Transmission, Distribution & Storage
Changes in the Operating Conditions of Distribution Gas Networks as a Function of Altitude Conditions and the Proportion of Hydrogen in Transported Natural Gas
Nov 2025
Publication
The article presents a comparison between the pressure conditions of a real low-pressure gas network and the results of hydraulic calculations obtained using various simulation programs and empirical equations. The calculations were performed using specialized gas network analysis software: STANET (ver 10.0.26) SimNet SSGas 7 and SONET. Additionally the simulation results were compared with calculations based on the empirical Darcy–Weisbach and Renouard equations. In the first part of the analysis two calculation models were compared. In one model the geodetic elevation of individual network nodes was included (elevation-aware model) while in the second calculations were performed without considering node elevation (flat model). For low-pressure gas networks accounting for elevation is critical due to the presence of the pressure recovery phenomenon which does not occur in medium- and high-pressure networks. Furthermore considering the growing need to increase the share of renewable energy the study also examined the network’s operating conditions when using natural gas–hydrogen mixtures. The following hydrogen concentrations were considered: 2.5% 5.0% 10.0% 20.0% and 50.0%. The results confirm the importance of incorporating elevation data in the modeling of low-pressure gas networks. This is supported by the small differences between calculated results and actual pressure measurements taken from the operating network. Moreover increasing the hydrogen content in the mixture intensifies the pressure recovery effect. The hydraulic results obtained using different computational tools were consistent and showed only minor discrepancies.
Correlation Development for Para-to-Ortho Hydrogen Catalytic Conversion in Vapor-Cooled Shields of Hydrogen Tanks
Nov 2025
Publication
The cooling effect from the para-ortho hydrogen conversion (POC) combined with a vaporcooled shield (VCS) and multi-layer insulation (MLI) can effectively extend the storage duration of liquid hydrogen in cryogenic tanks. However there is currently no effective and straightforward empirical correlation available for predicting the catalytic POC efficiency in VCS pipelines. This study focuses on the development of correlations for the catalytic conversion of para-hydrogen to ortho-hydrogen in pipelines particularly in the context of cryogenic hydrogen storage systems. A model that incorporates the Langmuir adsorption characteristics of catalysts and introduces the concept of conversion efficiency to quantify the catalytic process’s performance is introduced. Experimental data were obtained in the temperature range of 141.9~229.9 K from a cryogenic hydrogen catalytic conversion facility where the effects of temperature pressure and flow rate on the catalytic conversion efficiency were analyzed. Based on a validation against the experimental data the proposed model offers a reliable method for predicting the cooling effects and optimizing the catalytic conversion process in VCS pipelines which may contribute to the improvement of liquid hydrogen storage systems enhancing both the efficiency and duration of storage.
Tailored Heat Treatments to Characterise the Fracture Resistance of Critical Weld Regions in Hydrogen Transmission Pipelines
Nov 2025
Publication
A new protocol is presented to directly characterise the toughness of microstructural regions present within the weld heat-affected zone (HAZ) the most vulnerable location governing the structural integrity of hydrogen transport pipelines. Heat treatments are tailored to obtain bulk specimens that replicate predominantly ferriticbainitic bainitic and martensitic microstructures present in the HAZ. These are applied to a range of pipeline steels to investigate the role of manufacturing era (vintage versus modern) chemical composition and grade. The heat treatments successfully reproduce the hardness levels and microstructures observed in the HAZ of existing natural gas pipelines. Subsequently fracture experiments are conducted in air and pure H2 at 100 bar revealing a reduced fracture resistance and higher hydrogen embrittlement susceptibility of the HAZ microstructures with initiation toughness values as low as 32 MPa√ m. The findings emphasise the need to adequately consider the influence of microstructure and hard brittle zones within the HAZ.
