Synthetic Fuels for Decarbonising UK Rural Transport
Definition
:1. Introduction
2. Overview of Synthetic Fuels
2.1. Production Processes of Synthetic Fuels
2.1.1. Type-1 Synthesis: Hydrogen Addition
2.1.2. Type-2 Synthesis: Carbon Rearrangement
- Sabatier Process: The Sabatier reaction involves converting carbon dioxide (CO2) into methane (CH4) by reacting it with hydrogen using a catalytic process. If the hydrogen used is derived from renewable energy sources, the Sabatier process can significantly reduce overall CO2 emissions compared to fossil-based natural gas systems. Specifically, for every gramme of synthetic methane produced via the Sabatier process, approximately 1.5 g of CO2 are captured from existing sources. The CO2 generated during the process itself is about 0.2–0.3 g per gramme of methane produced, which arises primarily from the energy inputs needed to produce hydrogen through electrolysis and to heat the reactors. Thus, the net CO2 reduction achieved through the Sabatier process is approximately 1.2–1.3 g per gramme of methane produced, assuming renewable energy is utilised for the production of hydrogen. This highlights the significant potential of the Sabatier process to contribute to carbon neutrality when paired with renewable energy sources [35].
- Pyrolysis of Biomass: Pyrolysis is a thermal decomposition process where biomass is converted into bio-oil, syngas, and biochar in the absence of oxygen. This process can offer a near-zero or even carbon-negative net lifecycle emissions profile if sustainably managed biomass feedstocks are used. During biomass growth, approximately 1.8 g of CO2 are absorbed for each gramme of synthetic fuel produced, thereby sequestering carbon from the atmosphere. The pyrolysis process itself generates around 0.6 g of CO2 per gramme of fuel produced due to energy demands during thermal conversion. Consequently, the net CO2 removal through biomass pyrolysis is approximately 1.2 g per gramme of synthetic fuel produced. Furthermore, the by-products of pyrolysis, such as biochar, can be applied to soil for carbon sequestration, which further enhances the carbon-negative potential of the process. This makes biomass pyrolysis a promising pathway for carbon reduction, especially when feedstocks are sourced sustainably [36,37].
- Upgrading of Heavy Oils: Upgrading heavy oils involves breaking down long-chain hydrocarbons into shorter, more usable fuel fractions. This process is inherently CO2-intensive due to the significant energy inputs required to achieve the desired chemical transformations. Specifically, for every gramme of upgraded synthetic fuel produced, approximately 2.5 g of CO2 are emitted. This substantial carbon footprint arises from the high temperatures and pressures required during upgrading. However, employing carbon capture and storage (CCS) at the upgrading facility can reduce net emissions to approximately 1.5 g of CO2 per gramme of fuel. Even with CCS, upgrading heavy oils results in a positive CO2 footprint, which is higher compared to synthetic fuels produced from biomass or through hydrogenation methods such as the Sabatier process. This makes heavy oil upgrading the least favourable of the three in terms of net carbon reduction, underscoring the need for further improvements in efficiency or carbon mitigation strategies [38].
2.2. Benefits and Challenges of Synthetic Fuels
Synthetic Fuels Offer Several Advantages in the Context of Decarbonising Transport
- Compatibility with Existing Infrastructure: Synthetic fuels can be used in existing internal combustion engines and fuel distribution systems with minimal modifications, facilitating a smoother transition from fossil fuels [40].
- Reduction of Greenhouse Gas Emissions: Lifecycle assessments (LCA) highlight that infrastructure development, such as reactors for pyrolysis and Sabatier processes, can result in considerable CO2 emissions during construction. However, once operational, these facilities have the potential to produce sustainable fuels with significantly lower lifecycle emissions. For example, ref. [41] found that aviation fuels derived from microalgae-based pyrolysis reduce total energy consumption by 27.88% over the fuel’s lifecycle compared to conventional aviation fuels. Moreover, sustainable infrastructure development, when incorporating renewable energy sources and eco-friendly materials, can lower upfront emissions by 20–30%, further minimising the long-term environmental footprint of synthetic fuel production. By optimising infrastructure and integrating low-carbon energy sources, the overall lifecycle CO2 emissions from synthetic fuel production can be substantially reduced, making these pathways both more competitive and environmentally sustainable. It is important to recognise that while synthetic fuels can drastically reduce emissions during operation, the initial construction of supporting infrastructure—such as electrolysis plants, storage facilities, and pipelines—does contribute to CO2 emissions. However, these emissions are primarily “front-loaded”, incurred mostly during the construction phase. Once operational, these systems have significantly lower emissions compared to traditional fossil fuel infrastructure [36]. Over time, the lifecycle CO2 impact of synthetic fuels becomes even more favourable as operational emissions are much lower than those of fossil fuels. As construction techniques evolve and more renewable energy is integrated into the production and distribution processes, the emissions from synthetic fuel production will decrease further [38]. This long-term reduction underscores the environmental viability of synthetic fuel pathways, particularly as they move toward carbon neutrality [39].
