A potential hydrogen isotope storage material Zr2Fe: deep exploration on phase transition behaviors and disproportionation mechanism
Abstract
Tritium, a radioactive isotope of hydrogen, is exceptionally rare and valuable. The safe storage, controlled release and efficient capture of tritium are subject to focused research in the International Thermonuclear Experimental Reactor. However, the application of an efficient tritium-getter material remains a critical challenge. Zr2Fe alloys exhibit a strong ability to absorb low-concentration hydrogen isotopes, but their practicability suffers from disproportionation reaction. Yet, the essential de-/hydrogenation performances and disproportionation mechanism of Zr2Fe are inconclusive. Here, we designed a comprehensive series of measurements that demonstrate the ultra-low hydrogenation equilibrium pressure (2.68 × 10-8 Pa at 25 °C) and unique
Keywords
INTRODUCTION
In recent decades, the energy demands for social development have steadily risen, while excessive provision and utilization of fossil energy have caused the energy crisis and presented adverse effects on environmental harmony. Nuclear energy generated by a controllable nuclear fusion reaction (deuterium and tritium plasma) in the International Thermonuclear Experimental Reactor (ITER) is recognized as one of the most desirable sustainable energy systems owing to its environment-friendliness, low cost, safety, substantial energy release and fuel abundance[1,2]. The retention of tritium is an essential issue during recovery and storage due to its radioactivity and rarity. Meanwhile, a crucial security concern is to ensure the absence of tritium leakage. Consequently, it is imperative to collect tritium in the exhaust gas and equipment space. Tritium-getter materials should exhibit excellent hydrogen absorption kinetics and ultra-low equilibrium hydrogenation pressure to ensure high absorption efficiency. Thus, hydrogen storage alloys (HSAs) are attracting widespread interest in the nuclear industry, owing to their ability to capture hydrogen isotopes and generate stable metal hydrides.
At present, metallic Pd, depleted U and ZrCo-based alloys are available in hydrogen isotope separation/purification and storage/delivery systems. Pd is the first-discovered HSA and exhibits a significant isotope effect. The hydrogenated product of Pd is PdH0.6 with a theoretical capacity of 0.565 wt%, and the hydrogenation equilibrium pressure under room temperature of Pd is about 2,700 Pa[3]. U-based alloys have rapid hydrogenation rates and relatively high rechargeable hydrogen storage capacities (~ 0.9 wt%) and reach low hydrogenation equilibrium pressures (10-3 ~ 10-4 Pa at room temperature), but radioactivity is a challenge for U[4]. Compared to the Pd and U, ZrCo-based alloys are non-radioactive and low cost, having a high theoretical hydrogen storage capacity of 2 wt%, and a relatively low equilibrium pressure (~ 10-3 Pa at room temperature)[5]. Therefore, Zr-based alloys, especially those with high hydrogen-affinity Zr content, are of great interest in Tokamak exhaust processing (TEP) systems[6-9]. The Zr-rich alloys were once regarded as potential tritium absorption materials for capturing low-concentration tritium due to their high hydrogen storage capacity, rapid hydriding kinetics and much lower hydrogenation equilibrium pressure. Furthermore, their comprehensive evaluation requires consideration of indicators such as disproportionation resistance[10].
Hydrogen isotopes have similar physical and chemical properties, so hydrogen is usually used instead of tritium in the study of hydrogen isotope storage metals[11]. Early, the hydrogen absorption and disproportionation behaviors of Zr2M (M = Ni, Co, Fe) alloys were reported and discussed in a summarized manner[12]. The room-temperature hydrogenation equilibrium pressure of Zr2Ni alloys is reported to be approximately 500 Pa, which is too high for hydrogen isotope storage applications. Meanwhile, Zr2Ni can be rapidly disproportionated into ZrNiH3, ZrH2 and a Zr-deficient compound (ZrNi) with the interaction of hydrogen at 500 °C; then, ZrNi reacts with H2 to form disproportionation products ZrH2 and Zr7Ni10[12,13]. Zr2Co alloys have an ultra-low hydrogenation equilibrium pressure of 3.22 × 10-6 Pa at 25 °C, significantly lower than that of ZrCo alloys (10-3 Pa), and exhibit great hydriding kinetics at a low hydrogen pressure of 5,000 Pa due to their high content of hydrogen-affinity Zr[14]. However, Zr2Co exhibits similar disproportionation behaviors to Zr2Ni. During the elevated temperature dehydrogenation, the Zr2CoH5 hydride first decomposes into ZrCoH3 and ZrH2, making it highly susceptible to disproportionation. Although the disproportionation products can be reconstructed back to Zr2Co at 800 °C, it is easy to induce tritium permeation and thermal radiation to the external environment during tritium recovery applications at such high reconstruction temperatures. Therefore, it is crucial to improve the anti-disproportionation properties of ultra-low hydrogen equilibrium pressure alloys at workable temperatures[15].