Effects of Sensitization on Hydrogen Embrittlement Behavior in 304 Stainless Steel
Nov 2025
Publication
This study investigated the hydrogen embrittlement behavior of 304 stainless steel under the combined condition of sensitization and hydrogen pre-charging. Specifically hydrogen trapping analysis and martensite transformation mapping were used to examine the respective roles of carbide precipitation and chromium depletion and key factors were identified through fractographic observations. Sensitization was simulated at 650 ◦C for 50 h followed by hydrogen pre-charging at 250 ◦C under 50 MPa for 3.5 days. Under hydrogen pre-charging sensitized specimens showed a 9.3 % drop in ultimate tensile strength a 17.3 % reduction in elongation and a 16 % decrease in relative reduction of area indicating higher hydrogen embrittlement susceptibility. Hydrogen desorption analysis revealed a redistribution of hydrogen from reversible to irreversible traps consistent with 139 nm coarsened Cr23C6 carbides while phase mapping revealed extensive formation of strain-induced martensite along grain boundaries and within grains. These martensitic regions accelerated hydrogen transport and promoted strain localization leading to the disappearance of intragranular dimples and the development of intergranular cracking. The results demonstrate that strain-induced martensite formed in chromiumdepleted regions is the dominant factor governing post-sensitization hydrogen embrittlement emphasizing the necessity of controlling chromium depletion to maintain the stability of the austenitic matrix in hydrogen environments.
Advanced Analytical Modeling of Polytropic Gas Flow in Pipelines: Unifying Flow Regimes for Efficient Energy Transport
Oct 2025
Publication
In the present work a new analytical model of polytropic flow in constant-diameter pipelines is developed to accurately describe the flow of compressible gases including natural gas and hydrogen explicitly accounting for heat exchange between the fluid and the environment. In contrast to conventional models that assume isothermal or adiabatic conditions the proposed model simultaneously accounts for variations in pressure temperature density and entropy i.e. it is based on a realistic polytropic gas flow formulation. A system of differential equations is established incorporating the momentum continuity energy and state equations of the gas. An implicit closed-form solution for the specific volume along the pipeline axis is then derived. The model is universal and allows the derivation of special cases such as adiabatic isothermal and isentropic flows. Numerical simulations demonstrate the influence of heat flow on the variation in specific volume highlighting the critical role of heat exchange under real conditions for the optimization and design of energy systems. It is shown that achieving isentropic flow would require the continuous removal of frictional heat which is not practically feasible. The proposed model therefore provides a clear reproducible and easily visualized framework for analyzing gas flows in pipelines offering valuable support for engineering design and education. In addition a unified sensitivity analysis of the analytical solutions has been developed enabling systematic evaluation of parameter influence across the subsonic near-critical and heated flow regimes.
Numerical Study of Liquid Hydrogen Internal Flow in Liquid Hydrogen Storage Tank
Oct 2025
Publication
As a key zero-carbon energy carrier the accurate measurement of liquid hydrogen flow in its industrial chain is crucial. However the ultra-low temperature ultra-low density and other properties of liquid hydrogen can introduce calibration errors. To enhance the measurement accuracy and reliability of liquid hydrogen flow this study investigates the heat and mass transfer within a 1 m3 non-vented storage tank during the calibration process of a liquid hydrogen flow standard device that integrates combined dynamic and static gravimetric methods. The vertical tank configuration was selected to minimize the vapor–liquid interface area thereby suppressing boil-off gas generation and enhancing pressure stability which is critical for measurement accuracy. Building upon research on cryogenic flow standard devices as well as tank experiments and simulations this study employs computational fluid dynamics (CFD) with Fluent 2024 software to numerically simulate liquid hydrogen flow within a non-vented tank. The thermophysical properties of hydrogen crucial for the accuracy of the phase-change simulation were implemented using high-fidelity real-fluid data from the NIST Standard Reference Database as the ideal gas law is invalid under the cryogenic conditions studied. Specifically the Lee model was enhanced via User-Defined Functions (UDFs) to accurately simulate the key phasechange processes involving coupled flash evaporation and condensation during liquid hydrogen refueling. The simulation results demonstrated good agreement with NASA experimental data. This study systematically examined the effects of key parameters including inlet flow conditions and inlet liquid temperature on the flow characteristics of liquid hydrogen entering the tank and the subsequent heat and mass transfer behavior within the tank. The results indicated that an increase in mass flow rate elevates tank pressure and reduces filling time. Conversely a decrease in the inlet liquid hydrogen temperature significantly intensifies heat and mass transfer during the initial refueling stage. These findings provide important theoretical support for a deeper understanding of the complex physical mechanisms of liquid hydrogen flow calibration in non-vented tanks and for optimizing calibration accuracy.
