Submitted:
13 May 2025
Posted:
14 May 2025
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Abstract
Keywords:
1. Introduction
1.1. Green Ammonia Market
1.2. H2 Transportation and Related Technologies
- Compressed gas tubes (tube trailers): This method is used to transport hydrogen in gaseous form over short distances, typically supplying industrial users or hydrogen refueling stations.
- Hydrogen pipelines: This method is one of the most efficient and cost-effective for long-distance hydrogen transport. Made from materials that can safely contain hydrogen, pipelines use strategically placed compressor stations along their routes to maintain pressure and control flow, enhancing efficiency.
- Liquefied hydrogen (LH2): This method involves cooling hydrogen to extremely low temperatures (-253°C or -423°F) to convert it into a dense liquid that occupies less space. Specialized cryogenic containers and tankers are used for LH2 transportation. Although the liquefaction process is energy-intensive, it offers a viable option for long-distance transport due to the reduced volume of liquid hydrogen.
- Liquid organic hydrogen carriers (LOHCs): LOHCs are organic compounds that absorb and release hydrogen through chemical reactions, allowing hydrogen to be stored and transported under ambient temperature and pressure conditions without significant losses. When needed, the hydrogen-rich LOHC is heated to the dehydrogenation temperature and exposed to a dehydrogenation catalyst to release hydrogen. However, handling LOHCs involves potential environmental exposure and fire risks, as they are flammable hydrocarbons.
- Ammonia: Traditionally used in various industries, ammonia is gaining attention as a promising hydrogen carrier due to its well-established international trade networks [14]. Although both ammonia and hydrogen are gaseous at standard conditions, ammonia is more efficient in delivering hydrogen over long distances after liquefaction. A liter of liquid ammonia contains a greater mass of hydrogen than a liter of liquid hydrogen because ammonia has a higher packing density of approximately 686 kg/m³ compared to 71.1 kg/m³ for liquid hydrogen. Although its hydrogen content by weight is only 17.65% compared to 100% for liquid hydrogen, ammonia’s volumetric hydrogen content (107.7 kgH2/m³) significantly exceeds that of liquid hydrogen (70.8 kgH2/m³) and LOHC (47.1 kgH2/m³), making it a more efficient carrier.
2. Technical Background
2.1. Energy Storage Solutions
2.1.1. BESSs
2.1.2. Hydrogen and Ammonia Energy Carriers as a Long-Term and Flexible Energy Storage Solution
2.2. Green Ammonia Production
2.2.1. Air Separation and Nitrogen Extraction
2.2.2. Electrolysis and Green Hydrogen Production
- Electrolyzer technologies and efficiencies: The key electrolyzer technologies include alkaline electrolyzers, proton-exchange membrane (PEM) electrolyzers, and solid oxide electrolyzers (SOECs). Alkaline and PEM electrolyzers are the most commercially mature options, achieving electrical-to-hydrogen conversion efficiencies of approximately 60%–70%. SOECs, on the other hand, operate at high temperatures and have the potential to reach even higher efficiencies – up to 80% or more – though they remain in the early stages of commercialization. The choice of technology depends on factors such as efficiency requirements, operational conditions, and system integration needs.
- Thermodynamic and operational challenges: The water-splitting process requires significant energy input (~237 kJ/mol under standard conditions), which must be supplied by intermittent renewable energy sources. This intermittency poses operational challenges for electrolyzers, such as fluctuating load factors that can impact efficiency and system reliability. To address these challenges, innovative strategies are being developed, including dynamic load-following operations and hybrid energy storage solutions. These approaches aim to ensure cost competitiveness while enabling seamless integration with variable renewable electricity supplies.
- Advancements in research and development: Significant research efforts are focused on improving the design and performance of electrolyzer cells to enhance efficiency, reduce capital costs, and extend operational lifetimes. Additionally, the development of advanced control systems is critical for managing power input fluctuations caused by renewable energy variability. These innovations are essential for reducing energy losses, maintaining stable production rates, and ensuring the economic viability of green ammonia facilities under real-world operating conditions.
2.2.3. Ammonia Haber-Bosch Reaction and Purification
2.2.4. Ammonia Storage and Transportation
2.3. Green Ammonia Technical and Economic Considerations
3. Regulatory Requirements on Clean Hydrogen
3.1. Regional Clean Hydrogen Emission Standards
- Achieve a GHG emissions intensity of 20g CO2e/MJLHV or less.
- Calculate GHG emissions up to the ‘point of production.’
- Provide a risk mitigation plan for fugitive hydrogen emissions.
- Meet additional requirements for biogenic inputs, where relevant and appropriate for the feedstock source and classification.

3.2. Challenges for Green Ammonia Hubs
| Production method | Scope | Year issued | Current status | Emissions intensity [kgCO2/kgH2] | ||
|---|---|---|---|---|---|---|
| EU | EU Taxonomy | All | Well-to-gate | 2021 | Operational | 3.0 |
| RED II | Renewable electricity, low carbon electricity (<65 gCO2,eq/kWh) | Well-to-wheel | 2023 | Under development | 3.4 | |
| UK | UK Low Carbon Hydrogen Standard | Electrolysis, natural gas with CCUS, biomass and waste | Well-to-gate | 2022 | Operational | 2.4 |
| Renewable Transport Fuel Obligation (RTFO) | Renewable energy, excluding bioenergy | Well-to-point of delivery | 2021 | Operational | 4.0 | |
| U.S. | Clean Hydrogen Production Tax Credit | All | Well-to-gate | 2022 | Under development | 2.5 - 4 1.5 – 2.5 0.45 – 1.5 < 0.45 |
| CA | Clean Hydrogen Investment Tax Credit | Electrolysis, natural gas with CCUS | Well-to-gate | 2022 | Under development | 2 – 4 0.75 – 2 < 0.75 |
| FR | France Ordinance No. 2021 - 167 | All | Well-to-gate | 2021 | Under development | 3.38 |
4. Materials and Methods
4.1. 100% Hydrogen-Ready Internal Combustion Engines

4.2. Economic and Technical Aspects of the Technology
5. Case Studies
6. Discussion
7. Conclusions
Author Contributions
Funding
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| H2-Engine | H2-FC | Redox flow | Li-Ion | |
|---|---|---|---|---|
| Storage system | Compressed hydrogen (400 bar) | Compressed hydrogen (400 bar) | Electrolyte tanks | Battery cells |
| Re-electrification | ICE | PEM fuel cell | Power electronics | Power electronics |
| Total round trip efficiency | 25% | 28% | 72% | 90% |
| CAPEX storage (€/kWh) | 1.2 | 1.2 | 36 | 45 |
| CAPEX re-electrification (€/kW) | 3,800 | 35 | 35 | |
| Calendar lifetime storage (a) | 30 | 30 | 25 | 13 |
| Calendar lifetime re-electrification (a) | 25 | 10 | 50 | 50 |
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