Regarding Zr2Fe alloys, it was reported that Zr2Fe beds can absorb the hydrogen isotopes to the concentration below the detection limit of gas chromatography (1 ppm) in a relatively short time, demonstrating excellent hydrogen absorption performance[16]. Importantly, its cyclic stability, i.e., the ability to resist disproportionation, is still a key consideration. Prigent et al.[17] investigated the cyclic performance of Zr2Fe alloys under a hydrogen pressure of 1 bar, and the results demonstrated a sharp decay of hydrogen absorption capacity after cycling. Its initial hydrogenation capacity is about 1.88 wt%, following dehydrogenation at 350 °C for 3 h; the hydrogenation capacity decreases to only 0.84 wt% in the third cycle. Disproportionation products do not contribute to hydrogen storage capacity, directly indicating the disproportionation degree. Hara et al.[12] suggested that Zr2Fe has peculiar behaviors of disproportionation that differ from Zr2Ni and Zr2Co, and exhibits relatively poorer stability to hydrogen-induced disproportionation. Song et al.[18] pointed out that Zr2Fe would still be disproportionated even if hydrogenated at room temperature, and that the degree of disproportionation significantly intensified with initial hydrogen pressure. Nevertheless, Janot et al.[19] reported that only Zr2FeH5 and Zr3FeH6.7 phases were formed after hydrogen absorption in the Zr2Fe and Zr3Fe alloys. The phase transitions of Zr2FeD5 during the temperature-rise process were studied in situ by neutron diffraction; it was found that the disproportionation phase of ZrD2 would not exist below 330 °C[20]. It follows that the disproportionation mechanism in the Zr2Fe-H system remains controversial, and de-/hydrogenation performance has not been thoroughly investigated with comprehensive consideration of in-process control parameters. Simultaneously, the lack of consolidated understanding of the kinetic and thermodynamic properties, as well as the specific de-/hydrogenation performance indexes of Zr2Fe, also hinders the exploration of disproportionation behaviors.
In this work, we have comprehensively studied the de-/hydrogenation properties in Zr2Fe-H systems by precisely modulating hydrogen pressure, temperature and reactant loadings, and then investigated the variations of the corresponding crystal structures and phases. Subsequently, we progressively elicited and identified the practical triggering factors for the disproportionation reaction. The correlation between general de-/hydrogenation and disproportionation reactions was further examined in terms of kinetics and thermodynamics. Meanwhile, the reaction pathways of disproportionation reaction were defined. Finally, in conjunction with density functional theory (DFT) calculations in terms of energy variation and bonding strength, the mechanisms of general de-/hydrogenation and disproportionation in the Zr2Fe-H system were deeply probed, and their competitive relationship in kinetics was further elucidated.
EXPERIMENTAL
Sample preparation
Zr2Fe ingot was synthesized by induction levitation melting with high-purity metals in accordance with the stoichiometric ratio. The equipment used is a SPG-60AB high-frequency induction heater produced by Shenzhen Shuangping Power Supply Technologies Co. Ltd. The melting process of high-purity zirconium and iron (total weight of around 25 g) was performed in a water-cooled copper crucible under the protection of a 1.4 bar argon atmosphere (99.999%). The protection gas in the melting chamber was ensured by flushing with argon at room temperature. The ingot was turned over for re-melting three times to ensure high homogeneity. Stoichiometric amounts of high-purity zirconium (Zr, 99.9%) and iron (Fe, 99.9%) were supplied by the General Research Institute for Non-ferrous Metals.
Microstructure characterization
The morphology of the alloy was observed using a Hitachi SU-70 field-emission scanning electron microscope (FESEM). The elemental mapping was detected using an energy dispersive X-ray spectrometer (EDX) mounted on a scanning electron microscope (SEM). The phase structure was characterized by an X-ray diffractometer (XRD, Rigaku Ultima IV) with Cu-Kα radiation (λ = 0.154056 nm). The differential scanning calorimetry (DSC, Netzsch STA449F3) was detected in the Ar atmosphere.