Enhancing Regional Integrated Energy Systems Through Seasonal Hydrogen Storage: Insights from a Stackelberg Game Model
Nov 2025
Publication
This study enhances regional integrated energy systems by proposing a Stackelberg planning–operation model with seasonal hydrogen storage addressing source–network separation. An equilibrium algorithm is developed that integrates a competitive search routine with mixed-integer optimization. In the price–energy game framework the hydrogen storage operator is designated as the leader while energy producers load aggregators and storage providers act as followers facilitating a distributed collaborative optimization strategy within the Stackelberg game. Using an industrial park in northern China as a case study the findings reveal that the operator’s initiative results in a revenue increase of 38.60% while producer profits rise by 6.10% and storage-provider profits surge by 108.75%. Additionally renewable accommodation reaches 93.86% reflecting an absolute improvement of 20.60 percentage points. Total net energy imbalance decreases by 55.70% and heat-loss load is reduced by 31.74%. Overall the proposed approach effectively achieves cross-seasonal energy balancing and multi-party gains providing an engineering-oriented reference for addressing energy imbalances in regional integrated energy systems.
Application of Machine Learning and Data Augmentation Algorithms in the Discovery of Metal Hydrides for Hydrogen Storage
Nov 2025
Publication
The development of efficient and sustainable hydrogen storage materials is a key challenge for realizing hydrogen as a clean and flexible energy carrier. Among various options metal hydrides offer high volumetric storage density and operational safety yet their application is limited by thermodynamic kinetic and compositional constraints. In this work we investigate the potential of machine learning (ML) to predict key thermodynamic properties—equilibrium plateau pressure enthalpy and entropy of hydride formation—based solely on alloy composition using Magpie-generated descriptors. We significantly expand an existing experimental dataset from ~400 to 806 entries and assess the impact of dataset size and data augmentation using the PADRE algorithm on model performance. Models including Support Vector Machines and Gradient Boosted Random Forests were trained and optimized via grid search and cross-validation. Results show a marked improvement in predictive accuracy with increased dataset size while data augmentation benefits are limited to smaller datasets and do not improve accuracy in underrepresented pressure regimes. Furthermore clustering and cross-validation analyses highlight the limited generalizability of models across different material classes though high accuracy is achieved when training and testing within a single hydride family (e.g. AB2). The study demonstrates the viability and limitations of ML for accelerating hydride discovery emphasizing the importance of dataset diversity and representation for robust property prediction.
A CFD Comparison of Interfacial Phase Change Models for Boil-off, Self-pressurisation and Thermal Stratification in Liquid Hydrogen Storage Tanks
Nov 2025
Publication
Liquid hydrogen (LH2 ) is a promising energy carrier for future clean fuel technologies. However its cryogenic storage and handling pose significant challenges particularly due to self-pressurisation and boil-off from ambient heat ingress. Accurate modelling of these phenomena is essential for the safe and efficient design of LH2 storage systems. A key aspect of such modelling is the selection and implementation of an appropriate interfacial phase change model. This study presents a comparative assessment of three widely used phase change models; the Schrage model the Modified Energy Jump (MeJ) model and the Lee model. A parametric study was conducted across three coefficients for each model with validation performed against five experimental benchmark cases from NASA’s K-Site and MHTB cryogenic tanks focusing on planar interface problems with thermally induced phase change under normal gravity. A CFD approach using STAR-CCM+ was employed to evaluate each model’s ability to predict tank pressure temperature and boil-off behaviour. The Schrage model demonstrated the most robust and accurate results exhibiting minimal sensitivity to coefficient variation and offering both numerical stability and physical fidelity. It demonstrated a maximum mean absolute percentage error (MAPE) of just 3.0% in its pressurisation predictions. The MeJ model showed comparable accuracy when its heat transfer coefficient was appropriately selected highlighting its reliance on an empirically derived coefficient. In contrast the Lee model performed the poorest exhibiting numerical divergence at high coefficient values and substantial deviation in its prediction of self-pressurisation with errors of up to 11% MAPE. These findings provide practical guidance for the selection and implementation of phase change models in CFD simulations and highlight key considerations for modelling LH2 storage tanks in industrial applications.
