Evaluation of the Applicability of Synthetic Fuels and Their Life Cycle Analyses
Abstract
:1. Introduction
2. Methodology of the Evaluation
2.1. Evaluation Criteria: Fuel Properties and Requirements for the Application of New Fuels
2.2. Evaluation Criteria: Integration into the Transport System and Fuel Infrastructure
2.3. Evaluation Criteria: Ecological Analysis (LCA)
3. Sustainable Aviation Fuels (SAFs)
3.1. Requirements for the Application of SAFs
3.2. Usage and Infrastructure for SAF
3.3. Ecological Analysis (LCA)
3.4. High-Potential Synthetic Fuels for Use in Aviation
3.5. Conclusions
4. Synthetic Fuels for Maritime Transport
4.1. Requirements for the Application of Synthetic Maritime Fuels
4.2. Usage and Infrastructure of Synthetic Maritime Fuels
4.3. Ecological Analysis (LCA)
4.4. High Potential Synthetic Fuels for Use in Maritime Transport
4.5. Conclusions
5. Synthetic Fuels for Road Transport
5.1. Requirements for the Application of Synthetic Fuels in Road Transport
5.2. Integration into the Road Transport System and Fuel Infrastructure
5.3. Ecological Analysis (LCA)
5.4. Outlook for the Use of Synthetic Fuels in Heavy-Duty Transport
5.5. High-Potential Synthetic Fuels for Use in Passenger Transport
5.6. Conclusions
6. Concluding Remarks and Outlook
Author Contributions
Funding
Data Availability Statement
Acknowledgments
Conflicts of Interest
References
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Synthetic Diesel | Synthetic Gasoline | Synthetic Kerosene | Ether | Alcohols | Gases | |||||||
---|---|---|---|---|---|---|---|---|---|---|---|---|
FT-Diesel * | FT Gasoline | MtG ** | FT Kerosene | MtJ | DME | OME3-5 | Methanol | Higher Alcohols | H2 | CH4 | NH3 | |
Standard | EN 15940 [22] (EN 590 [23]) | EN 228 [24] | ASTM D7566 [19] | -- | ISO 16861 b) [25] | -- | ASTM D5797 c) [26] | ASTM D7862 c),d) [27] | EN 17124 [28] | EN 16723-2 [29] + | -- | |
Appl.‡ | Heavy-duty vehicles | Passenger cars | Aviation | Heavy-duty vehicles, shipping | Road transport, shipping | Road transport, shipping | ||||||
Tb (°C) | 360 e) (FBP) | 210 e) (FBP) | 205...300 e) | g) | −24.8 e) | 105...280 h) | 65 f) | 99.5... 117.7 d),e) | −253 f) | −162 f) | −33.4 f) | |
Tf (°C) | −40...6 f) | −90.5...−95.4 f) | ≤−40 e) | g) | ≈−140 h) | −70... 48 h) | −98 f) | −89.5... −114.7 d),e) | −259 f) | −182 f) | −77.7 f) | |
ρ (kg/m³) | 765–810 e) (800–845 e)) | 720–775 e) | 730–770 e) | g) | gaseous | 961–1100 h) | 792 h) | 801–810 d),e),j) | 0.084 f) | 0.671 f) | 0.720 f) | |
FP (°C) | ≥55e) | ≤−35 f) | ≥38 e) | g) | −42.2 f) | 54–115 h) | 9 f) | 24...35 d),e) | -- | -- | -- | |
CN | ≥51 e) | -- | -- | -- | >55 e) | 63–100 h) | 5 h) | 17–25 d),h) | -- | -- | -- | |
ON | -- | ≥95 e) (RON) ≥85 e) (MON) | -- | -- | -- | -- | 109 i) (RON) 89 i) (MON) | 96–113 d),e) (RON) 78–94 d),e) (MON) | -- | ≥65 f) (MN) | -- | |
Hu (MJ/kg) | ≈44 h) | -- | ≥42.8 e) | g) | 27.60 h) | 17.5–20.3 h) | -- | -- | 120 k) | 50 k) | 18.6 k) | |
Hu (MJ/l) | -- | 30–33 i) | -- | g) | 18.44 h) | 19.5–19.7 h) | 15.8 i) | 26–27 d),i) 31.1 a),i) | 8.5 k) | 22 k) | 12.7 k) |
SAF 50%vol Blend | 100% SAF | |
---|---|---|
Fuel production | – Complex production process. – Side products. | – Complex production process. – Side products. |
Infrastructure availability | + Present infrastructure can be used. ● Open question if the unlimited use of infrastructure is possible, e.g., due to costs. | + Present infrastructure can be used. ● Open question if the unlimited use of infrastructure is possible, e.g., due to costs → parallel infrastructure at airports may be necessary. |
Applicability (drop-in/blend/engine customization) | + Comply with ASTM D7566 → completely compatible with existing fleet and technology. – Higher fuel costs. | + Regarding the technical point of view, compatible with existing fleet. + Higher efficiency in combustion. + If replacement of seals, fittings, valve, et cetera, is necessary, this can take place during regular inspections/maintenance. ● Possibly inspections/maintenance is more often necessary to secure the compatibility with the material. – No approval according to ASTM D7566. – Higher fuel costs. |
Pollutant emissions from usage | ● Less emissions compared with pure fossil jet fuel. | ● Significant reduction in emissions, including non-CO2 effects. |
