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Journal ArticleDOI

Magnesium hydride for energy storage applications: The kinetics of dehydrogenation under different working conditions

TL;DR: In this paper, a new approach to the kinetics of magnesium hydride dehydrogenation is considered, where a combined kinetic analysis method, which considers the thermodynamic of the process according to the microreversibility principle, has been used for performing the kinetic analysis of data obtained under different thermal schedules at hydrogen pressures ranging from high vacuum up to 20 bar.
About: This article is published in Journal of Alloys and Compounds.The article was published on 2016-10-05 and is currently open access. It has received 22 citations till now. The article focuses on the topics: Magnesium hydride & Dehydrogenation.

Summary (2 min read)

1. Introduction

  • Magnesium hydride is a material of the most interest for a number of technical applications, mainly as hydrogen storage material for PEM fuel cells, due to its large reversible storage capacity (7.6 mass%) of high purity hydrogen [1-5], and as a thermal energy storage system in thermosolar plants due to the high enthalpy of the hydrogenation-dehydrogenation reactions [6-10].
  • Moreover, magnesium has a relatively high abundance in earth.
  • For any of these two applications, the kinetics of the dehydrogenation-hydrogenation reactions is of paramount importance.
  • A very large number of studies of absorption and desorption of hydrogen in MgH2 and related compounds have been performed employing either volumetric analysis under isothermal conditions or thermogravimetry (TG) and differential scanning calorimetry (DSC) at linear rising temperature under a flow of hydrogen or an inert gas [11, 17-18, 21-28].
  • A proper kinetic analysis of reversible thermal decomposition reactions under a given constant pressure of the gas self-generated in the reaction would imply to consider the thermodynamic of the process by taking into account the microreversibility principle [26, 30, 34-35].

2. Experimental

  • Commercially available magnesium hydride purchased from Aldrich (product number 683043, with average particle size of 50 μm) was used for performing the study.
  • Typical sample size was ~85 mg, which was placed in alumina pan.
  • The system was connected to a mass flow controller and a pressure controller in order to carry out the experiments under 50 cm3 min-1 hydrogen flow and at constant pressure.
  • Moreover, the recorded melting point of this standard is compared to the known melting point and the difference is calculated for temperature calibration.
  • The α-T plots were obtained by numerical integration of the normalized DSC plots.

3. Theoretical

  • The dehydrogenation of magnesium hydride takes place according to the following reversible reaction: ←→ (1) According to the microreversibility principle, in a reversible reaction the mechanism in one direction is exactly the reverse of the mechanism in the other direction.
  • If the reaction is carried out under high vacuum in such a way that the pressure p is extremely low with regard to the equilibrium pressure, the term p/p* would be close to zero and equation (2a) becomes: 2 3.1.
  • The equation for the combined kinetic analysis is obtained rearranging the equation (2a) in logarithmic form after replacing the f(α) function by the Sestak-Berggren equation: /1 1 ∗ ln 5 or /1 ln 5 , 8    when far from equilibrium (i.e.; p/p* = 0).
  • The set of experimental data, corresponding to different heating schedules, is substituted either into equation (5a) or (5b) and the left-hand side of the equations is plotted versus the inverse of temperature.
  • The Pearson linear correlation coefficient is set as an objective function for optimization, and the values of the parameters n and m that provide the best linear fit to the plot are determined.

4. Results and discussion

  • 1. Kinetics of magnesium hydride dehydrogenation in vacuum.
  • It is noteworthy to point out that it has been theoretically demonstrated in literature that the β-MgH2 phase is capable of accommodating only very small concentrations of hydrogen vacancies that are mainly isolated rather than forming clusters [44].
  • The original experimental curves were reconstructed by simulating a set of curves using the kinetic parameters resulting from the above analysis.
  • Thus, equation 4b, without accounting for (1- p/p*), was employed for the calculations, and the activation energy values obtained are presented in Table 2.
  • For MgH2 dehydrogenation under 20 bar the mean activation energy is even higher if calculated without considering the pressure term (271 kJ mol-1) and a high deviation in the activation energy of 40 kJ mol-1 is obtained between the maximum and minimum values of α.

5. Conclusions

  • Kinetics of MgH2 dehydrogenation has been studied in three different experimental conditions.
  • The reliability of the calculated kinetic parameters has been tested by comparing simulated and experimental curves.
  • A unified theory that explains this behavior is given.
  • The activation energy of the reaction is less influenced by the experimental conditions, and the values obtained agree with the value reported for MgH bond energy, which suggests that the breaking of this bond could be the rate limiting step of the MgH2 thermal dehydrogenation.