Thermal and Heat Transfer Dynamics in High Pressure, High Aspect Ratio Hydrogen Tank Filling Processes
Nov 2025
Publication
A thermodynamic modeling framework is introduced to describe hydrogen refueling station configurations and capture detailed thermal dynamics in vehicle tanks with large aspect ratios. With an aspect ratio larger than three axial discretization of temperature allows to recover accurate temperature profiles and show that the gas and liner temperature are always highest towards the rear of the tanks. The framework is validated against experimental data and used to investigate the internal heat transfer dynamics. As aspect ratio grows larger the amount of cooling received by the rear region decreases as the incoming turbulent jet does not reach the latter. The current thermal management strategy of pre-cooling is therefore limited showing marginal improvements even with a cooling temperature of -50 ◦C. Potential solutions are to increase the filling duration time or to carefully design the tank with higher thermal diffusivity and adequate external means of cooling.
Material Compatibility in Hydrogen Infrastructure: Challenges, Advances, and Future Prospects
Oct 2025
Publication
The adoption of hydrogen as a clean energy carrier depends heavily on the development of materials capable of enduring the extreme conditions associated with its production storage and transportation. This review critically evaluates the performance of metals polymers and composites in hydrogen-rich environments focusing on degradation mechanisms such as hydrogen embrittlement rapid gas decompression and long-term fatigue. Metals like carbon steels and high-strength alloys can experience a 30–50 % loss in tensile strength due to hydrogen exposure while polymers suffer from permeability increases and sealing degradation. Composite materials though strong and lightweight may lose up to 15 % of their mechanical properties over time in hydrogen environments. The review highlights current mitigation strategies including hydrogen-resistant alloys polymer blends protective coatings composite liners and emerging technologies like predictive modeling and AI-based material design. With hydrogen production expected to reach 500 GW globally by 2030 improving material compatibility and developing international standards are essential for scaling hydrogen infrastructure safely and cost-effectively. This work presents an integrated analysis of material degradation mechanisms highlights key challenges across metals polymers and composites in hydrogen environments and explores recent innovations and future strategies to enhance durability and performance in hydrogen infrastructure.
Computational Fluid Dynamic Modeling and Parametric Optimization of Hydrogen Adsorption in Stationary Hydrogen Tanks
Nov 2025
Publication
A. Ousegui and
B. Marcos
This study investigates hydrogen storage enhancement through adsorption in porous materials by coupling the Dubinin–Astakhov (D-A) adsorption model with H2 conservation equations (mass momentum and energy). The resulting system of partial differential equations (PDEs) was solved numerically using the finite element method (FEM). Experimental work using activated carbon as an adsorbent was carried out to validate the model. The comparison showed good agreement in terms of temperature distribution average pressure of the system and the amount of adsorbed hydrogen (H2). Further simulations with different adsorbents indicated that compact metal–organic framework 5 (MOF-5) is the most effective material in terms of H2 adsorption. Additionally the pair (273 K 800 s) remains the optimal combination of injection temperature and time. The findings underscore the prospective advantages of optimized MOF-5-based systems for enhanced hydrogen storage. These systems offer increased capacity and safety compared to traditional adsorbents. Subsequent research should investigate multi-objective optimization of material properties and system geometry along with evaluating dynamic cycling performance in practical operating conditions. Additionally experimental validation on MOF-5-based storage prototypes would further reinforce the model’s predictive capabilities for industrial applications.
