Production & Supply Chain
A Review on Green Hydrogen Production by Aqueous Phase Reforming of Lignocellulose and Derivatives
Mar 2025
Publication
With the intensification of the global energy crisis hydrogen has attracted significant attention as a high-energy-density and zero-emission clean energy source. Traditional hydrogen production methods are dependent on fossil fuels and simultaneously contribute to environmental pollution. The aqueous phase reforming (APR) of renewable biomass and its derivatives has emerged as a research hotspot in recent years due to its ability to produce green hydrogen in an environmentally friendly manner. This review provides an overview of the advancements in APR of lignocellulosic biomass as a sustainable and environmentally friendly method for hydrogen production. It focuses on the reaction pathways of various biomass feedstocks (such as glucose cellulose and lignin) as well as the types and performance of catalysts used in the APR process. Finally the current challenges and future prospects in this field are briefly discussed.
Simulation of a Hybrid Plant with ICE/HT-PEMFC and On-Site Hydrogen Production from Methane Steam Reforming
Oct 2025
Publication
Hydrogen-based technologies prominently fuel cells are emerging as strategic solutions for decarbonization. They offer an efficient and clean alternative to fossil fuels for electricity generation making a tangible contribution to the European Green Deal climate objectives. The primary issue is the production and transportation of hydrogen. An on-site hydrogen production system that includes CO2 capture could be a viable solution. The proposed power system integrates an internal combustion engine (ICE) with a steam methane reformer (SMR) equipped with a CO2 capture and energy storage system to produce “blue hydrogen”. The hydrogen fuels a high-temperature polymer electrolyte membrane (HTPEM) fuel cell. A battery pack incorporated into the system manages rapid fluctuations in electrical load ensuring stability and continuity of supply and enabling the fuel cell to operate at a fixed point under nominal conditions. This hybrid system utilizes natural gas as its primary source reducing climate-altering emissions and representing an efficient and sustainable solution. The simulation was conducted in two distinct environments: Thermoflex code for the integration of the engine reformer and CO2 capture system; and Matlab/Simulink for fuel cell and battery pack sizing and dynamic system behavior analysis in response to user-demanded load variations with particular attention to energy flow management within the simulated electrical grid. The main results show an overall efficiency of the power system of 39.9% with a 33.5% reduction in CO2 emissions compared to traditional systems based solely on internal combustion engines.
Which Offers Greater Techno-Economic Potential: Oil or Hydrogen Production from Light Oil Reservoirs?
Jun 2025
Publication
The global emphasis on clean energy has increased interest in producing hydrogen from petroleum reservoirs through in situ combustion-based processes. While field practices have demonstrated the feasibility of co-producing hydrogen and oil the question of which offers greater economic potential oil or hydrogen remains central to ongoing discussions especially as researchers explore ways to produce hydrogen exclusively from petroleum reservoirs. This study presents the first integrated techno-economic model comparing oil and hydrogen production under varying injection strategies using CMG STARS for reservoir simulations and GoldSim for economic modeling. Key technical factors including injection compositions well configurations reservoir heterogeneity and formation damage (issues not addressed in previous studies) were analyzed for their impact on hydrogen yield and profitability. The results indicate that CO2-enriched injection strategies enhance hydrogen production but are economically constrained by the high costs of CO2 procurement and recycling. In contrast air injection although less efficient in hydrogen yield provides a more cost-effective alternative. Despite the technological promise of hydrogen oil revenue remains the dominant economic driver with hydrogen co-production facing significant economic challenges unless supported by policy incentives or advancements in gas lifting separation and storage technologies. This study highlights the economic trade-offs and strategic considerations crucial for integrating hydrogen production into conventional petroleum extraction offering valuable insights for optimizing hydrogen co-production in the context of a sustainable energy transition. Additionally while the present work focuses on oil reservoirs future research should extend the approach to natural gas and gas condensate reservoirs which may offer more favorable conditions for hydrogen generation.
