Reference Tables
Comparison of PEM, alkaline, and emerging electrolyzer technologies covering efficiency, load flexibility, capex, and balance-of-plant.
Electrolyzer Technology Comparison · Refs: IEA 2023, IRENA 2020, NREL 2022, Buttler & Spliethoff 2018
| Parameter | Alkaline (AEL) | PEM | SOEC | Notes / Reference |
|---|---|---|---|---|
| Technology maturity (TRL) | 9 (commercial) | 8-9 (commercial) | 6-7 (demo/early) | IEA 2023 |
| Typical stack size (single) | 0.5 - 6 MW | 0.1 - 5 MW | up to 2.6 MW (Sunfire) | Vendor datasheets 2024 |
| Cell stack lifetime | 60,000 - 90,000 hr | 50,000 - 80,000 hr | 20,000 - 40,000 hr | IRENA 2020 |
| Stack efficiency (LHV) | 63 - 71% | 60 - 68% | 75 - 85% | NREL 2022 |
| System efficiency (LHV) | 51 - 60% | 46 - 60% | 76 - 81% (high-T) | With BoP losses |
| Specific energy | 50-78 kWh/kg H2 | 50-83 kWh/kg H2 | 39-50 kWh/kg H2 | At nominal load; theoretical LHV = 33.3 kWh/kg |
| Operating temperature | 60-90 C | 50-80 C | 700-850 C | SOEC needs heat integration |
| Operating pressure | 1-30 bar | 15-80 bar | 1-15 bar (prototype) | PEM highest pressure |
| Current density | 0.2-0.6 A/cm2 | 1.0-2.5 A/cm2 | 0.3-1.0 A/cm2 | Higher j -> smaller stack |
| Load range (% nominal) | 15-100% | 5-120% | 30-125% | PEM best for variable renewable |
| Cold start time | 50 min - 2 hr | 5-15 min | hours | SOEC penalized by thermal cycling |
| Ramp rate | 0.2-20%/s | up to 100%/s | slow | PEM best dynamic response |
| Stack CAPEX (2024) | $250-450/kW | $700-1400/kW | $2800-4700/kW | IEA 2023 price drop ongoing |
| System CAPEX (2024) | $500-1100/kW | $1100-2100/kW | $3500-6500/kW | Full package inc BoP |
| Key consumables | 30% KOH | Platinum, Iridium, PFSA membrane | Ni cermet, YSZ ceramic | PEM PGM bottleneck |
| Water quality | Type II (5 microS/cm) | Type I / ASTM D1193 (>1 MOhm-cm) | Steam-quality | PEM strict |
| H2 purity (stack out) | 99.5 - 99.9% | >99.99% | >99.9% | PEM less KOH carryover |
| H2 purity (after dryer) | >99.999% | >99.999% | >99.999% | PSA or TSA added |
| O2 impurity in H2 | <2% (at turndown) | <0.1% | <0.5% | Alkaline limits low load |
| Footprint (rel. PEM) | 1.5 - 2x | 1x baseline | 0.8 - 1.2x | Alkaline is largest |
| Response to curtailment | Limited | Excellent | Poor (thermal stress) | PEM best for solar/wind |
| Degradation rate | 0.25-1.5 uV/hr | 0.5-3 uV/hr | 6-50 uV/hr | Bohlen CIRED 2019 meta |
| Safety concerns | Caustic KOH leaks; H2/O2 mixing at turndown | PFSA membrane fire risk; HF gas on decomposition | High T; thermal shock | Hazardous area Class 1 Div 2 minimum |
| SELECTION HEURISTICS | ||||
| Grid-connected, steady baseload, >10 MW | ||||
| Directly coupled to PV/wind with heavy curtailment | ||||
| Industrial site with abundant 500-900 C waste heat | ||||
| H2 fueling station (need >30 bar, compact) | ||||
| Remote/marine site, minimal maintenance | ||||
| Rapid deployment, modular skids | ||||
| High purity for semiconductor / fuel cell grade |
Source: PEM_vs_Alkaline_Electrolyzer_Reference_v1.xlsx
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