Decarbonizing Rural Off-Grid Areas Through Hybrid Renewable Hydrogen Systems: A Case Study from Turkey
Abstract
1. Introduction
2. Materials and Methods
2.1. Modeling and Optimization
2.1.1. Load Profile Assessment
2.1.2. Deferrable Load
2.1.3. Solar Panel and Wind Turbine Selection
2.1.4. Hydrogen Energy Storage System Components
- Hydrogen is preferred because of its ability to flexibly balance seasonal production–consumption imbalances and its long-term storage capability. In the system, the electrolysis of water is carried out by means of an electrolyzer powered by excess electricity obtained from solar and wind resources and the hydrogen obtained is stored in tanks under certain pressure conditions [44].
- In this study, a proton exchange membrane (PEM) electrolyzer, the default model of HOMER Pro 3.14.2, was used. PEM technology is more suitable than alkaline electrolyzers due to its rapid response to variable production profiles of renewable energy sources, compact design, and high purity hydrogen production. The capital cost for the electrolyzer is defined as USD 1000/kW, with a replacement cost of USD 800/kW and an annual maintenance cost of USD 15/year. This value is in line with the recommended range of USD 900–1500/kW for commercial scale PEM electrolyzers reported by the International Energy Agency [45].
- For hydrogen tanks, capital cost is taken as USD 700/kg, replacement cost as USD 600/kg, and annual operating cost as USD 30/tank. These values correspond to the average of the estimates reported by IRENA [46] and a conservative approach has been adopted, taking into account regional cost differences and supply uncertainties.
- The capital cost of the fuel cell is USD 3000/kW, the refurbishment cost is USD 2400/kW, and the hydrogen cost is USD 3.5/kg. These costs are in line with the center range of values reported by the International Energy Agency [47]. This choice aimed to provide a balanced assumption for the study region, without extremes.
2.1.5. Converter
2.2. System Architecture
2.3. Life Cycle Assessment (LCA) and Impact Analysis of Hydrogen Leakage
3. Results and Discussions
3.1. Energy Production and Supply Reliability
3.2. Hydrogen Storage Performance and System Continuity
3.3. Comparative Energy Efficiency Analysis of Hybrid Systems
3.4. Impact of H2 Leakage on Carbon Equivalent Emissions: A Scenario Based Analysis
3.5. Life Cycle (LCA) Emission Analysis of the System
3.6. Literature Comparison
3.7. Critical Evaluation and Limitations of the Study
4. Conclusions
Author Contributions
Funding
Institutional Review Board Statement
Informed Consent Statement
Data Availability Statement
Acknowledgments
Conflicts of Interest
Abbreviations
AC | Alternating Current |
CC | Cycle Charging |
CO2 | Carbon dioxide |
COE | Cost of Energy |
DC | Direct Current |
EF | Emission Factor |
GHG | Greenhouse Gas |
GHI | Global Horizontal Irradiance |
GWP | Global Warming Potential |
H2 | Hydrogen |
HOMER | Hybrid Renewable and Distributed Generation System Design Software |
IEA | International Energy Agency |
IICEC | International Center for Energy and Climate |
LCA | Life Cycle Analysis |
LCE | Life Cycle Emission |
LF | Load Following |
NPC | Net Present Cost |
NREL | National Renewable Energy Laboratory |
