Degradation-Aware Stochastic Scheduling of Multi-Stack Power-to-X Plants Under Joint Renewable and Electricity Price Uncertainty
Abstract
1. Introduction
1.1. Power-to-X and the Role of Electrolyser-Based Hydrogen Production
1.2. The Degradation–Flexibility Trade-Off
1.3. Multi-Stack Scheduling and Load-Allocation Strategies
1.4. Stochastic and Robust Optimization for Hydrogen Systems
1.5. Flexible Operation, Market Participation and Economic Context
1.6. Research Gap and Motivation
1.7. Contributions
- 1.
- A degradation-aware two-stage stochastic MILP framework is formulated for the day-ahead scheduling of multi-stack electrolyser fleets in PtX plants. First-stage decisions fix the binary commitment and startup matrices of every stack as here-and-now variables, while second-stage recourse dispatches power across stacks as scenario-indexed wait-and-see variables under jointly sampled realizations of renewable generation and electricity prices. This constitutes, to the best of our knowledge, the first formulation that simultaneously handles stack-resolved degradation and joint renewable-price uncertainty within a single tractable optimization model.
- 2.
- A piecewise linear, physically grounded multi-stack degradation model is embedded in the MILP backbone through a convex epigraph formulation. The model captures load-dependent and start–stop cycling contributions to voltage drift at the stack level and couples them to stack replacement cost through a capital-recovery coefficient, enabling the optimizer to trade short-term dispatch benefits against long-term ageing penalties at the stack level, a capability that existing deterministic [20,23,24,27] and stochastic [32,33,34] models cannot provide.
- 3.
- A Gaussian copula scenario generation and reduction pipeline is designed to represent the joint statistical dependence between renewable generation and day-ahead electricity prices, preserving the tail behaviour critical to degradation-accelerating events such as extreme ramps, zero-price periods and forced shutdowns. The pipeline combines empirical CDF marginals, Gaussian copula sampling under Sklar’s theorem, and k-medoids clustering under the Partitioning-Around-Medoids heuristic for scenario reduction. The full pipeline is implemented in MATLAB with the built-in intlinprog and linprog solvers, without requiring any commercial optimization toolbox, which makes the framework fully reproducible and directly usable by the PtX modelling community.
- 4.
- A comprehensive benchmarking study on a 100 MW wind-driven PtX plant with ten heterogeneous stacks quantifies, for the first time on a single common instance, the joint economic and reliability impact of ignoring either degradation or uncertainty. The proposed framework is compared against four formal ablations of the general MILP backbone: (i) deterministic degradation-ignorant scheduling, (ii) deterministic degradation-aware scheduling, (iii) degradation-ignorant stochastic scheduling, and (iv) a rule-based proportional heuristic. Out-of-sample evaluation on 50 independent test scenarios demonstrates that the proposed framework achieves the lowest levelised cost of hydrogen at EUR 24/kg, the highest expected hydrogen delivery at 7.68 t/day, the highest demand reliability at 85.0%, the lowest expected shortfall at 1348 kg, and up to 50% total cost reduction over deterministic degradation-ignorant baselines. The complete benchmark pipeline, including the four baselines and the out-of-sample re-dispatch, runs end-to-end in under two minutes on standard workstation hardware.
