Green Chemical Systems

How Model Fidelity Changes Green Hydrogen LCOH

A critical note on how fixed-efficiency electrolyzer models and low-resolution renewable data can bias green-hydrogen LCOH estimates.

Problem: TEA can hide the operating physics between renewable power and LCOH

Green-hydrogen techno-economic analysis often has a simple computational chain:

renewable power time series
  -> electrolyzer model
  -> hydrogen production
  -> LCOH

The weak point is the middle of the chain. Many TEA studies use a fixed electrolyzer efficiency, so hydrogen production is treated as nearly proportional to input power:

m˙H2,t ≈ ηfixedPt HHVH2 .

That is convenient, but it hides load-dependent behavior. A PEM electrolyzer does not have one efficiency number. Its cell voltage and efficiency change with current density, part-load operation, overload, activation loss, ohmic loss, and diffusion loss. If a renewable-powered electrolyzer spends much of its time away from the design point, a fixed-efficiency TEA is not a harmless simplification.

The second simplification is temporal aggregation. Hourly wind and solar output contain zero-output periods, curtailment, short peaks, and overload opportunities. If the same resource profile is replaced by daily or monthly averages, the electrolyzer can appear to run more smoothly than it actually would. Hydrogen output and LCOH then become artifacts of the data resolution.

The paper asks a useful practical question: how much fidelity is needed in the electrolyzer model and renewable-data resolution before a green-hydrogen LCOH estimate becomes credible?

Where this paper sits

The contribution is a systematic comparison of TEA modeling choices:

fixed-efficiency PEMEL
  vs variable-efficiency I-V PEMEL

hourly renewable data
  vs daily averages
  vs monthly averages

WT, PV, and hybrid WT+PV systems
  under overload and minimum part-load assumptions

multi-year weather
  across Korea, China, Australia, and Germany

That makes the paper valuable as a bias study. It does not prove that one model is universally correct. It shows how seemingly modest modeling choices can move the economics by several percent, and in temporal-resolution cases by much more.

Modeling architecture

The framework is straightforward:

meteorological data
  -> wind speed, solar irradiance, ambient temperature
  -> WT and PV generation models
  -> fixed-efficiency or variable-efficiency PEMEL model
  -> hydrogen production
  -> CAPEX and OPEX
  -> LCOH
  -> scenario comparison

Wind generation is computed through a piecewise turbine power curve with cut-in, rated, and cut-out speeds. PV output uses irradiance and ambient-temperature-dependent module efficiency. The electrolyzer is then represented in two ways.

The fixed-efficiency model uses the efficiency at the design current density, i=2 A cm-2, for all operating points:

ηEL (i) = ηdesign .

The variable-efficiency model uses a steady-state I-V approximation:

Vcell = Erev + ηact + ηohm + ηdiff .

This is still not a full dynamic electrolyzer model. Thermal dynamics, start-up and shut-down behavior, pressure dynamics, ramp-rate constraints, and cycling-driven degradation are outside the model. The improvement is narrower: efficiency changes with operating current instead of being pinned to one design-point value.

The economic metric is LCOH. The paper assumes a 25-year lifetime, 7% discount rate, and 8000 h annual operating time. Those choices matter for absolute values, but the paper’s main point is the relative bias caused by model fidelity and time resolution.

Why fixed efficiency creates bias

A fixed-efficiency model is close to replacing an entire efficiency curve with one point. The accumulated hydrogen-production error can be read as:

ΔH = ∑t Pt [ ηvar (it) - ηdesign ] .

The sign is not predetermined. If the electrolyzer often operates at moderate part-load where the variable-efficiency model is better than the design-point efficiency, the fixed model underestimates hydrogen production. If the electrolyzer often operates in overload where ohmic and diffusion losses become larger, the fixed model can overestimate production by ignoring the efficiency penalty.

This is the most important nuance in the paper. The claim is not “variable efficiency always gives a more optimistic TEA.” In the baseline Korean cases, the variable-efficiency model gives higher hydrogen production and lower LCOH. WT falls from USD 6.02/kg to USD 5.73/kg, PV from USD 4.12/kg to USD 4.01/kg, and hybrid from USD 4.57/kg to USD 4.35/kg. But as overload increases, the advantage of the variable model shrinks because high-current operation carries an efficiency cost that the fixed model cannot see.

So the better statement is: fixed-efficiency bias is controlled by the distribution of current density, not by a universal direction of error.