OH | Hydroxyl |
PV | Photovoltaic |
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Reference | Aim | Analysis Method | Advantages | Disadvantages |
---|---|---|---|---|
[23] | Design and evaluate a hybrid renewable energy system integrating PV, wind, batteries, electrolyzers, and hydrogen storage to provide carbon-neutral electricity supply for university campuses. | HOMER Pro | - Carbon neutral energy solution - Local data-driven model - Ensuring seamlessness with H2 | - LCOE high (USD 10.66/kwh) - High system cost |
[24] | To conduct a techno-economic assessment of an isolated microgrid hybrid renewable energy system with PV, wind, battery, fuel cell, electrolyzers, and hydrogen storage, focusing on reliability and cost effectiveness. | HOMER | - Low NPC and COE - Providing reliable energy with 0% and 1% capacity shortage - Flexible storage with combination of H2 and battery | High initial investment cost |
[25] | To compare on-grid and off-grid hybrid photovoltaic-hydrogen energy system scenarios for an academic building in Poland, with emphasis on energy independence and CO2 reduction. | HOMER Pro | 100% off-grid system - 11,815 kg/year CO2 reduction with H2 | - LCOE: PV-on-grid system EUR 0.132/kWh; alternative scenarios EUR 1.00/kWh and EUR 1.17/kWh. - High investment cost |
[26] | To develop an integrated PV-wind-biomass hybrid system with battery and pumped storage to meet the electricity, heating, and hot water demands of university campuses with 100% renewable energy. | Meteonorm v7.1 dataset, GRG algorithm, campus scale modeling | - USD 0.1626/kWh low COE - Heating and hot water needs are also met - Carbon neutral energy planning at campus level | - High initial cost - Limited economic utilization of excess energy |
[27] | To analyze the techno-economic feasibility of a solar PV-hydrogen fuel cell hybrid renewable energy system aiming to reduce excess electricity and improve night supply for academic research buildings. | HOMER Pro + Fuzzy Logic powered optimization | - Contribution of the H2 system to the night load - Low rate of excess electricity (15.7%) - Economic CoE (USD 0.203/kWh) | High cost |
[28] | Optimizing multiple hybrid configurations combining PV, wind and battery, or hydrogen storage using advanced algorithms aimed at improving cost efficiency and system reliability. | Optimization with improved Chaotic Search + Simulated Annealing + HS algorithms | - Battery-based systems offer lower LCC and higher reliability - Robust algorithm with less than 11% error rate | - Low fuel cell and electrolyzer efficiency |
[29] | Techno-economic analysis of PV-wind-electrolyzer-H2 tank-battery systems for hydrogen production at refueling stations under different operational scenarios. | HOMER Pro | - Low cost result with USD 0.0158/kWh and USD 0.401/kg H2 | Hydrogen demand scenario static |
[30] | To evaluate the techno-economic performance of a hydrogen refueling station powered by a PV-wind hybrid power system, using a case study for Izmir-Çeşme. | HOMER Pro simulation | - LCOE: USD 0.146/kWh - LCOH: USD 7.526/kg | - %41 excess electricity |