Sustainable Hydrogen Production from Nuclear Energy
Aug 2025
Publication
The rapid increase in global warming requires that sustainable energy choices aimed at achieving net-zero greenhouse gas emissions be implemented as soon as possible. This objective emerging from the European Green Deal and the UN Climate Action could be achieved by using clean and efficient energy sources such as hydrogen produced from nuclear power. “Renewable” hydrogen plays a fundamental role in decarbonizing both the energy-intensive industrial and transport sectors while addressing the global increase in energy consumption. In recent years several strategies for hydrogen production have been proposed; however nuclear energy seems to be the most promising for applications that could go beyond the sole production of electricity. In particular nuclear advanced reactors that operate at very high temperatures (VHTR) and are characterized by coolant outlet temperatures ranging between 550 and 1000 ◦C seem the most suitable for this purpose. This paper describes the potential use of nuclear energy in coordinated and coupled configurations to support clean hydrogen production. Operating conditions energy requirements and thermodynamic performance are described. Moreover gaps that require additional technology and regulatory developments are outlined. The intermediate heat exchanger which is the key component for the integration of nuclear hybrid energy systems was studied by varying the thermal power to determine physical parameters needed for the feasibility study. The latter consisting of the comparative cost evaluation of some nuclear hydrogen production methods was carried out using the HEEP code developed by the IAEA. Preliminary results are presented and discussed.
Impact of Plastic Composition on the Performance of the Integrated Process of Pyrolysis and Oxidative Steam Reforming for Hydrogen Production
Aug 2025
Publication
The pyrolysis and oxidative steam reforming (P-OSR) of different types of plastics (HDPE PP PET and PS) has been carried out in a two reactor system provided with a conical spouted bed reactor (CSBR) and a fluidized bed reactor (FBR). The effect plastic composition has on the oxidative steam reforming step has been analyzed using two space time values (3.1 gcatalyst min gplastic − 1 and 12.5 gcatalyst min gplastic − 1 ) at a reforming temperature of 700 ◦C S/P ratio of 3 and ER of 0.2 (optimum conditions for autothermal reforming). The different composition of the plastics leads to differences in the yields and compositions of pyrolysis products and consequently in the performance of the oxidative steam reforming step. High conversions (> 97 %) have been achieved by using a space time of 12.5 gcat min gplastic − 1 with H2 production increasing as follows: PET ≪ PS < HDPE ≤ PP. A maximum H2 production of 25.5 wt% has been obtained by using PP which is lower than that obtained in the process of pyrolysis and in line conventional steam reforming (P-SR) of the same feedstock (34.8 wt%). The lowest H2 production (10.5 wt%) has been achieved when PET was used due to the high oxygen content of this plastic. The results obtained in this study prove that P-OSR performs very well with different feedstock thereby confirming the versatility and efficiency of this process to produce a hydrogen-rich gas.
MOF-Derived Electrocatalysts for High-Efficiency Hydrogen Production via Water Electrolysis
Jun 2025
Publication
Water electrolysis for hydrogen production has garnered significant attention in the context of increasing global energy demands and the “dual-carbon” strategy. However practical implementation is hindered by challenges such as high overpotentials high catalysts costs and insufficient catalytic activity. In this study three mono and bimetallic metal−organic framework (MOFs)-derived electrocatalysts Fe-MOFs Fe/Co-MOFs and Fe/Mn-MOFs were synthesized via a one-step hydrothermal method using nitroterephthalic acid (NO2-BDC) as the ligand and NN-dimethylacetamide (DMA) as the solvent. Electrochemical tests demonstrated that the Fe/Mn-MOFs catalyst exhibited superior performance achieving an overpotential of 232.8 mV and a Tafel slope of 59.6 mV·dec−1 alongside the largest electrochemical active surface area (ECSA). In contrast Fe/Co-MOFs displayed moderate catalytic activity while Fe-MOFs exhibited the lowest efficiency. Stability tests revealed that Fe/Mn-MOFs retained 92.3% of its initial current density after 50 h of continuous operation highlighting its excellent durability for the oxygen evolution reaction (OER). These findings emphasize the enhanced catalytic performance of bimetallic MOFs compared to monometallic counterparts and provide valuable insights for the development of high-efficiency MOF-based electrocatalysts for sustainable hydrogen production.
Design and Optimization of a Solar Parabolic Dish for Steam Generation in a Blue Hydrogen Production Plant
Oct 2025
Publication
The integration of renewable energy into industrial processes is crucial for reducing the carbon footprint of conventional hydrogen production. This work presents detailed design optical–thermal simulation and performance analysis of a solar parabolic dish (SPD) system for supplying high-temperature steam to a Steam Methane Reforming (SMR) plant. A 5 m diameter dish with a focal length of 3 m was designed and optimized using COMSOL Multiphysics (version 6.2) and MATLAB (version R2023a). Optical ray tracing confirmed a geometric concentration ratio of 896× effectively focusing solar irradiation onto a helical cavity receiver. Thermal–fluid simulations demonstrated the system’s capability to superheat steam to 551 ◦C at a mass flow rate of 0.0051 kg/s effectively meeting the stringent thermal requirements for SMR. The optimized SPD system with a 5 m dish diameter and 3 m focal length was designed to supply 10% of the total process heat (≈180 GJ/day). This contribution reduces natural gas consumption and leads to annual fuel savings of approximately 141000 SAR (Saudi Riyal) along with a substantial reduction in CO2 emissions. These quantitative results confirm the SPD as both a technically reliable and economically attractive solution for sustainable blue hydrogen production.