Hydrogen storage performance measurements
A hydrogen storage performance test device (Sievert's type volumetric equipment) is made up of an electric furnace, a 10 ml stainless-steel reactor, two reservoirs with volumes of 100 ml and 750 ml, and three pressure sensors (test range: 0.01 - 160 bar, 0.001 - 10 bar and 0.1 - 1,024 Pa, respectively). High-purity hydrogen (99.999%) is adopted. In the initial activation process, crushed Zr2Fe alloy powders were placed into a reactor and annealed at high temperatures under evacuation for a specific time, to get rid of the surface-adsorbed impurity gas. The activated samples were then used for subsequent experiments. The hydriding kinetics of activated samples were tested under the same initial hydrogen pressures (1 bar) at room temperature with different sample loadings of 0.25, 0.5 and 1.5 g. The Pressure-Composition-Temperature (PCT) measurements for de-/hydrogenation at different temperatures (325, 350, 375, 450, and 500 °C) were performed by progressively adjusting the hydrogen pressure in the reactor, with temperature fluctuations of less than 5 °C. The temperature-programmed dehydrogenation (TPD) experiments were performed with an initial hydrogen pressure of 10 Pa and a heating rate of 3 °C/min and 5 °C/min. Measurements involving disproportionation were conducted by designing parameters such as hydrogen pressure, temperature, reaction time, and the amount of hydrogen absorption. These parameters were systematically controlled to regulate the disproportionation reaction during de-/hydrogenation processes.
Apparent activation energy calculations
The hydrogenation fraction of a sample can be written as follows:
where α is the reaction fraction, and H0, Ht and H1 refer to the hydrogen capacity of a sample at begin, time t and final, respectively.
The rate of hydrogenation can be expressed by the following basic rate equation:
where f(α) is a mathematical model that simulates the reaction, and the parameter k(T) is the temperature-dependent reaction rate constant.
By integrating the above equation according to the method proposed by Sharp[21] and Jone[22], the reaction progress versus reaction time is obtained as follows:
Where g(α) represents the expression of a specific kinetic model. Different kinetic models each have a corresponding set of theoretical values (tα/t0.5)theo. By fitting the experimental values with the theoretical values, the appropriate kinetic model can be determined[23,24]. The relationship between g(α) and t allows for the calculation of k(T). Finally, the apparent activation energy can be derived from the Arrhenius equation:
where k(T), A, R and T represent the rate coefficient of reaction, the pre-exponential factor, the molar gas constant and the tested temperature, respectively.
Theoretical calculations
DFT calculations were applied on projected augmented wave (PAW)-based Vienna ab initio simulation package (VASP) method, which is used for the description of exchange-correlation between the electrons combined with the generalized-gradient approximation (GGA) in the parameterization of Perdew-Burke-Ernzerhof (PBE) pseudopotential to the electrons[25,26]. The selected models for Zr2Fe (mp-1159), ZrH2 (mp-24286), and Zr2FeH5 (mp-643907) from the Materials Project and Zr2FeH2 from the Inorganic Crystal Structure Database were subjected to geometrical optimization. The plane wave cutoff energy was set to 380 eV; the self-consistent convergence criteria of electron and ion are respectively set to be 10-6 eV and 0.02 eV/Å, and 5 × 5 × 6 Gamma centered Monkhorst-Pack grid k-points are employed for corresponding structure optimizations. The visualization and annotation of the models were achieved by Visualization for Electronic and Structure Analysis (VESTA)[27], and the projected density of states (PDOS) was further determined and then projected using P4VASP. The chemical bonding analysis of Metal-H interaction was carried out using the crystal orbital Hamilton population (COHP), which was calculated by the Local Orbital Basis Suite Toward Electronic-Structure Reconstruction code (LOBSTER)[28]. The integral of the COHP (ICOHP) describes the bond strength by integrating energy below Fermi energy[29].
RESULTS AND DISCUSSION
The phase composition and crystal structure of the Zr2Fe sample were confirmed by XRD, as shown in Figure 1A, where most of the diffraction peaks match well with tetragonal Zr2Fe (JCPDS no. 04-003-5495, space group: I4/mcm). The diffraction peaks at 35.3°, 42.9° and 44.9° respectively correspond to the (211), (202) and (310) planes of tetragonal Zr2Fe. Besides, three obvious diffraction peaks located at 38.4°, 41.9° and 65.0° can be seen, corresponding well to the (511), (440) and (822) planes of cubic Zr2Fe (JCPDS no. 04-002-9744, space group: Fd3m). The crystal structure phase composition was analyzed by Rietveld refinement, and the weighted ratio of tetragonal Zr2Fe and cubic Zr2Fe is obtained as 86.5:13.5. Figure 1B presents a SEM image with energy dispersive X-ray spectroscopy (EDX) elemental mapping of Zr2Fe powder. The distribution regions of the Zr and Fe elements are basically consistent with the area of Zr2Fe, demonstrating the compositional homogeneity of Zr2Fe.