GHG balance over the entire life cycle | ● Less emissions in future scenario compared with fossil fuel. | + Less emissions in the future scenario compared with the SAF 50%vol blend. |
R&D requirements |
|
|
FT-Diesel | Methane (LNG) | Methanol | OME | Hydrogen | Ammonia | |
---|---|---|---|---|---|---|
Fuel production | – Complex production process. – Side products. | + Fewer costs. + Production without side products possible. + CO2 active process. + Maximum energy content per C atom. | + Production without side products is possible. + CO2 active process. ● Energy content per C atom not as high as for diesel or LNG due to partially oxidized C atom. | ● Production via methanol → additional process steps. | + No DAC or other carbon source necessary. | + No DAC or other carbon source necessary. |
Infrastructure availability | + Present infrastructure can be used. | ● Global infrastructure partially existent. ● Up to now, fueling was only possible via bunker vessel, LNG terminals necessary. | ● Global infrastructure partially existent; expansion for maritime sector necessary. | – Not present; usage within existing systems depends on the amount of the admixture. | – Global infrastructure partially existent; expensive expansion for maritime sector necessary. | ● Global infrastructure partially existent; expansion for maritime sector necessary. |
Applicability (drop-in/blend/engine customization) | + Replacement for MGO/HFO (90% of all ships). ● Adjustment of engine control may be necessary. – Higher fuel costs. | + Replacement for fossil LNG. + Fewer fuel costs than FT-diesel. ● Share of LNG ships <10%. ● Usage competition with the energy sector. – Modifications of MGO/HFO engines necessary. – Lower energy density than diesel → larger tank necessary (would reduce capacity) or less range. | + Development of methanol ships is technically matured; single ships are already in use. + Promotion by global players. – Currently, no standard, only single permits. – Energy density half as much as diesel → larger tank necessary (would reduce capacity) or less range. – Nearly no existing ships; modification of MGO/HFO ships necessary. | – Maximum share of the admixture up to 15% due to compatibility with materials. | ● Single test cases but no technically mature ships. – Low energy density → low range. – Currently, no standard. | ● Usage competition with chemical industry, esp. fertilizer. – No compatibility with current engines and technology. – Currently, the technology is in development → no market-ready ships. – Toxic → application for cargo ships only. – Currently, no standard. |
Pollutant emissions from usage | + Less soot emissions compared with MGO/HFO. + No emissions of SOx. ● Reduction in emissions not as much as for other synthetic fuels. | + Significant reduction in emissions, e.g., complies with limits for NOx. + No emissions of SOx. – Risk of methane slip → has to be avoided. | + Significant reduction in emissions, eventually, no exhaust gas treatment will be necessary. + Largest potential for a reduction in soot emissions in the group of carbon containing fuels. + No emissions of SOx. | + Reduction in SOx and soot emissions when used as a blending component. | + No carbon containing emissions → no CO2 emissions. + No emissions of SOx. | + No carbon-containing emissions → no CO2 emissions. + No emissions of SOx. – Increased NOx emissions and emissions of N2O possible. |
GHG balance over the entire life cycle | ● Slightly higher GHG emissions. | + Relatively less GHG emissions. – CH4 emissions possible. | + Relatively less GHG emissions. | ● Slightly higher GHG emissions. | + No carbon-containing emissions. | + No carbon-containing emissions. – Emissions of N2O possible. |
R&D requirements |
|
|
|
|
|
|
FT-Diesel | Methane (LNG) | Methanol | OME | DME | |
---|---|---|---|---|---|
Fuel production | – High fuel costs. | + Low fuel costs. | ● Low fuel costs, but low calorific value. | – Moderate fuel costs and low calorific value. | ● Moderate fuel costs and moderate heating value. |
+ Very pure production possible. | |||||