2. System Description and Modelling
2.1. Plant Architecture and Nomenclature
2.2. Electrolyser Dispatch and Commitment Model
2.3. Piecewise Linear Degradation Accounting
2.4. Joint Wind Price Uncertainty and Scenario Generation
2.5. Economic Objective and Reliability Metric
3. Two-Stage Stochastic MILP Formulation
3.1. Extensive-Form Stochastic Program
3.2. Compact Vector Form
3.3. Constraint Dimensioning
3.4. Sparse Assembly, Solver Deployment, and Effective LCOH
4. Scenario Generation and Reduction
4.1. Empirical Marginal Estimation
4.2. Gaussian Copula and Rank Correlation
4.3. Monte Carlo Sampling in the Copula Domain
4.4. Cluster-Based Reduction via k-Medoids
4.5. Out-of-Sample Partitioning and Statistical Validation
5. Case Study
5.1. Plant Configuration and Physical Parameters
5.2. Synthetic Input Data and Sampling Configuration
5.3. Benchmark Methods
5.3.1. B1—Deterministic Degradation-Ignorant (Det. no-Deg)
5.3.2. B2—Deterministic Degradation-Aware (Det. Deg-Aware)
5.3.3. B3—Stochastic Degradation-Ignorant (Stoch. no-Deg)
5.3.4. B4—Rule-Based Heuristic (Rule-Based)
5.3.5. B5—Proposed Framework (This Work)
Perfect-Foresight Oracle
5.4. Computational Environment and Solver Settings
5.5. Performance Indicators
6. Results and Discussion
6.1. Out-of-Sample Key Performance Indicators
6.2. Input Data and Scenario Statistics
6.3. Ablation Decomposition of the Modelling Ingredients
6.4. Cost Composition and Operational Regime Identification
6.5. Break-Even Penalty Analysis
6.6. First-Stage Commitment and Dispatch Solution
6.7. Degradation Model and Outcomes
6.8. Sensitivity Analysis
6.9. Cross-Method KPI Summary and Benchmark Positioning
6.10. Summary of Quantitative Contributions
7. Conclusions
7.1. Methodology Summary
7.2. Key Numerical Findings
7.3. Limitations
7.4. Future Work
Author Contributions
Funding
Institutional Review Board Statement
Informed Consent Statement
Data Availability Statement
Conflicts of Interest
Abbreviations
| PtX | Power-to-X |
| MILP | Mixed-Integer Linear Programming |
| PEM | Proton-Exchange Membrane |
| LCOH | Levelized Cost of Hydrogen |
| PWL | Piecewise Linear |
| SoH | State of Health |
| CDF | Cumulative Distribution Function |
| PAM | Partitioning-Around-Medoids |
| VPI | Value of Perfect Information |
| EMPC | Economic Model Predictive Control |
| CCHP | Combined Cooling, Heating and Power |
| IGDT | Information-Gap Decision Theory |
| CAPEX | Capital Expenditure |
| HHV | Higher Heating Value |
| LHV | Lower Heating Value |
| HTO | Hydrogen-to-Oxygen |
| RFNBO | Renewable Fuels of Non-Biological Origin |
| SOS2 | Special Ordered Sets of type 2 |
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| Reference | Multi-Stack | Degrad.-Aware | Stoch./Robust | RES & Price Unc. | Formal MILP | Indust.-Scale |
|---|---|---|---|---|---|---|
| Zhang & Yuan [20] | ✗ | ✓ | ✗ | ✗ | ✓ | ∼ |
| Lu et al. [27] | ✓ | ✓ | ✗ | ✗ | ✓ | ✓ |
| Qiu et al. [11] | ✓ | ∼ | ✗ | ✗ | ✓ | ✓ |
| Li et al. [9] | ✓ | ✗ | ✗ | ✗ | ∼ | ✓ |
| Wang et al. [10] | ✓ | ✓ | ✗ | ✗ | ∼ | ✓ |
| Li et al. [12] | ✓ | ✗ | ✗ | ✗ | ✓ | ✓ |
| Han et al. [13] | ✓ | ✗ | ✗ | ✗ | ✓ | ✓ |
