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Temperature Control Strategy for Hydrogen Fuel Cell Based on IPSO-Fuzzy-PID
Dec 2024
Publication
Hydrogen fuel cell water-thermal management systems suffer from slow response time system vibration and large temperature fluctuations of load current changes. In this paper Logistic chaotic mapping adaptively adjusted inertia weight and asymmetric learning factors are integrated to enhance the particle swarm optimization (PSO) algorithm and combine it with fuzzy control to propose an innovative improved particle swarm optimization-Fuzzy control strategy. The use of chaotic mapping to initialize the particle population effectively enhances the variety within the population which subsequently improves the ability to search globally and prevents the algorithm from converging to a local optimum solution prematurely; by improving the parameters of learning coefficients and inertia weight the global and local search abilities are balanced at different stages of the algorithm so as to strengthen the algorithm’s convergence certainty while reducing the dependency on expert experience in fuzzy control. In this article a fuel cell experimental platform is constructed to confirm the validity and efficiency of the recommended strategy and the analysis reveals that the improved particle swarm optimization (IPSO) algorithm demonstrates better convergence performance than the standard PSO algorithm. The IPSO-Fuzzy-PID management approach is capable of providing a swift response and significantly diminishing the overshoot in the system’s performance to maintain the system’s safe and stable execution.
Underground Hydrogen Storage in Salt Caverns: Laboratory Experiments to Determine Integrity of Rock Salt and Wellbore Through Effective Permeability Measurements
Dec 2024
Publication
Underground hydrogen storage in salt caverns is a promising solution for short-term storage allowing multiple cycles per year. This study experimentally investigates the integrity of such caverns and their wellbores under operating conditions typical of German salt caverns. Specifically we measure the permeability of rock salt cement (API Class G and High Magnesium Resistant (HMR+)) rock salt-anhydrite composites cement-salt composites and casing-cement composites. Rock salt demonstrates extremely low permeability (10− 23 m2 ) while casing-cement composites (HMR+) exhibit permeabilities similar to pure cement (10− 20 m2 or lower). Both salt-cement (HMR+) and casing-cement (HMR+) composites meet the strict tightness requirements for hydrogen storage (10− 19 m2 or less). While thin anhydrite layers in rock salt can increase permeability compaction can reduce it to levels comparable to rock salt. This study’s novelty lies in evaluating the feasibility of a real German cavern for hydrogen storage using a custom-built transient permeability setup capable of testing casing-cement composites at a 1:1 wellbore scale.
A General Criterion for the Design and Operation of Flexible Hydrogen Storage in Power-to-X Processed
Dec 2024
Publication
This paper introduces a general criterion for the optimal design and operation of hydrogen storage tanks. Specifically the proposed procedure identifies the optimal delivery schedule that minimizes the capacity of material storage systems. Indeed many manufacturing processes need some buffer storage to administer mass flows appropriately according to the operating needs (one class above all: Power-to-X processes) and have one of their highest expenditures right in those tanks when proving not sufficiently flexible. Hence the novelty of the proposed method lies in a rigorous mathematical formulation that converts arbitrarily fluctuating inlet streams into optimally fluctuating outlet streams that minimize the storage volume and comply with different operating requirements. The criterion is validated by considering the techno-economic assessment of a chemical plant featuring a dedicated green hydrogen production facility that feeds the process. Specifically the required capacity of the “Flexible” hydrogen buffer storage which connects the green hydrogen generation system to the conversion process significantly decreases by 91.31%–99.31% (depending on the flexibility ranges enabled by the downstream conversion process) compared to the “Rigid” storage alternative based on a constant outlet mass flow withdrawal coinciding with the hydrogen consumption rate at nominal operating conditions. Correspondingly the resulting levelized cost of hydrogen benefits accordingly ranging from 4.19 to 6.03 USD/kg (California 2023).
Leakage Rates of Hydrogen-methane Gas Blends under Varying Pressure Conditions
Nov 2024
Publication
Integration of hydrogen into the existing natural gas infrastructure is considered a potential pathway that can accelerate the incorporation of hydrogen into the energy sector. While blending renewable hydrogen with natural gas offers advantages such as reduced carbon intensity and the ability to utilize existing infrastructure for hydrogen storage and transportation there are several concerns including leakage and associated issues. Un derstanding the behavior of hydrogen blended with natural gas in the existing infrastructure is crucial to ensure safe and efficient integration. In this study the leakage rates of mixtures of hydrogen and methane at different molar concentrations (5% 10% 20% and 50% hydrogen) through both precision machined orifices and com mon pipe fitting threads were investigated. The experiments showed that the leakage rates of these mixtures increased as the hydrogen content increased; however gas chromatography (GC) analysis showed that hydrogen did not leak preferentially at a greater rate than methane. The results indicate that mixing hydrogen with methane can increase the volume of gas leakage under the same pressure conditions. These findings suggest that mixing hydrogen with natural gas may result in increased volumetric flow rate of gas leaks but hydrogen alone does not leak preferentially to methane.
Recent Advances in Combustion Science Related to Hydrogen Safety
Dec 2024
Publication
Hydrogen is a key pillar in the global Net Zero strategy. Rapid scaling up of hydrogen production transport distribution and utilization is expected. This entails that hydrogen which is traditionally an industrial gas will come into proximity of populated urban areas and in some situations handled by the untrained public. To realize all their benefits hydrogen and its technologies must be safely developed and deployed. The specific properties of hydrogen involving wide flammability range low ignition energy and fast flame speed implies that any accidental release of hydrogen can be easily ignited. Comparing with conventional fuels combustion systems fueled by hydrogen are also more prone to flame instability and abnormal combustion. This paper aims to provide a comprehensive review about combustion research related to hydrogen safety. It starts with a brief introduction which includes some overview about risk analysis codes and standards. The core content covers ignition fire explosions and deflagration to detonation transition (DDT). Considering that DDT leads to detonation and that detonation may also be induced directly under special circumstances the subject of detonation is also included for completeness. The review covers laboratory medium and large-scale experiments as well as theoretical analysis and numerical simulation results. While highlights are provided at the end of each section the paper closes with some concluding remarks highlighting the achievements and key knowledge gaps.