Infrastructure availability | + Already partly available as blend (R33) a). ● Currently, (still) no existing fueling infrastructure for pure paraffinic diesel (EN 15940) in DE. + Required infrastructure can be set up with low capital expenditure. | ● Currently, only approx. 100 LNG refueling stations are available. | – Currently, no existing fueling infrastructure. | – Currently, no existing fueling infrastructure. | – Currently, no existing fueling infrastructure. |
Applicability (drop-in/blend/engine customization) | + Compliant with standards as a blend (R33) and can therefore be used in all diesel vehicles without conversion. ● Vehicles must be approved by the manufacturer for operation with pure paraffinic diesel (DIN EN 15940). + Many current engine generations are already approved, e.g., from Scania, Volvo, Mercedes, MAN, and others [62]. | + Direct replacement for fossil LNG. + LNG production vehicles available. ● Share of LNG SNF in the vehicle fleet <1%. | ● Individual test applications, but no production vehicles with EU approval are available yet. – Low energy density (shorter range). | ● Currently, only individual research applications. – Low energy density (shorter range). | ● Currently, only individual research applications. – Low energy density (shorter range). |
Pollutant emissions from vehicle use | + Reduced CO, soot, and HC emissions compared with conv. Diesel. | + Reduced CO and soot emissions compared with conv. Diesel. – Methane slip must be avoided. | + Reduced CO, soot, and HC emissions compared with conv. Diesel. | + Reduced soot emissions compared with conv. Diesel. | + Reduced soot emissions compared with conv. Diesel. |
GHG balance over the entire life cycle | ● GHG balance slightly higher due to the increased expenditure for fuel production. | + Lowest GHG footprint compared with electricity-based fuels, but high uncertainties due to methane slip. | + Relatively low GHG footprint compared with electricity-based fuels. | + Relatively low GHG footprint. | + Relatively low GHG footprint compared with electricity-based fuels. |
R&D requirements |
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Gasoline (FT/MtG) | Methane (CNG) | Methanol | |
---|---|---|---|
Fuel production | – High fuel costs. | + Low fuel costs. + Very pure production possible. | + Low fuel costs. ● Low calorific value. |
Infrastructure availability | + Compliant with DIN EN 228. → Existing infrastructure can be used. | ● Currently, only approx. 850 CNG filling stations are available. | – Currently, no existing fueling infrastructure. |
Applicability (drop-in/blend/engine customization) | + FT gasoline as a pure fuel is standard-compliant with DIN EN 228 and thus 100% drop-in-capable. | + Synth. methane as a pure fuel is standard-compliant with DIN EN 16723-2 and thus 100% drop-in-capable. | ● Individual test applications, but no production vehicles with EU approval are available yet. |
Pollutant emissions from vehicle use | + Predominantly reduced NOx, CO, soot, and HC emissions compared with conv. gasoline. + Fuel behaves neutrally in application. | + Reduced CO and soot emissions compared with conv. gasoline. – Methane slip must be avoided. | + Reduced CO, soot, and HC emissions compared with conv. gasoline. + Effectiveness degree increase possible. |
GHG balance over the entire life cycle | ● GHG balance slightly higher due to increased expenditure for fuel production. | + Relatively low GHG emissions, but high uncertainties due to methane slip. | + Relatively low GHG emissions. |
R&D requirements |
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Richter, S.; Braun-Unkhoff, M.; Hasselwander, S.; Haas, S. Evaluation of the Applicability of Synthetic Fuels and Their Life Cycle Analyses. Energies 2024, 17, 981. https://doi.org/10.3390/en17050981
Richter S, Braun-Unkhoff M, Hasselwander S, Haas S. Evaluation of the Applicability of Synthetic Fuels and Their Life Cycle Analyses. Energies. 2024; 17(5):981. https://doi.org/10.3390/en17050981
Chicago/Turabian StyleRichter, Sandra, Marina Braun-Unkhoff, Samuel Hasselwander, and Sofia Haas. 2024. "Evaluation of the Applicability of Synthetic Fuels and Their Life Cycle Analyses" Energies 17, no. 5: 981. https://doi.org/10.3390/en17050981
APA StyleRichter, S., Braun-Unkhoff, M., Hasselwander, S., & Haas, S. (2024). Evaluation of the Applicability of Synthetic Fuels and Their Life Cycle Analyses. Energies, 17(5), 981. https://doi.org/10.3390/en17050981