Why temporal aggregation is dangerous

With hourly data, hydrogen production is computed as:

Hhourly = ∑t f (Pt) .

If the same interval is replaced by a daily or monthly average, the calculation becomes closer to:

Hagg = |T| f ( 1 |T| ∑t∈T Pt ) .

These are equal only under restrictive conditions. The function f is not linear; it contains renewable power conversion, current mapping, electrolyzer efficiency, capacity limits, overload rules, curtailment, and zero-output periods. Therefore f(E[P]) is not generally equal to E[f(P)].

The Korea hybrid case shows the scale of the problem:

Temporal resolution LCOH Hydrogen production
Hourly USD 4.35/kg 940 kg/h
Daily USD 3.79/kg 1066 kg/h
Monthly USD 3.57/kg 1125 kg/h

Daily and monthly aggregation make the system look smoother, more continuously operated, and cheaper. In this case they raise estimated hydrogen production by roughly 13% and 20%.

But again, the direction is not a theorem. The paper notes cases where the relationship between daily and monthly data is not monotone. Wind power is strongly nonlinear in wind speed, and averaging wind speed before applying a turbine power curve is not equivalent to averaging power. Temporal aggregation bias includes both renewable-generation nonlinearity and electrolyzer-operation nonlinearity. The paper would be stronger if it decomposed those two effects explicitly.

Hybrid WT+PV and variability

The hybrid result is intuitive. If wind and solar do not peak at the same times, the variance of combined renewable power can be lower than either single source after normalization:

Var (PWT+PPV) = Var(PWT) + Var(PPV) + 2Cov(PWT,PPV) .

The multi-year results are consistent with this. Hybrid systems have smaller year-to-year LCOH variation than WT-only or PV-only systems. For the hybrid case, the LCOH standard deviation is about USD 0.082/kg under the fixed model and USD 0.072/kg under the variable model.

This is useful, but not universal. Hybrid advantage depends on the local covariance structure. If wind and solar are simultaneously weak in a region or season, the smoothing effect can be much weaker.

What is reliable, and what is still weak

Several conclusions are structurally reliable:

  1. A fixed-efficiency model is a point approximation of a load-dependent electrolyzer curve.
  2. Temporal aggregation of a nonlinear operating model generally creates bias.
  3. WT+PV hybridization can reduce variability when wind and solar profiles are complementary.

The weaker part is the operational realism. The variable PEMEL model is steady-state. It does not model transient dynamics, cycling degradation, pressure dynamics, start-up and shut-down costs, thermal constraints, or warranty-limited overload behavior. The overload rule is also stylized, closer to a sensitivity assumption than a dispatch policy.

The sizing structure is another limitation. The electrolyzer capacity is fixed at 100 MW while renewable capacity is adjusted for LCOH. That is useful for isolating fidelity and resolution effects, but a real project would jointly size electrolyzer, PV, wind, storage, and possibly grid interaction. Once storage, PPA structure, curtailment compensation, hydrogen storage, and transport enter the problem, the value of hourly resolution may become even more coupled to system design.

The cross-country comparison should also be read carefully. A representative site in Korea, China, Australia, or Germany is not the same as a national resource assessment. The absolute ranking is less important than the repeated pattern: model fidelity and temporal resolution can move LCOH enough to change early project-screening decisions.

Critical take

The strongest part of this paper is its refusal to treat TEA inputs as neutral bookkeeping. Electrolyzer efficiency fidelity and renewable-data resolution are modeling choices, and those choices can become economic claims. In the baseline scenarios, variable-efficiency PEMEL modeling lowers LCOH by a few percent. In the temporal-resolution comparison, daily and monthly aggregation can overstate hydrogen output by much more.

The paper should not be read as proving that hourly data plus a variable-efficiency PEMEL model is always “correct.” It shows something narrower and more useful: when renewable intermittency and nonlinear electrolyzer physics are present, fixed efficiency and low-resolution data create structural bias. The size and direction of that bias depend on current-density distribution, renewable-resource distribution, capacity ratio, and overload rule.

For green-hydrogen screening, that is already enough. If a project is economically marginal, a few percent from electrolyzer fidelity and a 10-20% production shift from temporal aggregation are not details. They can change whether the project looks viable.

References

  • Kang, B., Kim, H., & Park, J. (2026). Impact of electrolyzer-model fidelity and renewable-data resolution on techno-economic assessments of green hydrogen systems. Energy Conversion and Management, 364, 121676.