Projecting Technological Advancement of Electrolyzers and the Impact on the Competitiveness of Hydrogen
Dec 2024
Publication
Green hydrogen has the potential to decarbonize hard-to-abate sectors and processes and should therefore play an important role in the energy system in achieving climate goals. However the main hydrogen supply is still based on fossil fuels and only limited amounts of electrolyzers have been installed. Switching from fossil-based fuel sources to green hydrogen is highly dependent on when and at what price green hydrogen will become available which in turn is dependent on the technological development of electrolyzers. In this paper we apply the experience curve methodology to project the capital expenditure and electrical consumption developments of the three main electrolysis technologies: alkaline proton exchange membrane and solid oxide electrolysis. Based on our calculations we expect that both AEL and PEM will reach similar costs by 2030 of around 300 e per kW and SOEC will remain the most expensive technology with a considerable cost reduction down to 828 e per kW. The electrical consumptions will fall to 4.23 kWh per Nm3 for AEL 3.86 kWh per Nm3 for PEM and 3.05 kWh per Nm3 for SOEC. Based on this technological progress we calculate that the levelized cost of hydrogen will be reduced to 2.43–3.07 e per kg. To reach lower levelized cost of hydrogen notable reductions in electricity (purchase) cost are required.
Hydrogen Diffusion into Water and Cushion Gases - Relevance for Hydrogen Geo-storage
Dec 2024
Publication
Hydrogen (H2) has been recognized as a promising solution to reduce carbon dioxide (CO2) emissions. H2 is considered a green energy carrier for energy storage transport and usage and it can be produced from renewable energy resources (such as solar hydropower and wind energy). However H2 is a highly diffusive compound compared to other natural gases raising concerns about the possibility of H2 loss in geo-storage (e.g. in underground geological formations such as depleted oil/gas reservoirs aquifers or shale formations) or H2 leak via pipelines when blending H2 with natural gas in existing pipeline systems. Thus understanding H2 diffusion in subsurface formations and pipeline systems is vital. However despite its importance only limited data is available to assess the above situations. Therefore in this study molecular dynamics simulations were used to predict the self-diffusion coefficients of H2 in water and cushion gases (CH4 and N2) at relevant geothermal conditions (i.e. 300 K–373 K and pressures up to 50 MPa). The findings showed that H2 self-diffusion in methane and nitrogen increases with increasing temperature but decreases with increasing pressure. However H2 selfdiffusion in water increases with increasing temperature but is not impacted by increasing or decreasing pres sure. The results also indicated that the rate of H2 self-diffusion in cushion gas is faster than in water about exceeding two-digit times. Furthermore the outcomes reported extended or new data on H2 self-diffusion for the binary system of H2–H2O H2–CH4 and H2–N2. This study is beneficial and contributes to assessing efficiency and safety for executing H2 transportation and underground hydrogen storage (UHS) schemes.
Decarbonisation and Hydrogen Integration of Steel Industries: Recent Development, Challenges and Technoeconomics Analysis
Feb 2023
Publication
The steel industry is one of the major sources of greenhouse gas emissions with significant energy demand. Currently 73% of the world’s steel is manufactured through the coal-coke-based blast furnace-basic oxygen furnace route (BF-BOF) emitting about two tonnes of CO2 per tonne of steel produced. This review reports the major technologies recent developments challenges and technoeconomic comparison of steelmaking technol ogies emphasising the integration of hydrogen in emerging and established ironmaking and steelmaking pro cesses. Significant trials are underway especially in Germany to replace coal injected in the tuyeres of the blast furnace with hydrogen. However it is not clear that this approach can be extended beyond 30% replacement of coke because of the associated technical challenges. Direct smelting and fluidised bed technologies can emit 20%–30% less CO2 without carbon capture and storage utilisation. The implications of hydrogen energy in these technologies as a substitute for natural gas and coal are yet to be fully explored. A hydrogen-based direct reduction of iron ore (DRI) and steel scrap melting in an electric arc furnace (EAF) appeared to be the most mature technological routes to date capable of reducing CO2 emission by 95% but rely on the availability of rich iron concentrates as feed materials. Shaft furnace technologies are the common DRI-making process with a share of over 72% of the total production. The technology has been developed with natural gas as the main fuel and reductant. However it is now being adapted to operate predominantly on hydrogen to produce a low-carbon DRI product. Plasma and electrolysis-based iron and steelmaking are some of the other potential technologies for the application of hydrogen with a CO2 reduction potential of over 95%. However these technologies are in the preliminary stage of development with a technology readiness level of below 6. There are many technological challenges for the application of hydrogen in steel manufacturing such as challenges in distributing heat due to the endothermic H2 reduction process balancing carbon content in the product steel (particularly using zerocarbon DRI) removal of gangue materials and sourcing of cost-competitive renewable hydrogen and highquality iron ore (65>Fe). As iron ore quality degrades worldwide several companies are considering melting DRI before steelmaking possibly using submerged arc technology to eliminate gangue materials. Hence sig nificant laboratory and pilot-scale demonstrations are required to test process parameters and product qualities. Our analysis anticipates that hydrogen will play an instrumental role in decarbonising steel industries by 2035.
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