[31] | Developing a net zero energy district model that integrates PV generation with smart city and nature-based solutions for urban carbon neutrality. | Modeling + simulation + threshold analysis | - Comprehensive system approach for carbon neutralization - NZED possible with PV + behavioral change | - Declining yields at high population density - Storage required |
[32] | To analyze the technical and economic feasibility of a grid-connected PV-wind-electrolyzer-H2 tank system for hydrogen refueling stations, focusing on demand-driven operation. | HOMER Pro + Monte Carlo demand simulation | - Economically favorable NPC (USD 8.35 M) obtained with demand-driven design - Production of 40,000 kg of green hydrogen per year | High NPC, requires large-scale infrastructure |
[33] | Optimizing solar-wind hybrid energy systems for hydrogen production under specific regional conditions, evaluating LCOH, COE, and economic feasibility. | HOMER Pro Simulation | - LCOH: Lowest hydrogen cost at USD 1.15/kg - COE: USD 0.19/kWh - Economic feasibility study for Salalah region provided | - NPC value is higher than other systems - LCA, leakage and environmental emissions not included |
[34] | Design and optimize a standalone hybrid PV–wind–battery–electrolyzer–H2 tank system for hydrogen fueling stations, targeting continuous supply and carbon neutrality. | Economic and technical optimization with HOMER Pro software | - Provides a carbon neutral energy solution - Uninterrupted energy supply with hydrogen storage | - LCOE USD 8.76/kWh - System investment cost is high |
Architecture | Dispatch | NPC (USD) | COE (USD) | Operating Cost (USD/yr.) | Initial Capital (USD) | Ren Fraction (%) | Total Fuel (kg/yr.) |
---|---|---|---|---|---|---|---|
PV50-WT2-FC10-EL50-HT80-CONV25 | CC | 297,419 | 0.34 | 7849 | 212.5 | 100 | 1841 |
PV60-WT2-FC10-EL50-HT80-CONV25 | CC | 301,126 | 0.345 | 8035 | 214.5 | 100 | 2011 |
WT4-FC10-EL50-HT80-CONV25 | LF | 30,438 | 0.35 | 8122 | 216.5 | 100 | 1535 |
WT4-FC10-EL50-HT80-CONV25 | LF | 311,538 | 0.356 | 8236 | 222.5 | 100 | 1380 |
Parameter | Scenario 1 (PV + Wind + Battery + H2) | Scenario 2 PV + Wind + H2) | Scenario 3 (Wind + H2) | Scenario 4 Wind + Battery + H2) |
---|---|---|---|---|
Total Production (kWh/yr.) | 187,538 | 206,303 | 193,967 | 191,609 |
PV Production (kWh/yr.) | 78,751 (42%) | 94,502 (45.8%) | — | — |
Wind Generation (kWh/yr.) | 87,589 (46.7%) | 87,589 (42.5%) | 175,178 (90.3%) | 175,178 (91.4%) |
Fuel Cell Production (kWh/yr.) | 21,198 (11.3%) | 24,213 (11.7%) | 18,790 (9.69%) | 16,432 (8.58%) |
Total Consumption (kWh/yr.) | 175,719 | 185,541 | 162,660 | 155,128 |
AC Primary Load (kWh/yr.) | 59,561 | 59,345 | 59,213 | 59,612 |
Deferrable Load (kWh/yr.) | 21,360 | 21,360 | 21,241 | 21,240 |
Excess Electricity (kWh/yr.) | 8625 (4.6%) | 17,760 (8.61%) | 26,310 (13.6%) | 31,777 (16.6%) |
Unmet Electric Load (kWh/yr.) | 769 (0.94%) | 986 (1.21%) | 1236 (1.51%) | 838 (1.03%) |
Capacity Shortage (kWh/yr.) | 1488 (1.82%) | 2282 (2.79%) | 2357 (2.88%) | 1466 (1.79%) |
Components | Energy Production (kWh/yr.) | Fuel Cell Production | Hydrogen Annual Energy Flow (kWh/yr.) | Inverter Losses (kWh/yr.) | Rectifier Losses (kWh/yr.) | Hydrogen Efficiency (%) |
---|---|---|---|---|---|---|
PV + Wind + Hydrogen + Battery | 187,538 | 21,198 | 61,376 | 1517 | 1608 | 34.5 |
PV+ Wind + Hydrogen | 206,303 | 24,213 | 67,032 | 1527 | 1475 | 36.1 |