Figure 1. XRD pattern (A) and SEM image correlating the EDS mapping micrographs (B) of as-cast Zr2Fe alloy; (C) Pressure vs. temperature during thermal vacuum degassing activation experiment; (D) XRD pattern of activated Zr2Fe alloy; (E) Hydriding kinetics of Zr2Fe after different activation conditions; (F) XRD pattern of Zr2FeH5 hydride. XRD: X-ray diffractometer; SEM: Scanning electron microscope; EDS: X-ray spectrometer; EDX: Energy dispersive X-ray spectroscopy.
Hydrogen storage performance of Zr2Fe is greatly correlated with the condition of activation. Evacuation at high temperatures tends to dissociate the impurity gas adsorbed on the surface of the Zr2Fe alloy. A method of thermal vacuum degassing experiment was conducted to investigate the relationship between temperature and activation. The result [Figure 1C] clearly exhibits a direct relationship between temperature and the intensity of impurity gas desorption, demonstrating that the impurity desorption is concentrated at 200 ~ 300 °C and lasts until 430 °C, thereby guiding the activation procedure of Zr2Fe. Figure 1D presents the XRD pattern of the sample after activation; it is found that the crystal phase composition and structure of as-cast Zr2Fe are maintained, indicating that only trace impurities covering the surface are removed. Subsequently, the hydriding kinetics with a reactant loading of 0.25 g were tested to assess the hydrogenation performance at 1 bar and the effect of activation condition [Figure 1E]. Under activation conditions of 400 °C/2 h and 400 °C/1 h (vacuuming), the former exhibits faster kinetics, with a higher hydrogen storage capacity of 1.87 wt%, indicating that impurities desorption rate is relatively low at 400 °C. Furthermore, after vacuuming at 450 °C for 0.5 h, rapid kinetics can be achieved, with a hydrogen storage capacity reaching 1.89 wt%. There is no significant further improvement in hydrogen absorption performance at longer activation durations at 450 °C, which is consistent with the vacuum degassing experiment. The XRD pattern of the hydrogenation product of the Zr2Fe alloy is shown in Figure 1F; it is found that both tetragonal Zr2Fe and cubic Zr2Fe are hydrogenated to tetragonal Zr2FeH5, forming a single-phase structure.
The hydrogen storage properties and thermodynamic parameters of Zr2Fe alloys were further investigated through de-/hydrogenation PCT tests (10-5 ~ 10 bar) and the Van't Hoff calculation. It can be observed that Zr2Fe exhibits sloped de-/hydrogenation PCT curves at 325, 350 and 375 °C [Figure 2A]. It is worth mentioning that the hydrogen pressure corresponding to the midpoint of the saturation capacity (~ 1 wt%) is adopted as equilibrium hydrogen pressure (Peq) due to the non-significant plateau properties of the PCT curves. It can be obtained that the hydrogenation equilibrium pressures are 305, 777 and 1,800 Pa at 325, 350 and 375 °C, respectively, and the dehydrogenation equilibrium pressures are 213, 540 and 1,295 Pa. Due to the difference of lattice strain during the de-/hydrogenation, there is little hysteresis between absorption and desorption processes[30]. For dehydrogenation at 375 ℃, the hydrogen background pressure of 200 Pa can only make the dehydrogenation capacity reach 0.99 wt%, much lower than the corresponding saturation capacity, indicating the incomplete dehydrogenation due to the excessively low equilibrium pressure of Zr2Fe. Deeper dehydrogenation of Zr2Fe hydride requires a higher temperature and continuous ultra-high vacuum environment.
Figure 2. Hydrogenation and dehydrogenation PCT curves of Zr2Fe samples at different temperatures (A) and their corresponding Van't Hoff plots (B); XRD patterns of hydrogenated (C) and dehydrogenated (D) Zr2Fe corresponding to different cutoff capacities. PCT: Pressure-ccomposition-temperature; XRD: X-ray diffractometer.
The Van't Hoff calculation is shown in Figure 2B. The de-/hydrogenation thermodynamic parameters have been calculated in terms of the Peq at different temperatures (T) using[31]:
Where ΔH and ΔS are enthalpy and entropy change of reaction, while R and T are the molar gas constant and the experimental temperature, respectively. The specific thermal parameters including ΔH and ΔS, listed in Figure 2B, are obtained from the fitting curves of Van't Hoff plots. The calculated hydrogenation enthalpy of the Zr2Fe-H system is -114.46 kJ/mol H2, slightly lower than that of the Zr2Co-H system[14], laterally indicating similar hydrogenation behavior between these two systems. According to Van't Hoff equation, significantly low hydrogenation Peq (25 °C) of Zr2Fe was acquired as 2.68 × 10-8 Pa, which is several orders of magnitude lower than the equilibrium pressure of Zr2Co (3.22 × 10-6 Pa) and ZrCo (10-3 Pa). This makes Zr2Fe ideal for capturing low concentrations of hydrogen isotopes, improving the safety and effectiveness of the TEP system.
