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This review paper provides a critical examination of underground hydrogen storage (UHS) as a viable solution for large-scale energy storage, surpassing 10 GWh capacities, and contrasts it with aboveground methods. It exploes into the challenges posed by hydrogen injection, such as the potential for hydrogen loss and alterations in the petrophysical and petrographic characteristics of rock structures, which could compromise the efficiency of UHS systems. Central to our analysis is a detailed overview of hydrogen solubility across various solvents, an extensive database of potential mineralogical reactions within underground storage environments, and their implications for hydrogen retention. We particularly focus on the effects of these reactions on the porosity of reservoir and cap rocks, the role of diffusion in hydrogen loss, and the consequences of multiphase flow induced by hydrogen injection. Our findings highlight the critical mineralogical reactions—specifically, goethite reduction and calcite dissolution—and their pronounced impact on increasing cap rock porosity. We underscore a notable discovery: hydrogen's solubility in non-aqueous phases is significantly higher than in aqueous phases, nearly an order of magnitude greater. The paper not only presents quantitative insights into the mechanisms of hydrogen loss but also pinpoints areas in need of further research to deepen our understanding of UHS dynamics. By identifying these research gaps, we aim to guide future studies towards enhancing the operational efficiency and safety of UHS facilities, thereby supporting the transition towards sustainable energy systems. This work is pivotal for industry stakeholders seeking to optimize UHS practices, ensuring both the effective utilization of hydrogen as a clean energy carrier and the advancement of global sustainable energy goals.
This review paper provides a critical examination of underground hydrogen storage (UHS) as a viable solution for large-scale energy storage, surpassing 10 GWh capacities, and contrasts it with aboveground methods. It exploes into the challenges posed by hydrogen injection, such as the potential for hydrogen loss and alterations in the petrophysical and petrographic characteristics of rock structures, which could compromise the efficiency of UHS systems. Central to our analysis is a detailed overview of hydrogen solubility across various solvents, an extensive database of potential mineralogical reactions within underground storage environments, and their implications for hydrogen retention. We particularly focus on the effects of these reactions on the porosity of reservoir and cap rocks, the role of diffusion in hydrogen loss, and the consequences of multiphase flow induced by hydrogen injection. Our findings highlight the critical mineralogical reactions—specifically, goethite reduction and calcite dissolution—and their pronounced impact on increasing cap rock porosity. We underscore a notable discovery: hydrogen's solubility in non-aqueous phases is significantly higher than in aqueous phases, nearly an order of magnitude greater. The paper not only presents quantitative insights into the mechanisms of hydrogen loss but also pinpoints areas in need of further research to deepen our understanding of UHS dynamics. By identifying these research gaps, we aim to guide future studies towards enhancing the operational efficiency and safety of UHS facilities, thereby supporting the transition towards sustainable energy systems. This work is pivotal for industry stakeholders seeking to optimize UHS practices, ensuring both the effective utilization of hydrogen as a clean energy carrier and the advancement of global sustainable energy goals.
In the paper, the author develops experimental research methods and studies the specifics of gas mixture dissolution in a liquid where gases have different Henry's constants as well as the mutual interference of gases with different solubilities in a liquid during the dissolution process. It is shown that the dissolution rate of the studied pure gases in a liquid is proportional to their Henry's constants, and the dissolution rate of a gas mixture in a liquid is close to the dissolution rate of that gas in the mixture that has a higher Henry's constant. It was found that when a gas mixture containing a highly soluble gas is dissolved, interfacial surface turbulence (interfacial surface convection) occurs, which leads to an increase in the dissolution rate of the gas with lower solubility, that is, to an increase in the mass transfer coefficient (β) for that gas. The experimental studies showed that when several gases dissolved in a liquid are simultaneously desorbed into a floating-up bubble, the contribution of each gas is proportional to its solubility coefficient and does not depend on the concentration of these gases in the liquid.
Basic physical processes proceeding in hydrocarbon fuels during operation are the following: evaporation, stratification, contamination with impurities (gaseous, liquid, and mechanical), and settling of high-melting components during cooling, as well as the mixing of hydrocarbon fuels of various groups and grades in tanks and hauling equipment as well as during pipeline transportation. The fuel quality changes the most when products that differ significantly in their physical and chemical properties are mixed. The principle of the technology for adjusting the fractional composition of the fuel proposed in the article is as follows: a mixture of petroleum products is bubbled with gas (air, nitrogen), while the free volume is continuously pumped out by a vacuum system, a vacuum close to saturated is maintained in the technological tank, the vapor pressure of the more volatile component of the liquid mixture. The article assesses the possibility of using this technology for separating a mixture, derives a formula for determining the mass of a highly volatile liquid separated from a mixture, and gives recommendations on the technological parameters of improving the quality of fuel in terms of fractional composition by the method of forced gas boiling (PGV) in a vacuum and presents a theoretical justification of the proposed technology.
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