Risk Assessment of Offshore Wind–Solar–Current Energy Coupling Hydrogen Production Project Based on Hybrid Weighting Method and Aggregation Operator
Oct 2025
Publication
Under the dual pressures of global climate change and energy structure transition the offshore wind–solar–current energy coupling hydrogen production (OCWPHP) system has emerged as a promising integrated energy solution. However its complex multi-energy structure and harsh marine environment introduce systemic risks that are challenging to assess comprehensively using traditional methods. To address this we develop a novel risk assessment framework based on hesitant fuzzy sets (HFS) establishing a multidimensional risk criteria system covering economic technical social political and environmental aspects. A hybrid weighting method integrating AHP entropy weighting and consensus adjustment is proposed to determine expert weights while minimizing risk information loss. Two aggregation operators—AHFOWA and AHFOWG—are applied to enhance uncertainty modeling. A case study of an OCWPHP project in the East China Sea is conducted with the overall risk level assessed as “Medium.” Comparative analysis with the classical Cumulative Prospect Theory (CPT) method shows that our approach yields a risk value of 0.4764 closely aligning with the CPT result of 0.4745 thereby confirming the feasibility and credibility of the proposed framework. This study provides both theoretical support and practical guidance for early-stage risk assessment of OCWPHP projects.
A Comparative Study of Alternative Polymer Binders for the Hydrogen Evolution Reaction
Aug 2025
Publication
Given the economic industrial and environmental value of green dihydrogen (H2) optimization of water electrolysis as a means of producing H2 is essential. Binders are a crucial component of electrocatalysts yet they remain largely underdeveloped with a significant lack of standardization in the field. Therefore targeted research into the development of alternative binder systems is essential for advancing performance and consistency. Binders essentially act as the key to regulating the electrode (support)–catalyst–electrolyte interfacial junctions and contribute to the overall reactivity of the electrocatalyst assembly. Therefore alternative binders were explored with a focus on cost efficiency and environmental compatibility striving to achieve desirable activity and stability. Herein the alkaline hydrogen evolution reaction (HER) was investigated and the sluggish water dissociation step was targeted. Controlled hydrophilic poly(vinyl alcohol)-based hydrogel binders were designed for this application. Three hydrogel binders were evaluated without incorporated electrocatalysts namely PVA145 PVA145-blend-bPEI1.8 and PVA145-blend-PPy. Interestingly the study revealed that the hydrophilicity of the binders exhibited an enhancing effect on the observed activity resulting in improved performance compared to the commercial binder Nafion™. Notably the PVA145 system stands out with an overpotential of 224 mV at−10 mA·cm−2 (geometric) in 1.0 M KOH compared to the 238 mV exhibited by Nafion™. Inclusion of Pt as active material in PVA145 as binder exhibited a synergistic increase in performance achieving a mass activity of 1.174 A.cm−2.mg−1 Pt in comparison to Nafion™’s 0.344 A.cm−2.mg−1 Pt measured at−150 mV vs RHE. Our research aimed to contribute to the development of cost-effective and efficient binder systems stressing the necessity to challenge the dominance of the commercially available binders.
Biohydrogen Production from Industrial Waste: The Role of Pretreatment Methods
Oct 2025
Publication
This study aimed to investigate the effectiveness of dark fermentation in biohydrogen production from agro-industrial wastes including apple pomace brewer’s grains molasses and potato powder subjected to different pretreatment methods. The experiments were conducted at a laboratory scale using 1000 cm3 anaerobic reactors at a temperature of 35 ◦C and anaerobic sludge as the inoculum. The highest yield of hydrogen was obtained from pre-treated apple pomace (101 cm3/g VS). Molasses a less complex substrate compared to the other raw materials produced 25% more hydrogen yield following pretreatment. Methanogens are sensitive to high temperatures and low-pH conditions. Nevertheless methane constituted 1–6% of the total biogas under these conditions. The key factor was appropriate treatment of the inoculum to limit competition from methanogens. Increasing the inoculum dose from 150 cm3/dm3 to 250 cm3/dm3 had no further effect on biogas production. The physicochemical parameters and VFA data confirmed the stability and usefulness of activated sludge as a source of microbial cultures for H2 production via dark fermentation.