To further study the phase transition behaviors during de-/hydrogenation in Zr2Fe-H system, the Zr2Fe hydrides with various hydrogen concentrations in the process of hydrogen absorption and thermal desorption were intercepted for XRD analysis [Figure 2C and D]. In the initial hydrogenation (0 ~ 0.3 wt%), the tetragonal Zr2Fe phase transforms into the Zr2FeHx phase. Observably, the diffraction peaks at 35.3° and 44.9° are shifted to a smaller angle of about 1°, which represents a sharp expansion in the corresponding (211) and (310) interplanar spacing. Some diffraction peaks at 32°, 37.9° and 43° corresponding to the (002), (112) and (202) crystal planes, respectively, are significantly shifted to larger angles. The lattice calculations
The lattice parameters of Zr2Fe at different stages of hydrogenation
Hydrogenation stages | Lattice parameters (Å) | Volume (Å3) | Average Expansion rate per 0.1 wt% | ||
a | b | c | |||
Zr2Fe | 6.369 | 6.369 | 5.591 | 226.771 | 1.75% (0 ~ 0.3 wt%) 1.31% (0.3 ~ 0.7 wt%) 0.77% (0.7 ~ 1.0 wt%) 0.58% (1.0 ~ 1.89 wt%) |
0.3 wt% | 6.643 | 6.643 | 5.408 | 238.670 | |
0.7 wt% | 6.794 | 6.794 | 5.442 | 251.205 | |
1.0 wt% | 6.846 | 6.846 | 5.484 | 257.034 | |
1.89 wt% | 6.932 | 6.932 | 5.624 | 270.268 |
For Zr-based HSAs, the occurrence of disproportionation reactions is inevitable for removing more hydrogen at higher temperatures. Thus, the factors influencing disproportionation of Zr2Fe need to be critically considered. Initially, rapid hydrogenation experiments were conducted, as shown in Figure 3A. Given that the hydrogenation of Zr2Fe is an exothermic reaction as mentioned above, the exothermic heat can result in instantaneous temperature rise during the hydrogen absorption of Zr2Fe to saturation, and the higher quantity of the reactant loading in a fixed-volume reactor can generate more exothermic heat in a comparable time. The corresponding XRD analyses of the products [Figure 3B] need to be discussed in conjunction. It can be found that the sample with loading 0.25 g exhibits a maximum surge temperature of 78 °C and achieves the rated hydrogen storage capacity of Zr2Fe alloys (1.89 wt%) during hydrogenation. The XRD results indicate that the product is predominantly composed of Zr2FeH5, suggesting that the relatively low-temperature fluctuation (78 °C) is insufficient to induce a disproportionation reaction. At the sample loading of 1.5 g, the maximum surge temperature reaches 416 °C and the hydrogen storage capacity drops to only 1.67 wt%. At this point, it is clear that Zr2FeH5 is considered the principal phase, where some impurity phases such as ZrH2 and ZrFe2 located at 32.3° and 42.3°, respectively, are identified as disproportionation phases. Evidently, as the sample loading further increases to 2 g, the disproportionation becomes more severe. The intensification of temperature rise during reaction greatly damages hydrogen storage performance, and there is a strong correlation between them [Supplementary Figure 2]. It can be inferred that the increased thermal motion of the atoms at elevated temperatures leads to more unstable positions in the crystals, which may promote the generation of disproportionation phases.
Figure 3. Hydriding kinetics (initial pressure: 1 bar) of Zr2Fe with different sample loadings (A) and XRD patterns of the corresponding products (B); The schematic diagram of hydrogenation process with different pressures and temperatures (C) and XRD patterns of hydrogenation products of Zr2Fe under corresponding hydrogenation conditions (D). XRD: X-ray diffractometer.
In order to further investigate the triggering mechanism of disproportionation, a series of rapid hydrogenation experiments with different configurations of pressure and temperature are conducted, as depicted in Figure 3C, and the corresponding XRD analyses of products are shown in Figure 3D. It reveals that certain disproportionation products will be produced during the process of over-rapid hydrogenation to saturation of Zr2Fe (The maximum surge temperature is 37 °C). This result suggests that excessively rapid insertion of H atoms can induce disproportionation, and the thermodynamic condition of disproportionation is easy to satisfy. Meanwhile, PCT tests for hydriding disproportionation were conducted, and the ΔH and ΔS of the reaction were obtained, with values of -174.79 kJ/mol H2 and
Further investigation found that disproportionation can be induced by high temperatures at low pressures as well, because the high temperature may enhance the atomic thermal motion to deliver additional energy for disproportionation to overcome the kinetic barrier. Unfortunately, the high-temperature environment is the primary cause of disproportionation in actual applications, and thus should be given particular consideration. However, at high temperatures, the measured values of hydrogen storage equilibrium pressures and capacities are implicated by the interference of hydriding disproportionation behavior, making it impossible to accurately measure the general hydrogenation PCT curves at high temperatures. According to the special hydrogenation phase transition behaviors of Zr2Fe, we calculated the
Figure 4. (A) Simulated/measured hydrogenation PCT curves of Zr2Fe-H system at 450 ~ 600 °C Controlled hydrogen absorption curves of Zr2Fe at 350 ~ 500 °C (B) and XRD of the corresponding hydrogenation products (C). PCT: Pressure-ccomposition-temperature; XRD: X-ray diffractometer.