A Comprehensive Review on the Compatability of Polymeric Materials for Hydrogen Transportation and Storage
Nov 2025
Publication
This review evaluates the current state of the art on polymeric materials for hydrogen transportation and storage highlighting the importance of developing a sustainable hydrogen infrastructure worldwide. It analyses different polymeric materials used for hydrogen transportation and storage applications including high-density polyethylene (HDPE) polytetrafluoroethylene (PTFE) polyimides (PI) polyether ether ketone (PEEK) polyamide ethylene propylene diene monomer (EPDM) polyvinylidene fluoride (PVDF) and fluorinated ethylene propylene (FEP). These materials are assessed using key characteristics such as hydrogen permeability mechanical strength chemical resistance and thermal stability. The review finds that while PEEK and polyimides exhibit the highest thermal stability (up to 400 °C) and pressure resistance (300–400 bar) HDPE remains the most cost-effective option for low-pressure applications. PTFE and FEP offer the lowest hydrogen permeability (<0.01 cm3 mm/m2·day·bar) making them ideal for sealing and lining in hydrogen storage systems. Furthermore key research gaps are identified and suggestions for future research and development directions are outlined. This comprehensive review is a valuable resource for researchers and engineers working towards sustainable hydrogen infrastructure development.
Unlocking Hydrogen Carrier Potential of the Yangtze River in China
Oct 2025
Publication
The Yangtze River as the world’s largest clean energy corridor links key economic regions and plays a crucial role in inland waterway transportation. However few studies have comprehensively evaluated the potential of the Yangtze River for cross-regional hydrogen transport. Here we develop a comprehensive integrated power and hydrogen supply chain (IPHSC) optimization model to evaluate the potential of cross-regional hydrogen transport via the Yangtze River. The IPHSC optimization model covers the entire hydrogen production-storage-transportation-utilization chain through cross-sector modeling of energy transportation water scheduling and environmental protection. Results show that in the 2060 carbon neutrality scenario the deployment of 62.2 kilotons of 574 differentiated liquid hydrogen (LH2) carrier ships could enable the transportation of 5018 kilotons (1512 million ton-km) of hydrogen annually meeting nearly 20% of the total electrolytic hydrogen demand across eight riverine provinces. Unlike west-to-east electricity transmission in China the central Yangtze River region is expected to become the main hub for hydrogen exports in the future. Compared with alternative methods such as transmission lines or pipelines LH2 carrier ships offer the lowest energy supply costs at 3 US cents/kWh for electricity and 5 US cents/kWh for hydrogen. Additionally a full-parameter attribution analysis of over 40 factors is conducted to assess variations in supply costs. Our study offers a thorough evaluation of the feasibility and economic benefits of hydrogen transportation via inland waterways providing a comprehensive multi-sectoral coupling assessment framework for regions with well-established inland waterway networks such as Europe and the United States.
Quantifying Conservatism in ASME B31.12 Option A for Hydrogen Pipeline Repurposing
Nov 2025
Publication
Hydrogen is a key enabler of the energy transition and repurposing existing natural gas pipelines offers a costeffective pathway for large-scale hydrogen transport. However hydrogen embrittlement raises integrity concerns and current design standards such as ASME B31.12 Option A adopt highly conservative safety margins without a quantified reliability basis. This study evaluates whether the conservative safety margins in ASME B31.12 Option A for hydrogen pipelines can be safely relaxed. A semi-elliptical flaw (depth 0.25t length 1.5t) is assessed using the Failure Assessment Diagram (FAD) method and Monte Carlo simulations with up to 2.5 × 107 iterations. Fracture toughness is fixed at 69.3 MPa√m while wall thickness and yield strength vary statistically. Three design scenarios explore safety factor products from 0.388 to 0.720 at 0 ◦C and 20 ◦C. Results show that flaw acceptability is maintained in all deterministic cases and the probability of failure remains below 10− 6 . No failures occur when the safety factor product drops below 0.637. The analysis uses only codified flaw assumptions and public material data. These findings confirm that Option A provides a highly conservative envelope and demonstrate the value of a reliability-based approach for assessing hydrogen pipeline repurposing while addressing the gap between prescriptive standards and quantified reliability. This integrated FAD–probabilistic framework demonstrates that Option A includes significant conservatism and supports a reliability-based approach to evaluate hydrogen pipeline repurposing without experimental inputs.
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