Wind + Hydrogen | 193,967 | 18,790 | 51,183 | 806 | 4192 | 36.7 |
Wind + Hydrogen + Battery | 191,609 | 16,432 | 45,987 | 781 | 3873 | 35.7 |
Scenarios | H2 Consumption (kg/yr.) | Leakage Rate (%) | Leaking H2 (kg/yr.) | CO2 Equivalent Emission (kg/yr.) |
---|---|---|---|---|
Scenario 1 | 1841 | 1 | 18.41 | 607.53 |
5 | 92.05 | 3052.5 | ||
10 | 184.1 | 6075.3 | ||
Scenario 2 | 2011 | 1 | 20.11 | 663.63 |
5 | 100.55 | 3318.5 | ||
10 | 201.1 | 6636.3 | ||
Scenario 3 | 1535 | 1 | 15.35 | 506.55 |
5 | 76.75 | 2532.75 | ||
10 | 153.5 | 5065.5 | ||
Scenario 4 | 1380 | 1 | 13.80 | 455.4 |
5 | 69 | 2277 | ||
10 | 138 | 4554 |
Component | Unit Capacity | Emission Factor (kg CO2-eq/kW or kg) | Lifespan (yr.) | Scenario 1 (50 kW PV + H2 + 2 WT + 4 kWh Battery) Annual Emission (kg CO2-eq) | Scenario 2 (60 kW PV + H2 + 2 WT) Annual Emission (kg CO2-eq) | Scenario 3 (4 WT+ H2) Annual Emission (kg CO2-eq) | Scenario 4 (4 WT + H2 + 4 kWh Battery) Annual Emissions (kg CO2-eq) |
---|---|---|---|---|---|---|---|
PV Panel | kW | 1000 [56] | 25 | 2000 | 2400 | 0 | 0 |
Wind Turbine | units | 1300 [42] | 20 | 130 | 130 | 260 | 260 |
Fuel Cell | kW | 10 [13] | 20 | 5 | 5 | 5 | 5 |
Electrolyzer | kW | 453 [57] | 15 | 1510 | 1510 | 1510 | 1510 |
H2 Tank | kg | 875 [46] | 20 | 3500 | 3500 | 3500 | 3500 |
Lithium-Ion Battery | kWh | 63 [58] | 10 | 25.2 | 0 | 0 | 25.2 |
Inverter | kW | 50 | 15 | 83.33 | 83.33 | 83.33 | 83.33 |
H2 Leakage | kg/yr. | 33 | 607.53 | 663.63 | 506.55 | 455.4 | |
Total Emission | kg CO2-eq | 7861.063 | 8291.96 | 5864.88 | 5838.93 | ||
Specific CO2 emissions | g CO2-eq/kWh | 44.74 | 44.69 | 36.05 | 37.64 |
Study | System Components | COE (USD/kWh) | Excess Electricity (%) | Specific Emission (g CO2-eq/kWh) | Notes |
---|---|---|---|---|---|
This study | PV + Wind + H2 + Battery | 0.340 | <10 | 44.74 | Rural community, LCA, has H2 efficiency |
[24] | PV + Wind + H2 | 0.189 | >20 | N/A | Grid-connected, large-scale |
[25] | PV + H2 + Battery | 1 (€/kwh) | >25 | N/A | Urban, off-grid |
[27] | PV + H2 + Fuel Cell | 0.177 | N/A | N/A | No LCA analysis |
[30] | PV + Wind + H2 (Refueling) | 0.146 | 41 | N/A | Transportation-oriented, no housing burden |
[32] | PV+ Wind+ H2 | N/A | >25 | ~50–65 | Mains connected, LCA available |
[34] | PV + Wind+ H2 | 7.4 (€/kwh) | >25 | N/A | Transportation oriented |
[59] | PV + Wind + Diesel + H2 | – | ~15 | ~70–90 | Includes LCA, island application |
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Oymak, A.; Tur, M.R. Decarbonizing Rural Off-Grid Areas Through Hybrid Renewable Hydrogen Systems: A Case Study from Turkey. Processes 2025, 13, 2909. https://doi.org/10.3390/pr13092909
Oymak A, Tur MR. Decarbonizing Rural Off-Grid Areas Through Hybrid Renewable Hydrogen Systems: A Case Study from Turkey. Processes. 2025; 13(9):2909. https://doi.org/10.3390/pr13092909
Chicago/Turabian StyleOymak, Aysenur, and Mehmet Rida Tur. 2025. "Decarbonizing Rural Off-Grid Areas Through Hybrid Renewable Hydrogen Systems: A Case Study from Turkey" Processes 13, no. 9: 2909. https://doi.org/10.3390/pr13092909
APA StyleOymak, A., & Tur, M. R. (2025). Decarbonizing Rural Off-Grid Areas Through Hybrid Renewable Hydrogen Systems: A Case Study from Turkey. Processes, 13(9), 2909. https://doi.org/10.3390/pr13092909