- Energy Security: Synthetic fuels can be produced from a variety of feedstocks, including renewable electricity, biomass, and waste, reducing dependence on imported fossil fuels and enhancing energy security [41].
- High Production Costs: The current production methods for synthetic fuels, particularly those involving electrolysis, are expensive due to the high cost of electrolysers and other catalysts. Reducing these costs through technological advancements is crucial for the economic viability of synthetic fuels [16,42].
- Energy Efficiency: Direct electrification through EVs offers the highest energy efficiency, typically ranging from 80–90%. In contrast, converting renewable electricity into hydrogen via electrolysis and then into synthetic fuels through processes such as Fischer-Tropsch synthesis results in significantly lower efficiencies, around 30–50%, due to energy losses during each conversion stage [36]. Although EVs are the most efficient option, synthetic fuels remain essential for sectors where direct electrification is not feasible, such as aviation and long-haul shipping. For instance, ref. [41] reported an energy efficiency of 86.29% for microalgae-based biofuels using the pyrolysis after lipid extraction pathway, demonstrating a highly competitive energy conversion efficiency compared to other biofuel processes. The energy consumption ratio (ECR) of 0.1008 for Isochrysis-based fuels further highlights their favourable energy output relative to input. Additionally, co-pyrolysis processes, with energy efficiencies between 71–75%, provide a viable alternative for bio-refineries, particularly for producing liquid fuels for sectors such as aviation, where electrification is impractical but high energy conversion efficiency remains critical. In addition to the favourable energy efficiency of co-pyrolysis processes (71–75%) and microalgae-based biofuels using the pyrolysis after lipid extraction pathway with an energy efficiency of 86.29%, the potential for CO2 mitigation in pyrolysis pathways must also be considered. Ref. [41] assessed the lifecycle greenhouse gas (GHG) emissions for these processes and found that the lipid extraction pathway for Isochrysis produces 68.03 g CO2e/MJ—significantly lower than direct pyrolysis pathways (R1). This advanced process reduces total energy input and fossil fuel consumption by up to 37% compared to other pyrolysis methods. Comparatively, the lipid extraction pathway results in a 30% reduction in CO2 emissions compared to direct pyrolysis due to its higher energy efficiency and yield, underscoring the environmental benefits of this approach [41]. These findings indicate that advanced pyrolysis technologies, such as lipid extraction followed by pyrolysis, can serve as a critical solution for reducing CO2 emissions, particularly in sectors such as aviation, where electrification is less viable and synthetic fuels play a pivotal role. Table 2 compares different fuel pathways based on well-to-wheel efficiency, CO2 emissions, and energy consumption ratio (ECR).
Fuel Pathway | Well-to-Wheel Efficiency (%) | CO2 Emissions (g CO2e/MJ) | Energy Consumption Ratio (ECR) |
---|---|---|---|
EV (Direct Electrification) | 80–90 | - | - |
Hydrogen (Electrolysis + Conversion) | 30–50 | - | - |
Synthetic Fuels (Fischer-Tropsch) | 30–50 | - | - |
Microalgae Pyrolysis (Isochrysis, R2) | 86.29 | 68.03 | 0.1008 |
Co-Pyrolysis (Bio-refinery) | 71–75 | Varies (higher) | Varies |
- End-of-Life Management: Ref. [41] highlighted the importance of considering end-of-life strategies in synthetic fuel production systems, particularly when managing by-products such as pyrolysis char and other carbon-rich residues. Char produced during the pyrolysis process can be repurposed as a soil amendment, offering dual benefits [37]. Not only does it enhance soil quality, but it also contributes to carbon sequestration, thereby significantly reducing the overall environmental footprint of the process. Moreover, innovative approaches to recycling infrastructure materials are being explored to mitigate the environmental impact of synthetic fuel production further. For instance, repurposing pyrolysis char for carbon sequestration adds another layer of environmental benefit to the synthetic fuel lifecycle [42,43]. Advances in bio-refinery design, which emphasise waste minimisation and resource recovery, are proving to be essential in ensuring the sustainability of synthetic fuel infrastructure over the long term.End-of-life management for renewable energy infrastructure presents its own set of challenges. For example, wind turbine blades—typically made from fibreglass or carbon fibre composites—are difficult to recycle due to their complex material makeup. Similarly, solar panels contain materials such as silicon, glass, and metals that are energy-intensive to recycle [36]. However, new recycling technologies are emerging to address these issues. For instance, biodegradable composites are being developed for turbine blades and pilot projects are testing methods to repurpose decommissioned blades for use in civil engineering applications. Likewise, advances in solar panel recycling technologies are significantly improving the recovery rates of valuable materials such as silicon and silver [35].