To confirm the aforementioned conjecture, the apparent activation energy (Ea) was introduced to provide a more detailed explanation. A practical approach for finding kinetic models was adopted for the hydriding disproportionation reaction, as illustrated in Figure 5A-D. Figure 5A exhibits the relative kinetics performance for the hydriding disproportionation reaction across the temperature range of 550 to 625 °C, where the reaction kinetics gradually slow down with the increasing extent of reaction. In contrast, Figure 5B shows the plots based on the experimental value (t/t0.5)expvs. the modeled theoretical value
Figure 5. (A) The normalized kinetics curves of hydriding disproportionation reaction; (B) Comparison of different kinetic models; (C) Fitting results of kinetics curves with R3 model; (D) Activation energy calculation using Arrhenius plot.
Furthermore, the reaction pathways of the hydriding disproportionation should be investigated clearly. Firstly, we selected the temperature of 500 °C at which disproportionation is pronounced in the thermostatic hydrogenation test [Figure 6A]. As presented in Figure 4A, it is evident that the equilibrium pressure remains low in instances of low hydrogen capacity fractions. Thus, it can be noticed that even at the low hydrogen pressure of 0.03 bar and 500 °C, the initial process still exhibits a relatively rapid kinetics hydrogen absorption. The XRD pattern of the intermediate state [Figure 6B] indicates that Zr2Fe has been fully hydrogenated to Zr2FeHx (1 < x < 2) at Point A. Subsequently, the hydrogen-absorbing reaction with slower kinetics can be remarkably distinguished, as its final product is predominantly the disproportionation phase according to the XRD pattern of Point B [Figure 6B]. This identifies Point A as the transition point between general hydrogenation and disproportionation, and the Zr2Fe will be preferentially hydrogenated above the equilibrium pressure of hydrogenation. Consequently, one of the disproportionation paths is confirmed as:
Figure 6. Kinetic tests for Zr2Fe samples under 500 °C/0.03 bar and 600 °C/0.01 bar H2 (A, C) and the corresponding XRD patterns for the marked point (B, D). XRD: X-ray diffractometer.
The procedure of Point A to C corresponds to thermal preservation for 10 h with isolation of almost all hydrogen. The XRD pattern of the product suggests that only a part of Zr2FeHx transforms to ZrH2 and ZrFe2, consuming the residual hydrogen inside the container. While the diffraction peaks of hydride are still obvious, with a right shift of 0.4° in comparison to Point A, as Zr2FeHx (0 < x < 1), suggesting that partial H atoms have been detached from hydride due to the decrease in hydrogen pressure. This result demonstrates the occurrence of the following reactions during the transition from Point A to C:
Furthermore, both reactions (7) and (8) are also expected to occur in a sufficient hydrogen environment such as Point A to B; however, in such a scenario, reaction (8) will be significantly diminished and reaction (7) becomes the competitively dominant reaction.
Whether Zr2Fe can be directly disproportionated was further discussed. The tested temperature was increased to 600 °C to elevate the hydrogenation equilibrium pressure. Simultaneously, a lower hydrogen pressure (0.01 bar) was given to allow only trace amounts of hydrogen to be initially dissociated [Figure 6C]. The XRD pattern in Figure 6D displays the presence of the principal Zr2Fe phase and less amount of ZrH2 phase in the intermediate state (5 min). Notably, disproportionation reaction can still occur, which definitively suggests that Zr2Fe can undergo direct disproportionation as follows:
In the end, due to the low pressure of 200 Pa, the disproportionation reaction lacks the necessary driving force to fully form into the ZrH2 and ZrFe2 phases, leaving residual small amounts of cubic Zr2Fe. The crystallization of the disproportionation products was promoted at higher temperatures, indicating a stronger interaction between Zr and H[36,37].