| Tang et al. [28] | ✓ | ∼ | ✗ | ✗ | ✓ | ✓ |
| Zheng et al. [30] | ✓ | ✗ | ✗ | ✗ | ✓ | ∼ |
| Superchi et al. [24] | ✗ | ✓ | ✗ | ✗ | ✓ | ✓ |
| Thummalacherla & Bhattacharya [23] | ∼ | ✓ | ✗ | ✗ | ✓ | ✓ |
| Chi et al. [43] | ✗ | ✗ | ✗ | ✗ | ✓ | ✓ |
| Maluenda et al. [31] | ✗ | ✗ | ✗ | ✗ | ✓ | ∼ |
| Cao et al. [32] | ✗ | ✗ | ✓ | ∼ | ✓ | ✓ |
| Sun et al. [33] | ✗ | ✗ | ✓ | ∼ | ✓ | ✓ |
| Zhou et al. [34] | ✗ | ✗ | ✓ | ∼ | ✓ | ✓ |
| Wang et al. [35] | ✗ | ✗ | ✓ | ✓ | ✓ | ✓ |
| Abdelghany et al. [37] | ✗ | ✗ | ✓ | ∼ | ∼ | ∼ |
| Dolatabadi & Mohammadi-Ivatloo [40] | ✗ | ✗ | ✓ | ✓ | ✓ | ∼ |
| Siqin et al. [41] | ✗ | ✗ | ✓ | ✓ | ✓ | ✓ |
| Cao et al. [36] | ✗ | ✗ | ✓ | ∼ | ✓ | ✓ |
| Mansour-Saatloo et al. [38] | ✗ | ✗ | ✓ | ∼ | ✓ | ∼ |
| Wu et al. [39] | ✗ | ✗ | ✓ | ∼ | ✓ | ∼ |
| Zhang et al. [42] | ✗ | ✗ | ✓ | ∼ | ✓ | ✓ |
| This work | ✓ | ✓ | ✓ | ✓ | ✓ | ✓ |
| Operating Point | |||||
|---|---|---|---|---|---|
| [–] | [MW] | [–] | [kg/h] | [EUR/kg] | |
| Under-loaded | 0.30 | 3.0 | 1.50 | 61.21 | 5.88 |
| In-plateau | 0.75 | 7.5 | 1.03 | 153.02 | 1.62 |
| Overloaded | 1.05 | 10.5 | 2.00 | 214.22 | 2.24 |
| Constraint Family | Reference | Expression | Row Count |
|---|---|---|---|
| Power upper bound | (1) | 4800 | |
| Power lower bound | (1) | 4800 | |
| Wind availability | (2) | 480 | |
| Startup indicator | (3) | 230 | |
| Aggregate ramp | (4) | 920 | |
| PWL degradation cuts | (8) | 1600 | |
| Demand balance | (14) | S | 20 |
| total rows | 12,850 | ||
| H2 Faraday equality | (5) | 4800 | |
| total rows | 4800 | ||
| Marginal | [%] | |||||||
|---|---|---|---|---|---|---|---|---|
| Wind [MW]—pool | – | – | 28.4 | 41.2 | 55.1 | 69.3 | 82.7 | 0.110 |
| Wind [MW]—reduced | 2.3 | 4.2 | 29.1 | 41.8 | 54.7 | 68.5 | 83.2 | 0.108 |
| Price [EUR/MWh]—pool | – | – | 42.5 | 63.1 | 79.8 | 97.4 | 118.6 | – |
| Price [EUR/MWh]—reduced | 4.1 | 5.1 | 43.2 | 64.0 | 80.5 | 96.1 | 117.8 | – |
| Symbol | Description | Value | Unit |
|---|---|---|---|
| Plant architecture and dispatch (Section 2.2) | |||
| N | Number of electrolyser stacks | 10 | – |
| Nominal power per stack | 10 | MW | |
| Minimum safe load () | MW | ||
| Overload ceiling () | MW | ||
| T | Scheduling horizon | 24 | h |
| Aggregate ramp limit | 6 | MW/h | |
| Reference HHV efficiency | – | ||
| Hydrogen lower heating value | kWh/kg | ||
| Economic coefficients (Section 2.5) | |||
| Daily contractual demand | 9000 | kg/day | |
| Shortfall penalty | 50 | EUR/kg | |
| Cold-start cost | 800 | EUR/event | |
| CAPEX per stack | 8 | M EUR | |
| Nominal stack lifetime | 80,000 | h | |
| Degradation model (Section 2.3) | |||
| Nominal cell voltage | V | ||
| End-of-life cell voltage | V | ||
| Load-induced drift rate | V/h | ||
| Idle-induced drift rate † | V/h | ||
| Cycle damage increment | V/cycle | ||
| Capital-recovery coefficient | EUR/V | ||
| K | Number of PWL breakpoints | 8 | – |
| PWL load grid | |||
| PWL multipliers | – | ||
| Initial SoH spread | – | ||
| Uncertainty model (Section 4) | |||
| Synthetic calibration sample size | 8760 | h | |
| Wind price rank correlation | – | ||
| Training pool size | 300 | – | |
