CG H2 | Pipeline | LH2 | LOHC | ||||||
---|---|---|---|---|---|---|---|---|---|
2020 | 2050 | 2020 | 2050 | 2020 | 2050 | 2020 | 2050 | ||
H2 Production | €/kg | 8.11 | 4.69 | 8.11 | 4.69 | 8.11 | 4.69 | 8.11 | 4.69 |
Hydrogenation | €/kg | – | – | – | – | – | – | 0.93 | 0.26 |
Liquefaction | €/kg | – | – | – | – | 3.10 | 2.48 | – | – |
Compression | €/kg | 0.70 | 0.42 | 0.64 | 0.28 | – | – | – | – |
Storage | €/kg | 0.32 | 0.29 | 0.32 | 0.29 | 0.13 | 0.31 | 0.57 | 0.54 |
Transport | €/kg | 0.82 | 0.58 | 1.22 | 1.26 | 0.23 | 0.22 | 0.36 | 0.32 |
Dehydrogenation | €/kg | – | – | – | – | – | – | 3.67 | 1.85 |
Refueling Station | €/kg | 5.38 | 1.85 | 4.88 | 1.75 | 3.69 | 1.26 | 4.99 | 2.00 |
LOHC Production | €/kg | – | – | – | – | – | – | 0.02 | 0.02 |
Supply costs | €/kg | 13.21 | 7.94 | 12.77 | 8.27 | 13.38 | 8.97 | 13.85 | 9.69 |
Difference 7% IR | €/kg | − 0.44 | − 0.18 | − 0.52 | − 0.27 | − 0.49 | − 0.25 | − 0.60 | − 0.26 |
Difference 9% IR | €/kg | 0.45 | 0.18 | 0.53 | 0.28 | 0.50 | 0.26 | 0.62 | 0.27 |