The aforementioned study on dehydrogenation phase transition has indicated that disproportionation phases will be generated during the high-temperature dehydrogenation of Zr2Fe hydrides. Therefore, we performed TPD experiments under hydrogen pressures kept within 1,000 Pa to investigate the dehydrogenation behaviors over a wide temperature range, as depicted in Figure 7A and B. It can be seen that the dehydrogenation evenly occurs below 500 °C, with a small dehydrogenation peak observed at about 200 °C. The slope of the curve begins to decline obviously around 500 °C and then continues to decrease until 600 °C, reflecting the occurrence of hydrogen absorption and the gradual obscuration of dehydrogenation. Later, the slope gradually rises, followed by a vigorous hydrogen release after 670 °C, attributed to the decomposition of ZrH2[14]. This process corresponds to the exothermic and endothermic reactions observed in the DSC curve of the Zr2FeH5 [Supplementary Figure 4]. One thing to mention: according to reaction (7), the hydriding disproportionation reaction occurs when the x of Zr2FeHx is less than 3, and the disproportionation reaction from Zr2FeHx (3 < x < 5) is regarded as dehydriding disproportionation reaction. When Zr2FeH5 is subjected to certain high pressures and temperatures, dehydriding disproportionation occurs instead of general dehydrogenation [Supplementary Figure 5], apparently indicating that the equilibrium pressure of dehydriding disproportionation is much higher than that of general dehydrogenation. Thus, the dehydriding disproportionation reaction is definitely accompanied by a dehydrogenation process of Zr2FeHx (3 < x < 5) at high temperatures above 375 °C. Furthermore, the above-mentioned investigation found that the dehydrogenated product of Zr2FeHx with x less than 3 can be obtained when dehydrogenation is below the critical temperature of disproportionation (375 °C). Therefore, in our experiments and practical applications, the dehydriding disproportionation reaction can almost be avoided.
Figure 7. TPD curves of Zr2FeH5 at the temperature range of 25 ~ 750 °C (A) and 25 ~ 500 °C (B); and XRD patterns for the marked points (C). TPD: Temperature-programmed dehydrogenation; XRD: X-ray diffractometer.
Subsequently, we set 500 °C as the peak temperature, where the slope observably decreases in Figure 7A, and implemented a heating-preservation dehydrogenation program, as depicted in Figure 7B. Here, the XRD characterization of turning Point A and Point B was carried out respectively, as displayed in Figure 7C. During the heating dehydrogenation, Zr2FeHx was dehydrogenated to the x value of about 1.2 as heating to 500 °C (Point A), with almost no disproportionation occurring. It is evident that the sample switches to lower hydrogen release after temperature stabilization, while the hydriding disproportionation reaction (7) continues until Point B. The explanation can also be derived that the side reaction of hydriding disproportionation intensifies with increasing temperature at a range of 375 to 600 °C when the sample interacts with H progressively. Furthermore, the gradual decrease of the curve slope in Figure 7A demonstrates that dehydrogenation and hydriding disproportionation can occur simultaneously. This brings out the importance of inhibiting the disproportionation reaction.
Figure 8A displays the optimized lattice structures of Zr2Fe, Zr2FeH2, Zr2FeH5, ZrFe2 and ZrH2, and the corresponding schematic illustration for de-/hydrogenation and disproportionation. The de-/hydrogenation can be modulated depending on the temperature and hydrogen pressure, while above 375 °C, the disproportionation reaction will aggressively compete for the reactants Zr2Fe/Zr2FeHx. Kinetic activation energy and thermodynamic principles have been utilized to explain the apparent mechanism of de-/hydrogenation and disproportionation. Furthermore, DFT calculations were introduced to further investigate intrinsic causes of the behaviors of Zr2Fe alloy interacting with hydrogen. Herein, the hydrogen removal energy Er(H) is defined as follows:
Figure 8. (A) The schematic illustration of the relationship between hydrogenation, dehydrogenation and hydrogen-induced disproportionation in Zr2Fe-H system with lattice structures of Zr2Fe, Zr2FeH2, Zr2FeH5, ZrFe2 and ZrH2 PDOS and interstices diagram of Zr2FeH5 (B) and ZrH2 (C) A typical example of Zr3Fe interstices (D) and calculated COHP between Zr, Fe and H in Zr3Fe (E-F). PDOS: Projected density of states; COHP: Crystal orbital hamilton population.
where Er(H) represents the required energy for removing one particular H atom within the lattice, and EH is the energy of single H atom. E1 and E0 denote the energy of optimized structure with and without removal of single H atom, respectively.
