2024
DOI: 10.1051/e3sconf/202452401016
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Technical and economic analysis, calculation and justification of hydrogen production through solar thermochemical reactor in Republic of Uzbekistan

Kh.S. Akhmadov,
N.M. Nazarova,
A.R. Juraev
et al.

Abstract: In this study, the economic viability of hydrogen production in the Republic of Uzbekistan was evaluated. Specifically, the costs and breakeven prices for hydrogen production were analysed across five selected regions within the Republic. The analysis focused on the potential reduction in production costs achievable through investor engagement. Among the regions studied, Tashkent exhibited the lowest production cost at 1.2 USD/kg. In scenarios devoid of investor participation, the levelized cost of hydrogen (L… Show more

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Cited by 3 publications
(1 citation statement)
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“…where, 𝜌 is the density (kg/m 3 ), 𝐢 𝑝 is the specific heat capacity at constant stress (J/(kgβ€’K)), 𝑇 is the absolute temperature (K), 𝑒 π‘‘π‘Ÿπ‘Žπ‘›π‘  is the velocity vector of translational motion (m/s), π‘ž is the heat flux by conduction (W/m 2 ), π‘ž π‘Ÿ is the heat flux by radiation (W/m 2 ), 𝛼 is the coefficient of thermal expansion (1/K), 𝑆 is the second Piola-Kirchhoff stress tensor (Pa), 𝑄 contains additional heat sources (W/m 3 ) [15][16][17][18][19].…”
Section: For Heat Transfer In Fluidsmentioning
confidence: 99%
“…where, 𝜌 is the density (kg/m 3 ), 𝐢 𝑝 is the specific heat capacity at constant stress (J/(kgβ€’K)), 𝑇 is the absolute temperature (K), 𝑒 π‘‘π‘Ÿπ‘Žπ‘›π‘  is the velocity vector of translational motion (m/s), π‘ž is the heat flux by conduction (W/m 2 ), π‘ž π‘Ÿ is the heat flux by radiation (W/m 2 ), 𝛼 is the coefficient of thermal expansion (1/K), 𝑆 is the second Piola-Kirchhoff stress tensor (Pa), 𝑄 contains additional heat sources (W/m 3 ) [15][16][17][18][19].…”
Section: For Heat Transfer In Fluidsmentioning
confidence: 99%