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Abstract: Thermochemical energy storage (TCES) is considered as a promising technology to accomplish high energy storage efficiency in concentrating solar power (CSP) plants. Among the various possibilities, the calcium-looping (CaL) process, based on the reversible calcination–carbonation of CaCO3 stands as a main candidate due to the high energy density achievable and the extremely low price, nontoxicity, and wide availability of natural CaO precursors such as limestone. The CaL process is already widely studied for CO2 capture in fossil fuel power plants or to enhance H2 production from methane reforming. Either one of these applications requires particular reaction conditions to which the sorbent performance (reaction kinetics and multicycle conversion) is extremely sensitive. Therefore, specific models based on the conditions of any particular application are needed. To get a grip on the optimum conditions for the carbonation of limestone derived CaO in the CaL-CSP integration, in the present work is pursued a...

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Cites background from "Magnesium hydride for energy storag..."

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References
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TL;DR: In this article, the authors have developed recommendations for reliable evaluation of kinetic parameters (the activation energy, the preexponential factor, and the reaction model) from the data obtained by means of thermal analysis methods such as TGA, differential scanning calorimetry (DSC), and differential thermal analysis (DTA).

4,112 citations

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TL;DR: In this article, a technique was devised for obtaining rate laws and kinetic parameters which describe the thermal degradation of plastics from TGA data, based on the inter-comparison of experiments which were performed at different linear rates of heating.
Abstract: A technique was devised for obtaining rate laws and kinetic parameters which describe the thermal degradation of plastics from TGA data. The method is based on the inter-comparison of experiments which were performed at different linear rates of heating. By this method it is possible to determine the activation energy of certain professes without knowing the form of the kinetic equation. This technique was applied to fiberglass-reinforced CTL 91-LD phenolic resin, where the rate law - (1/we)(dw/dt) = 1018e−55,000/RT [(w - wf)/w0,]5, nr.−1, was found to apply to a major part of the degradation. The equation was successfully tested by several techniques, including a comparison with constant temperature data that were available in the literature. The activation energy was thought to be correct within 10 kcal.

3,002 citations

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TL;DR: This work summarizes commonly employed models and presents their mathematical development as nucleation, geometrical contraction, diffusion, and reaction order.
Abstract: Many solid-state kinetic models have been developed in the past century. Some models were based on mechanistic grounds while others lacked theoretical justification and some were theoretically incorrect. Models currently used in solid-state kinetic studies are classified according to their mechanistic basis as nucleation, geometrical contraction, diffusion, and reaction order. This work summarizes commonly employed models and presents their mathematical development.

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Journal ArticleDOI
TL;DR: The future of a particularly promising class of materials for hydrogen storage, namely the catalytically enhanced complex metal hydrides, is discussed and the predictions are supported by thermodynamics considerations, calculations derived from molecular orbital (MO) theory and backed up by simple chemical insights and intuition.
Abstract: This review focuses on key aspects of the thermal decomposition of multinary or mixed hydride materials, with a particular emphasis on the rational control and chemical tuning of the strategically important thermal decomposition temperature of such hydrides, Tdec. An attempt is also made to predict the thermal stability of as-yet unknown, elusive or even unknown hydrides. The future of a particularly promising class of materials for hydrogen storage, namely the catalytically enhanced complex metal hydrides, is discussed. The predictions are supported by thermodynamics considerations, calculations derived from molecular orbital (MO) theory and backed up by simple chemical insights and intuition.

1,404 citations

Journal ArticleDOI
TL;DR: The hydrogen storage properties of MgH 2 are significantly enhanced by a proper engineering of the microstructure and surface as discussed by the authors, which gives remarkable improvement of absorption/desorption kinetics.

1,081 citations

Frequently Asked Questions (1)
Q1. What have the authors contributed in "Magnesium hydride for energy storage applications: the kinetics of dehydrogenation under different working conditions" ?

Thus, the reaction follows a first order kinetics, equivalent to an Avarmi-Erofeev kinetic model with an Avrami coefficient equal to 1, when carried out under high vacuum, while a mechanism of tridimensional growth of nuclei previously formed ( A3 ) is followed under hydrogen pressure. It has been shown that the activation energy is closed to the Mg-H bond breaking energy independently of the hydrogen pressure surrounding the sample, which suggests that the breaking of this bond would be the rate limiting step of the process.