| S | Reduced training scenarios | 20 | – |
| Test pool size | 500 | – | |
| Reduced test scenarios | 50 | – | |
| Training random seed | 1 | – | |
| Test random seed | 999 | – | |
| Method | [kEUR] | LCOH [EUR/kg] | LCOHeff [EUR/kg] | [t/day] | Rel. [%] | Shortfall [kg] |
|---|---|---|---|---|---|---|
| B1 Det. no-deg | 365 | 175 | 41 | 2.09 | 22.1 | 7008 |
| B2 Det. deg-aware | 169 | 27 | 19 | 6.45 | 71.6 | 2555 |
| B3 Stoch. no-deg | 253 | 40 | 28 | 6.57 | 73.0 | 2428 |
| B4 Rule-based | 401 | 240 | 45 | 1.68 | 17.2 | 7467 |
| B5 Proposed | 180 | 24 | 20 | 7.68 | 85.0 | 1348 |
| Method | [kEUR] | [%] | [%] | [%] | [%] |
|---|---|---|---|---|---|
| B1 Det. no-deg | 365 | 1.4 | 2.3 | 96.0 | 4.0 |
| B2 Det. deg-aware | 169 | 7.1 | 15.7 | 75.6 | 24.4 |
| B3 Stoch. no-deg | 253 | 7.1 | 40.3 | 47.4 | 52.6 |
| B4 Rule-based | 401 | 1.2 | 4.2 | 93.1 | 6.9 |
| B5 Proposed | 180 | 11.1 | 46.1 | 37.5 | 62.5 |
| Window | Hours | [MW] | Duration [h] | H2 Contribution [%] |
|---|---|---|---|---|
| 04–06 | 25.1 | 3 | 19.0 | |
| 11–13 | 17.8 | 3 | 13.5 | |
| 15–22 | 37.2 | 8 | 60.0 | |
| Idle | rest | 0.0 | 10 | 7.5 |
| Stack Index i | Committed Hours | [MW] | Cycles | [kEUR] | |
|---|---|---|---|---|---|
| 3 | 0.138 | 14 | 7.3 | 3 | 24.1 |
| 4 | 0.183 | 10 | 6.9 | 1 | 8.8 |
| 5 | 0.227 | 14 | 7.4 | 3 | 23.4 |
| 6 | 0.272 | 10 | 7.1 | 2 | 16.3 |
| 10 | 0.450 | 8 | 6.8 | 1 | 8.9 |
| Total | — | 56 | — | 10 | 81.5 |
| Configuration | LCOH [EUR/kg] | ΔLCOH [EUR/kg] | Dominates B1–B4? |
|---|---|---|---|
| (A) Copula correlation ρ sweep (, ) | |||
| 21.4 | ✓ ✓ ✓ ✓ | ||
| 24.7 | ✓ ✓ ✓ ✓ | ||
| (reference) | 23.9 | 0.0 | ✓ ✓ ✓ ✓ |
| 24.3 | ✓ ✓ ✓ ✓ | ||
| 40.5 | ✓ ✗ ∼ ✓ | ||
| Plateau spread () | 3.3 | ||
| Relative variation | 14% | ||
| (B) k-medoids seed ω sweep (, ) | |||
| (reference) | 23.7 | ✓ ✓ ✓ ✓ | |
| 25.8 | ✓ ✓ ✓ ✓ | ||
| 30.0 | ✓ ✗ ✓ ✓ | ||
| 30.0 | ✓ ✗ ✓ ✓ | ||
| 36.0 | ✓ ✗ ✓ ✓ | ||
| Mean | 28.4 | ||
| Std. dev. σ | 4.7 | ||
| CV | 16.4% | ||
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Tegani, I.; Afghoul, H.; Alharbi, S.S.; Alharbi, S.S.; Tegani, S.; Kraa, O. Degradation-Aware Stochastic Scheduling of Multi-Stack Power-to-X Plants Under Joint Renewable and Electricity Price Uncertainty. Energies 2026, 19, 2482. https://doi.org/10.3390/en19102482
Tegani I, Afghoul H, Alharbi SS, Alharbi SS, Tegani S, Kraa O. Degradation-Aware Stochastic Scheduling of Multi-Stack Power-to-X Plants Under Joint Renewable and Electricity Price Uncertainty. Energies. 2026; 19(10):2482. https://doi.org/10.3390/en19102482
Chicago/Turabian StyleTegani, Ilyes, Hamza Afghoul, Salah S. Alharbi, Saleh S. Alharbi, Salem Tegani, and Okba Kraa. 2026. "Degradation-Aware Stochastic Scheduling of Multi-Stack Power-to-X Plants Under Joint Renewable and Electricity Price Uncertainty" Energies 19, no. 10: 2482. https://doi.org/10.3390/en19102482
APA StyleTegani, I., Afghoul, H., Alharbi, S. S., Alharbi, S. S., Tegani, S., & Kraa, O. (2026). Degradation-Aware Stochastic Scheduling of Multi-Stack Power-to-X Plants Under Joint Renewable and Electricity Price Uncertainty. Energies, 19(10), 2482. https://doi.org/10.3390/en19102482