According to the chemical environment of H atoms in the specific tetrahedral interstitial sites, different types of hydrogen interstice were segmented and rendered for clearer visualization. The interstices of Zr2FeH5 can be divided into two types: Zr3Fe and Zr4, with a quantity ratio of 4:1 in one unit cell. The PDOS
Based on this foundation, the weighted average Er(H) of the above three hydrides was calculated, respectively. For Zr2FeH2, there is one type of tetrahedral interstice, Zr3Fe. Therefore, it can be inferred that hydrogen preferentially occupies the Zr3Fe interstice with relatively high hydrogen binding energy in the early stage of hydrogenation. As the hydrogenation proceeds, the Zr4 interstices with relatively low hydrogen binding energy are filled posteriorly. This coherently corresponds to the lattice variation during the Zr2Fe hydrogenation, where larger energy variations respond to larger H-induced lattice distortions, implying that the hydrogen insertion and atomic migration overcome more resistance in the prior hydrogenation[39-42]. Furthermore, with the average Er(H) of Zr2FeH5 (0.5599 eV) being lower than that of
During hydriding disproportionation at high temperatures, the energy barrier of disproportionation reaction is activated, and Zr2FeHx is progressively converted to ZrH2 and ZrFe2, which implies that the disproportionation process induced by high temperatures is accompanied by the breaking of Metal-H bonds in the Zr2FeHx structure. Thus, we measure the metal and hydrogen interactions and qualify the bonding strength in Zr3Fe [Figure 8D] based on the COHP method, as shown in Figure 8E and F.
The ICOHP values at the Fermi level signify the energy contribution of bonding electrons shared between two atoms, and accurately reflect the strength of the bond. By definition, a more negative value of ICOHP suggests stronger bonding[29]. The absolute values of ICOHP crossing the Fermi level for Zr1-H, Zr2-H,
CONCLUSIONS
In summary, the de-/hydrogenation behaviors of the Zr2Fe-H system and their corresponding kinetic and thermodynamic characteristics have been comprehensively investigated. The ultra-low hydrogenation equilibrium pressure of Zr2Fe at 25 °C is determined as 2.68 × 10-8 Pa, and the thermodynamic parameters of enthalpy change ΔH and entropy change ΔS are -114.46 kJ/mol H2 and -143.23 J/K·mol H2 in hydrogenation reaction, while the ΔH and ΔS of the dehydrogenation are calculated as 116.34 kJ/mol H2 and 143.34 J/K·mol H2, respectively. Herein, key reference data of the relationship between the equilibrium pressure and various high temperatures (450 ~ 600 °C) were obtained according to the thermodynamic relationships. These data are utilized to profile the hydrogenation properties of Zr2Fe at high temperatures and distinguish between hydrogenation and hydriding disproportionation. The analysis suggests that the thermodynamic conditions for the hydriding disproportionation reaction are readily met; however, the reaction is subject to kinetic constraints. Further studies are needed to identify the triggering conditions and pathways (reactions 7&9) for disproportionation, and examine the interactions between disproportionation and de-/hydrogenation under various conditions. Sufficient energy, lattice variation, and atomic migration can contribute to overcoming the energy barrier for the disproportionation reaction (87.88 kJ/mol), inducing the hydriding disproportionation. Meanwhile, DFT calculations on crystal structure, hydrogen removal energy, and Metal-H bonding strength further demonstrate the unique phase transition mechanism of
DECLARATIONS
Authors’ contributions
Conceived the idea and designed the experiments: Yang, Z.; Chen, L.
Completed theoretical calculations and performed data interpretation: Jia, Y.; Yang, Z.
Supported equipment option and experimental data analysis: Yang, Z.; Liu, Y.
Provided administrative, technical, and material support: Feng, X.; Shi, Y.; Chen, C.; Luo, W.; Ying, T.; Xiao, X.; Chen, L.
Drafted the manuscript with revisions: Yang, Z.; Xiao, X.; Feng, X.; Chen, L.
Availability of data and materials
Some results supporting the study are presented in the Supplementary Materials. Other raw data that support the findings of this study are available from the corresponding author upon reasonable request.
Financial support and sponsorship
This work was supported by the National Key Research and Development Program of China (2022YFE03170002), the National Natural Science Foundation of China (52071286 and U2030208), and the Scientific Research Fund of Zhejiang University (XY2024014).
Conflicts of interest
All authors declared that there are no conflicts of interest.
Ethical approval and consent to participate
Not applicable.
Consent for publication
Not applicable.
Copyright
© The Author(s) 2025.
Supplementary Materials
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How to Cite
Yang, Z.; Jia, Y.; Liu, Y.; Xiao, X.; Ying, T.; Feng, X.; Shi, Y.; Chen, C.; Luo, W.; Chen, L. A potential hydrogen isotope storage material Zr2Fe: deep exploration on phase transition behaviors and disproportionation mechanism. Energy Mater. 2025, 5, 500011. http://dx.doi.org/10.20517/energymater.2024.83
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