Maximization and Efficient Production Rates of Different Zero Carbon Electrofuels using Dry Alkaline Electroyzers
Aug 2025
Publication
The present work focused on the comparison between HHO and hydrogen electrolyzers in design gas production and various parameters which affect the performance and efficiency of alkaline electrolyzers. The primary goal is to generate the highest possible hydrogen and HHO gas flow rates. Hydrogen and HHO were produced using 3 mm electrode of stainless steel 316L with 224 cm2 surface area. Hydroxy and hydrogen rates were affected by electrolyte content cell connection electric current operating time electrolyte temperature and voltage. Maximum HHO generation values were 1020 1076 1125 and 1175 mL min−1 n at 5 10 15 and 20 g L−1 of sodium hydroxide (NaOH) with supply currents of 15 15.3 15.6 and 16 A respectively. Once it stabilized after 30 min the temperature increased to 26 30 35 and 38 °C respectively and remained there. With currents of 18 18.45 18.7 19.2 19.5 and 19.8 A hydrogen output peak values after 60 min. stayed constant at 680 734 785 846 897 and 945 mL min-1. at 5 10 15 and 20 g L−1 NaOH catalyst concentrations. At 5 10 15 and 20 g L−1 catalyst ratios the temperatures were elevated to constant values of 28.5 32 37.9 40.5 41.4 and 43 °C respectively. With cell design [4C3A19N] electrolyte concentration of 5 g L−1 NaOH and current of 14 A maximum HHO productivity was 866 mL min−1. and 74.23% efficiency. In a cell design of [4C5A17N] with catalyst content of 10 g L−1 maximum productivity was 680 mL min−1 for hydrogen and highest production efficiency of 72.85% was attained at 18 A.
Optimization Using RSM of Combined Cycle of Power, NG, and Hydrogen Production by a Bi-geothermal Energy Resource and LNG Heat Sink
Aug 2025
Publication
This study presents a comprehensive optimization of a tri-generation system that integrates dual geothermal wells Liquefied Natural Gas (LNG) cold energy recovery and hydrogen production using an advanced Response Surface Methodology (RSM) approach. The system combines two geothermal wells with different temperature profiles power generation via an Organic Rankine Cycle (ORC) and hydrogen production through a Proton Exchange Membrane (PEM) electrolyzer enhanced by integrated LNG regasification for improved energy recovery. The primary novelty of this work lies in the first application of RSM for multi-objective optimization of geothermal-based tri-generation systems moving beyond the conventional single-objective approaches. A 40-run experimental design is employed to simultaneously optimize three critical performance indicators: exergy efficiency power-specific cost and hydrogen production rate considering six key operating parameters. The RSM framework enables systematic exploration of parameter interactions and delivers statistically validated predictive models offering a robust and computationally efficient optimization strategy. The optimized system achieves outstanding performance with an exergy efficiency of 44.60% a competitive power-specific cost of 19.70 $/GJ and a hydrogen production rate of 5.15 kg/hr. Comparative analysis against prior studies confirms the superiority of the RSM-based approach demonstrating a 1% improvement in exergy efficiency (44.60% vs. 44.16%) a significant 44.1% increase in hydrogen production rate (5.15 kg/hr vs. 3.575 kg/hr) and a 0.81% reduction in power-specific cost compared to genetic algorithm-based optimization.
Process Integration and Exergy-based Assessment of High-temperature Solid Oxide Electrolysis Configurations
Sep 2025
Publication
Solid oxide electrolysis (SOEL) is considered an efficient option for largely emission-free hydrogen production and thus for supporting the decarbonization of the process industry. The thermodynamic advantages of high-temperature operation can be utilized particularly when heat integration from subsequent processes is realized. As the produced hydrogen is usually required at a higher pressure level the operating pressure of the electrolysis is a relevant design parameter. The study compares pressurized and near-atmospheric designs of 126 MW SOEL systems with and without the integration of process heat from a downstream ammonia synthesis and the inefficiencies that occur in the processes. Furthermore process improvements by sweep-air utilization are investigated. Pinch analysis is applied to determine the potential of internal heat recovery and the minimum external heating and cooling demand. It is shown that pressurized SOEL operation does not necessarily decrease the overall power consumption for compression due to the high power requirement of the sweep-air compressor. The exergetic efficiencies of the standalone SOEL processes achieve similar values of = 81 %. Results further show that integrating the heat of reaction from ammonia synthesis can replace almost the entire electrically supplied thermal energy thereby improving the overall exergetic efficiency by up to 3.5 percentage points. However the exergetic efficiency strongly depends on the applied air ratio. The highest exergetic efficiency of 86 % can be achieved by employing sweep-air utilization with an expander. The results demonstrate that integrating downstream process heat and applying sweep-air utilization can significantly enhance overall efficiency and thus reduce external energy requirements.
