Comparison of hydrogen storage technologies: capacity, energy density, consumption, safety, cost, and challenges
Technology . | Storage Capacity (kg H2/m³) . | Energy Density (kWh/kg) . | Energy Consumption (kWh/kg) . | Safety (Pressure/Temperature) . | Cost (USD/kg H2) . | Advantages . | Challenges . | Citations . |
---|---|---|---|---|---|---|---|---|
Compressed Gas | ~20–40 | ~33 | 10–15 | 350–700 bar | 5–10 | Well-established, mature technology | Low volumetric density, requires high pressure (350–700 bar) | [133] |
Liquefied Hydrogen | ~71 | ~40 | 12–20 (liquefaction) | −253°C storage | 15–20 | High storage density, ideal for large volumes | High energy consumption for liquefaction, boil-off losses | [134] |
Metal Hydrides | ~100–150 | ~7–15 | 5–10 (thermal cycling) | ~10 bar, 300°C | 10–20 | High volumetric storage, reversible storage | Heavy, slow release kinetics, thermal management required | [136] |
MOFs | ~30–60 | ~33 | 5–8 (adsorption/desorption) | Low-pressure operation | >20 | Tunable storage properties, lightweight | Expensive materials, low energy density | [137] |
Chemical Storage (complex hydrides) | ~85–150 | ~5–10 | 6–12 (dehydrogenation) | ~1–10 bar, 100–200°C | 10–15 | High hydrogen content, easier to transport | Complex handling, energy required for hydrogen release | [138] |
Technology . | Storage Capacity (kg H2/m³) . | Energy Density (kWh/kg) . | Energy Consumption (kWh/kg) . | Safety (Pressure/Temperature) . | Cost (USD/kg H2) . | Advantages . | Challenges . | Citations . |
---|---|---|---|---|---|---|---|---|
Compressed Gas | ~20–40 | ~33 | 10–15 | 350–700 bar | 5–10 | Well-established, mature technology | Low volumetric density, requires high pressure (350–700 bar) | [133] |
Liquefied Hydrogen | ~71 | ~40 | 12–20 (liquefaction) | −253°C storage | 15–20 | High storage density, ideal for large volumes | High energy consumption for liquefaction, boil-off losses | [134] |
Metal Hydrides | ~100–150 | ~7–15 | 5–10 (thermal cycling) | ~10 bar, 300°C | 10–20 | High volumetric storage, reversible storage | Heavy, slow release kinetics, thermal management required | [136] |
MOFs | ~30–60 | ~33 | 5–8 (adsorption/desorption) | Low-pressure operation | >20 | Tunable storage properties, lightweight | Expensive materials, low energy density | [137] |
Chemical Storage (complex hydrides) | ~85–150 | ~5–10 | 6–12 (dehydrogenation) | ~1–10 bar, 100–200°C | 10–15 | High hydrogen content, easier to transport | Complex handling, energy required for hydrogen release | [138] |
Comparison of hydrogen storage technologies: capacity, energy density, consumption, safety, cost, and challenges
Technology . | Storage Capacity (kg H2/m³) . | Energy Density (kWh/kg) . | Energy Consumption (kWh/kg) . | Safety (Pressure/Temperature) . | Cost (USD/kg H2) . | Advantages . | Challenges . | Citations . |
---|---|---|---|---|---|---|---|---|
Compressed Gas | ~20–40 | ~33 | 10–15 | 350–700 bar | 5–10 | Well-established, mature technology | Low volumetric density, requires high pressure (350–700 bar) | [133] |
Liquefied Hydrogen | ~71 | ~40 | 12–20 (liquefaction) | −253°C storage | 15–20 | High storage density, ideal for large volumes | High energy consumption for liquefaction, boil-off losses | [134] |
Metal Hydrides | ~100–150 | ~7–15 | 5–10 (thermal cycling) | ~10 bar, 300°C | 10–20 | High volumetric storage, reversible storage | Heavy, slow release kinetics, thermal management required | [136] |
MOFs | ~30–60 | ~33 | 5–8 (adsorption/desorption) | Low-pressure operation | >20 | Tunable storage properties, lightweight | Expensive materials, low energy density | [137] |
Chemical Storage (complex hydrides) | ~85–150 | ~5–10 | 6–12 (dehydrogenation) | ~1–10 bar, 100–200°C | 10–15 | High hydrogen content, easier to transport | Complex handling, energy required for hydrogen release | [138] |
Technology . | Storage Capacity (kg H2/m³) . | Energy Density (kWh/kg) . | Energy Consumption (kWh/kg) . | Safety (Pressure/Temperature) . | Cost (USD/kg H2) . | Advantages . | Challenges . | Citations . |
---|---|---|---|---|---|---|---|---|
Compressed Gas | ~20–40 | ~33 | 10–15 | 350–700 bar | 5–10 | Well-established, mature technology | Low volumetric density, requires high pressure (350–700 bar) | [133] |
Liquefied Hydrogen | ~71 | ~40 | 12–20 (liquefaction) | −253°C storage | 15–20 | High storage density, ideal for large volumes | High energy consumption for liquefaction, boil-off losses | [134] |
Metal Hydrides | ~100–150 | ~7–15 | 5–10 (thermal cycling) | ~10 bar, 300°C | 10–20 | High volumetric storage, reversible storage | Heavy, slow release kinetics, thermal management required | [136] |
MOFs | ~30–60 | ~33 | 5–8 (adsorption/desorption) | Low-pressure operation | >20 | Tunable storage properties, lightweight | Expensive materials, low energy density | [137] |
Chemical Storage (complex hydrides) | ~85–150 | ~5–10 | 6–12 (dehydrogenation) | ~1–10 bar, 100–200°C | 10–15 | High hydrogen content, easier to transport | Complex handling, energy required for hydrogen release | [138] |
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