in land-based applications (such as geothermal applications) but it is seldom recommended in maritime applications because of the toxicity of the working fluid (ammonia-water mixture).
7. Future Trends, Challenges and Conclusions
Author Contributions
Funding
Institutional Review Board Statement
Informed Consent Statement
Data Availability Statement
Conflicts of Interest
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Measures | Possible CO2 Emissions Reductions |
---|---|
Advanced biofuels | 25–100% |
Liquefied Natural Gas (LNG) | 0–20% |
Hydrogen | 0–100% |
Ammonia | 0–100% |
Fuel cells | 2–20% |
Electricity | 0–100% |
Wind | 1–32% |
Solar | 0–12% |
Nuclear | 0–100% |
Advantages | Disadvantages |
---|---|
No sulfur in its molecular formula, hence no SOx emissions | Slip methane (un-combusted methane leak) enhances GHG gains compared to traditional fuels such as MGO and HFO [74,75] |
Lower CO2 emissions because of C:H ratio (25% less compared to diesel or bunker fuel), so can help the industry to decarbonize as a transitional fuel [74] | Still an emitter of CO2, hence cannot achieve decarbonization and need to take into account embodied CO2 (well-to-tank analysis) |
Compared to its gaseous state, takes up 600 times less space for storage and transportation [66] | But special care is required for transportation and storage |
Compared to hydrogen and ammonia storage, lower implications in terms of toxicity and safety | Safety issues (explosion hazard or cold fracture of hull due to low temperatures) |
Low NOx emissions if low-pressure dual fuel engine is used [74] | High NOx emissions if high-pressure dual fuel engine is used [74]. Depending on engine conditions, CO and unburnt hydrocarbons may increase [76]. |
Unit | Ammonia | Hydrogen | |
---|---|---|---|
Lower heating value | MJ/kg | 18.8 | 120.0 |
Flammability limits, gas in air | Vol. % | 15–28 | 4.7–75 |
Laminar flame speed | m/s | 0.015 | 3.51 |
Autoignition temperature | °C | 651 | 571 |
Absolute min. ignition energy | mJ | 8.0 | 0.018 |
Octane rating, RON | - | >130 | >100 |
Density, 25 °C, 1 atm | g/L | 0.703 | 0.082 |
Fuel Cell Type | Project/Vessel Name | Fuel | Capacity |
---|---|---|---|
AFC | Hydra | Metal hybride | 6.9 kW |
Hydrocell Oy | Metal hybride | 30 kW | |
LT-PEMFC | Elding | H2 | 10 kW |
ZemShip Alsterwasser | H2 | 96 kW | |
Nemo H2 | H2 | 60 kW | |
Hornblower Hybrid | H2 | 32 kW | |
Hydrogenesis | H2 | 12 kW | |
SF-BREEZE | H2 | 120 kW | |
Cobalt 233 Zet | H2 | 50 kW | |
US SSFC | Diesel * | 500 kW | |
HT-PEMFC | Pa-X-ell MS Mariella | Methanol | 2 × 30 kW |
RiverCell | Methanol | 250 kW | |
MF Vågen | H2 | 12 kW | |
RiverCell ELEKTRA | H2 | 3 × 100 kW | |
MCFC | MC WAP | Diesel * | 150/500 kW |
FelloSHIP Viking Lady | LNG * | 320 kW | |
US SSFC | Diesel * | 625 kW | |
SOFC | METHAPU Undine | Methanol | 20 kW |
SchIBZMS Forester | Diesel * | 100 kW | |
FELICITAS subproject 2 | LNG * | 250 kW |
Fuel Cell Type | Operating Temperature (°C) | Fuel | Internal Reforming | Power Capacity | Drawbacks |
---|---|---|---|---|---|
AFC | 60–200 | H2 | No | ≤500 kW | CO2 poisoning |
LT-PEMFC | 65–85 | H2 | No | ≤120 kW | CO + S poisoning |
HT-PEMFC | 140–220 | H2 | No | ≤500 kW | CO + S poisoning |
PAFC | 140–200 | H2, LNG and methanol | No | 120–400 kW | CO + S poisoning |
DMFC | 75–120 | methanol | No | ≤5 kW | Methanol crossover |
MCFC | 650–700 | H2, CO | Yes | 120 kW–10 MW | S poisoning, cycling effects, long start-up time |
SOFC | 500–1000 | H2, CO | Yes | ≤10 MW | S poisoning, cycling effects, mechanically fragile, long start-up time |
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Mallouppas, G.; Yfantis, E.A. Decarbonization in Shipping Industry: A Review of Research, Technology Development, and Innovation Proposals. J. Mar. Sci. Eng. 2021, 9, 415. https://doi.org/10.3390/jmse9040415
Mallouppas G, Yfantis EA. Decarbonization in Shipping Industry: A Review of Research, Technology Development, and Innovation Proposals. Journal of Marine Science and Engineering. 2021; 9(4):415. https://doi.org/10.3390/jmse9040415
Chicago/Turabian StyleMallouppas, George, and Elias Ar. Yfantis. 2021. "Decarbonization in Shipping Industry: A Review of Research, Technology Development, and Innovation Proposals" Journal of Marine Science and Engineering 9, no. 4: 415. https://doi.org/10.3390/jmse9040415
APA StyleMallouppas, G., & Yfantis, E. A. (2021). Decarbonization in Shipping Industry: A Review of Research, Technology Development, and Innovation Proposals. Journal of Marine Science and Engineering, 9(4), 415. https://doi.org/10.3390/jmse9040415