Design and Assessment of an Integrated PV-based Hydrogen Production Facility
Jun 2025
Publication
This study develops a photovoltaic (PV)-based hydrogen production system specifically designed for university campuses which is expected to lead in sustainability efforts. The proposed system aims to meet the electricity demand of a Hydrogen Research Center while supplying energy to an electric charging station and a hydrogen refueling station for battery-electric and fuel-cell electric vehicles operating within the campus. In this integrated system the electricity generation capacity of PV panels installed on the research center’s roof is determined and the surplus electricity after meeting the energy demand is allocated to cover the varying proportions needed for both electric charging station and hydrogen production system. The green hydrogen produced by the system is compressed to 100 350 and 700 bar with intermediate cooling stages where the heat generated at the compressor outlet is absorbed by a cooling fluid and repurposed in a condenser for domestic hot water production. A full thermodynamic analysis of this entirely renewable energy-powered system is conducted by considering a 9-hour daily operational period from 8:00 AM to 5:00 PM. The average incoming solar radiation is determined to be 484.63 W/m2 resulting in an annual electricity generation capacity of 494.86 MWh. Based on the assumptions and data considered the energy and exergy efficiencies of the proposed system are calculated as 17.71 % and 17.01 % respectively with an annual hydrogen production capacity of 3.642 tons. Various parametric studies are performed for varying solar intensity values and PV surface areas to investigate how the overall system capacities and efficiencies are affected. The results show that an integration of hydrogen production systems with solar energy offers significant advantages including mitigating intermittency issues found in standalone renewable systems reducing carbon emissions compared to fossil-based alternatives and enhancing the flexibility of energy systems.
Efficiently Coupling Water Electrolysis with Solar PV for Green Hydrogen Production
Aug 2025
Publication
Solar-driven water electrolysis has emerged as a prominent technology for the production of green hydrogen facilitated by advancements in both water electrolyzers and solar cells. Nevertheless the majority of integrated solar-to-hydrogen systems still struggle to exceed 20% efficiency particularly in large-scale applications. This limitation arises from suboptimal coupling methodologies and system-level inefficiencies that have rarely been analyzed. To address these challenges this study investigates the fundamental principles of solar hydrogen production and examines key energy losses in photovoltaic-electrolyzer systems. Subsequently it systematically discusses optimization strategies across three dimensions: (1) enhancing photovoltaic (PV) system output under variable irradiance (2) tailoring electrocatalysts and electrolyzer architectures for high-performance operation and (3) minimizing coupling losses through voltage-matching technologies and energy storage devices. Finally we review existing large-scale solar hydrogen infrastructure and propose strategies to overcome barriers related to cost durability and scalability. By integrating material innovation with system engineering this work offers insights to advance solar-powered electrolysis toward industrial applications.
Feasibility Assessment into the Use of Hybrid Gas-hydride Tanks for Use in Improving the Flexibility of Offshore Hydrogen Production using Wind Power
Oct 2025
Publication
Offshore hydrogen production offers a promising solution for harnessing wind energy far from shore by using hydrogen as an energy carrier instead of electrical cables. Flexibility in hydrogen production systems is crucial to maximising the conversion of intermittent wind energy into hydrogen. To improve the performance of lowpressure compressed gas buffer stores hybrid gas-hydride tanks have been identified as a viable solution increasing useable storage density from 1.2 kg m− 3 to 6.3 kg m− 3 with just a 5 vol% addition of hydride. This study evaluates the reduction in tank volume reduction in cost and enhancements in useable storage density achieved by integrating different hydrides under varying temperature conditions. Using hydrogen mass flow rate profiles a storage mass target was determined for optimisation. The results demonstrate that hybrid gas-hydride tanks can reduce tank size by around 80 % lowering costs by 24 % and achieve a 5.1-fold improvement in useable storage density.
