Abstract:A kinetic model has been developed, describing the kinetics of the hydrogen storage reactions in hydrideforming materials under equilibrium conditions. Based on first principles chemical reaction kinetics and statistical thermodynamics, the model is able to describe the complex processes occurring in hydrogen storage systems, including phase transitions. A complete set of equations, governing pressure-composition isotherms in both solid-solution and two-phase coexistence regions has been obtained. General expr… Show more
“…After the charge-transfer reaction at the electrode/electrolyte interface of the hydride-forming material ͑M s ͒ has been initiated, atomic hydrogen is chemically adsorbed ͑H ad ͒ at the electrode surface and is, subsequently, converted into the absorbed state ͑H abs ͒ and transported to the bulk of the hydride-forming material ͑M b ͒ by conventional solid-state diffusion. 9,12,21 In Fig. 1, the normalized hydrogen concentration in the bulk of the MH electrode is represented by x, and the normalized surface concentration is represented by , which is also known as the surface coverage.…”
Section: Modelmentioning
confidence: 99%
“…12 All above models have been successfully applied to simulate the isotherms of various hydride-forming materials, including AB 5 -based and Mg-based alloys. [6][7][8][9][11][12][13] In the present paper, a further extension of the EKM is proposed to include the dynamic electrochemical ͑de͒hydrogenation kinetics, i.e., to include the exchange current density of the charge-transfer reaction, electrical double-layer charging, and ͑instantaneous͒ phase transition. The electrode/electrolyte interface properties are described by conventional electrochemical parameters, i.e., by the exchange current density and specific electrical double-layer capacitance.…”
mentioning
confidence: 99%
“…12 This model was proposed as an extension of the KM. 9 It is also based on the first principles of electrochemical reaction kinetics and statistical thermodynamics and describes the complex, multistage, electrochemical ͑de͒hydrogena-tion process. A complete set of equations has been derived, describing the equilibrium hydrogen partial pressure and equilibrium electrode potential as a function of hydrogen content in both the solidsolution and two-phase coexistence regions.…”
mentioning
confidence: 99%
“…10 Combining the thermodynamics and kinetics offered an interesting opportunity to estimate not only the hydrogen storage-related thermodynamic parameters but also the relevant kinetic reaction rates and rate constants. 9,11 Finally, an electrochemical kinetic model ͑EKM͒ was developed, describing the electrochemical hydrogen storage in hydride-forming materials under equilibrium conditions. 12 This model was proposed as an extension of the KM.…”
mentioning
confidence: 99%
“…9 KM is based on the principles of statistical thermodynamics, described in LGM, [6][7][8] and also takes into account the complex gas-phase ͑de͒hydrogenation kinetics. The advantage of this kinetic approach is that it can, in principle, describe both equilibrium and nonequilibrium ͑dynamic͒ conditions.…”
The recently presented electrochemical kinetic model, describing the electrochemical hydrogen storage in hydride-forming materials, was extended by the description of the solid/electrolyte interface, i.e., the charge-transfer kinetics and electrical double-layer charging. A complete set of equations was derived, describing the equilibrium hydrogen partial pressure, the equilibrium electrode potential, the exchange current density, and the electrical double-layer capacitance as a function of hydrogen content in both solid-solution and two-phase coexistence regions. The model was applied to simulate isotherms of Pd thin films with nominal thicknesses of 200 and 10 nm. The model demonstrates good agreement between the simulation results and experimental data.
“…After the charge-transfer reaction at the electrode/electrolyte interface of the hydride-forming material ͑M s ͒ has been initiated, atomic hydrogen is chemically adsorbed ͑H ad ͒ at the electrode surface and is, subsequently, converted into the absorbed state ͑H abs ͒ and transported to the bulk of the hydride-forming material ͑M b ͒ by conventional solid-state diffusion. 9,12,21 In Fig. 1, the normalized hydrogen concentration in the bulk of the MH electrode is represented by x, and the normalized surface concentration is represented by , which is also known as the surface coverage.…”
Section: Modelmentioning
confidence: 99%
“…12 All above models have been successfully applied to simulate the isotherms of various hydride-forming materials, including AB 5 -based and Mg-based alloys. [6][7][8][9][11][12][13] In the present paper, a further extension of the EKM is proposed to include the dynamic electrochemical ͑de͒hydrogenation kinetics, i.e., to include the exchange current density of the charge-transfer reaction, electrical double-layer charging, and ͑instantaneous͒ phase transition. The electrode/electrolyte interface properties are described by conventional electrochemical parameters, i.e., by the exchange current density and specific electrical double-layer capacitance.…”
mentioning
confidence: 99%
“…12 This model was proposed as an extension of the KM. 9 It is also based on the first principles of electrochemical reaction kinetics and statistical thermodynamics and describes the complex, multistage, electrochemical ͑de͒hydrogena-tion process. A complete set of equations has been derived, describing the equilibrium hydrogen partial pressure and equilibrium electrode potential as a function of hydrogen content in both the solidsolution and two-phase coexistence regions.…”
mentioning
confidence: 99%
“…10 Combining the thermodynamics and kinetics offered an interesting opportunity to estimate not only the hydrogen storage-related thermodynamic parameters but also the relevant kinetic reaction rates and rate constants. 9,11 Finally, an electrochemical kinetic model ͑EKM͒ was developed, describing the electrochemical hydrogen storage in hydride-forming materials under equilibrium conditions. 12 This model was proposed as an extension of the KM.…”
mentioning
confidence: 99%
“…9 KM is based on the principles of statistical thermodynamics, described in LGM, [6][7][8] and also takes into account the complex gas-phase ͑de͒hydrogenation kinetics. The advantage of this kinetic approach is that it can, in principle, describe both equilibrium and nonequilibrium ͑dynamic͒ conditions.…”
The recently presented electrochemical kinetic model, describing the electrochemical hydrogen storage in hydride-forming materials, was extended by the description of the solid/electrolyte interface, i.e., the charge-transfer kinetics and electrical double-layer charging. A complete set of equations was derived, describing the equilibrium hydrogen partial pressure, the equilibrium electrode potential, the exchange current density, and the electrical double-layer capacitance as a function of hydrogen content in both solid-solution and two-phase coexistence regions. The model was applied to simulate isotherms of Pd thin films with nominal thicknesses of 200 and 10 nm. The model demonstrates good agreement between the simulation results and experimental data.
A new approach to describe the equilibrium kinetics of chemisorption is proposed. The description of the system is based on first-principles chemical reaction kinetics and statistical thermodynamics. The rate constants are described by using a novel way of activation energy characterization. General expressions for equilibrium gas pressure isotherms and forward/backward reaction rates are obtained as a function of surface coverage. A strong influence of attraction and repulsion interaction energies between the adsorbed species on the equilibrium kinetics is found.
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