3. Applications of Synthetic Fuels in Rural Transport
3.1. Supporting Agricultural and Heavy-Duty Vehicles
3.2. Enhancing Rural Mobility
3.3. Leveraging Existing Fuel Distribution Networks
3.4. Addressing Energy Security in Rural Areas
3.5. Preservation of Rural Heritage and Lifestyle
4. Establishing an Effective Synthetic Fuels Supply Chain
4.1. Localised Production and Renewable Integration
4.2. Efficient Distribution Networks
4.3. Storage and Supply Management
4.4. Community Involvement and Cooperative Models
4.5. Scalability and Flexibility
4.6. Regulatory Compliance and Incentives
4.7. Economic Viability and Long-Term Sustainability
4.8. Meeting Rural Mobility Needs
5. Potential Role of Community-Based Cooperatives in Synthetic Fuel Proliferation
6. Conclusions
Funding
Data Availability Statement
Acknowledgments
Conflicts of Interest
References
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Synthetic Fuel Production Process | CO2 Captured (g per g fuel) | CO2 Generated (g per g fuel) | Net CO2 Balance (g per g fuel) | Key Considerations |
---|---|---|---|---|
Sabatier Process | 1.5 | 0.2–0.3 | −1.2 to −1.3 | Dependent on renewable hydrogen production. Significant net reduction is achievable with green hydrogen. |
Pyrolysis of Biomass | 1.8 | 0.6 | −1.2 | Carbon-negative potential with sustainably managed biomass. Biochar can further sequester carbon. |
Upgrading of Heavy Oils | 0 | 2.5 | +1.5 (with CCS: +1.0) | Most CO2-intensive. CCS can mitigate emissions but still results in a net positive CO2 footprint. |
Stage | Key Success Factors | Technical Elements to Address |
---|---|---|
1. Localised Production and Renewable Integration | Utilisation of local renewable resources, sustainable energy models | Site selection for production facilities, integration with local renewables [55,56] |
2. Efficient Distribution Networks | Accessibility, strategic placement of distribution points | Leveraging existing infrastructure, optimising logistics [57,58] |
3. Storage and Supply Management | Consistent fuel supply, handling seasonal demand fluctuations | Advanced storage solutions, demand forecasting [59] |
4. Community Involvement and Cooperative Models | Community engagement, shared ownership, economic reinvestment | Cooperative structures, community education, and involvement [60] |
5. Scalability and Flexibility | Adaptability to demand growth and expansion capabilities | Modular infrastructure design, technology upgradability [61] |
6. Regulatory Compliance and Incentives | Alignment with regulations, financial support | Environmental compliance, securing subsidies and incentives [62,63] |
7. Economic Viability and Long-term Sustainability | Cost-effectiveness, access to financing, long-term benefits | Cost-benefit analysis, financing options, improving production efficiency [64,65] |
8. Meeting Rural Mobility Needs | Addressing specific rural transport requirements, ease of integration | Compatibility with existing ICE vehicles, ensuring fuel availability [66] |
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Dabo, A.-A.A.; Gough, A.; Alparslan, F.F. Synthetic Fuels for Decarbonising UK Rural Transport. Encyclopedia 2024, 4, 1553-1567. https://doi.org/10.3390/encyclopedia4040101
Dabo A-AA, Gough A, Alparslan FF. Synthetic Fuels for Decarbonising UK Rural Transport. Encyclopedia. 2024; 4(4):1553-1567. https://doi.org/10.3390/encyclopedia4040101
Chicago/Turabian StyleDabo, Al-Amin Abba, Andrew Gough, and F. Frank Alparslan. 2024. "Synthetic Fuels for Decarbonising UK Rural Transport" Encyclopedia 4, no. 4: 1553-1567. https://doi.org/10.3390/encyclopedia4040101
APA StyleDabo, A. -A. A., Gough, A., & Alparslan, F. F. (2024). Synthetic Fuels for Decarbonising UK Rural Transport. Encyclopedia, 4(4), 1553-1567. https://doi.org/10.3390/encyclopedia4040101