Development of Sustainability Assessment Framework for Preliminary Design of Chemical Process: Hydrogen Production as Case Study
Aug 2025
Publication
Sustainable process design has become increasingly important in transitioning from conventional to sustainable chemical production yet comprehensive sustainability assessment at the preliminary design stage remains a challenge. This study addresses this gap by proposing a hierarchical framework that integrates the Principles Criteria and Indicators (PC&I) method with multi-criteria decision-making (MCDM) tools including entropy weighting TOPSIS and weighted addition. The framework guides the systematic selection of sustainability indicators across economic environmental and social dimensions. To validate its applicability a case study on hydrogen production via four process routes natural gas reforming biomass-derived syngas methanol purge gas recovery and alkaline electrolysis is conducted. Results show that the methanol purge gas process exhibits the best overall sustainability followed by biomass syngas and alkaline electrolysis. The case demonstrates the framework’s capability to differentiate between alternatives under conflicting sustainability dimensions. This work provides a structured and replicable approach to support sustainable decision-making in early-stage chemical process design.
A Comprehensive Review of Green Hydrogen Technology: Electrolysis Methods, Topologies and Control Strategies, Applications
Oct 2025
Publication
As a pivotal clean energy carrier for achieving carbon neutrality green hydrogen technology has attracted growing global attention. This review systematically examines four mainstream water electrolysis technologies—alkaline electrolysis proton exchange membrane electrolysis solid oxide electrolysis and anion exchange membrane electrolysis—analyzing their fundamental principles material challenges and development trends. It further classifies and compares power electronic converter topologies including non-isolated and isolated DC–DC converters as well as AC–DC converter architectures and summarizes advanced control strategies such as dynamic power regulation and fault-tolerant operation aimed at enhancing system efficiency and stability. A holistic “electrolyzer–power converter–control strategy” integration framework is proposed to provide tailored technological solutions for diverse application scenarios. Finally the challenges and future prospects of green hydrogen across the energy transportation and industrial sectors are discussed underscoring its potential to accelerate the global transition toward a sustainable low-carbon energy system.
Experimental Investigation of Hydrogen Production Performance of PEM Electrolyze
Jul 2025
Publication
As global awareness of environmental protection increases hydrogen is seen as a promising solution due to its high energy density and zero-emission combustion. The PEM electrolyze combined with renewable energy power generation is an effective method to solve the problem of hydrogen production. The market competitiveness of PEM electrolyte will be enhanced in the future and the equipment cost can be reduced by 35.8%. The fast dynamic response performance of PEM electrolyzes especially during start-up and shutdown affects system flexibility and stability. The 190 Nm3/h test platform is established to study the fast dynamic response performance considering the cold startup thermal start-up and shutdown behaviors. The results shown that the 190 Nm³/h PEM electrolyze required 6340 s to achieve cold start-up 1100 s to achieve thermal start-up and 855 s to complete shutdown. When operating stably the temperature fluctuation of the PEM remains below 5 °C demonstrating the excellent temperature control performance. However during cold start-up and shutdown the concentrations of hydrogen and oxygen fluctuate significantly which can easily lead to a decrease in system performance. These findings provide guidance for optimizing the design and operating parameters of PEM Electrolyze systems.
Learning in Green Hydrogen Production: Insights from a Novel European Dataset
Jun 2025
Publication
The cost reduction of electrolysers is critical for scaling up green hydrogen production and achieving decarbonization targets. This study presents a novel and comprehensive dataset of electrolyser projects in Europe. It includes full cost and capacity details for each project and capturing project-specific characteristics such as technology type location and project type for the period 2005–2030. We apply the learning curve methodology to assess cost reductions across different electrolyser technologies and project sizes. Our findings indicate a significant learning effect for PEM and AEL electrolysers in the last 20 years with learning rates of 32.1% and 22.9% respectively. While AEL cost reductions are primarily driven by scaling effects PEM electrolysers benefit from both technological advancements and economies of scale. Small-scale electrolysers exhibit a stronger learning effect (25%) whereas large-scale projects show no clear cost reductions due to their early stage of deployment. Projections based on our learning rates suggest that reaching Europe’s 2030 target of 40 GW electrolyser capacity would require an estimated total investment of 14 billion EUR. These results align closely with previous studies and such predictions are closed to estimates from other organization. The dataset is publicly available allowing for further analysis and periodic updates to track cost trends.
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