Mohamed Sherif El-Eskandarany*
Nanotechnology and Advanced Materials Program, Energy and Building Research Center, Kuwait Institute for Scientific Research, Safat 13109, Kuwait. E-mail: msherif@kisr.edu.kw
First published on 9th January 2019
Because of its high thermal stability and poor hydrogenation/dehydrogenation kinetics, magnesium hydride (MgH2) requires mechanical treatment and/or doping with catalytic agents(s) to understand the decomposition temperature and accelerate the gas uptake/release kinetics. Whereas all catalytic species used for this purpose are crystalline materials, in this paper use of titanium nickel (Ti2Ni) metallic glassy (MG) nanopowders for enhancing the hydrogenation/dehydrogenation kinetics behavior of MgH2 powders is reported. In the present research, MG-Ti2Ni ribbons, prepared using a melt spinning technique were snipped into small pieces and then cryo-milled under a flow of liquid nitrogen to obtain submicron-powders (500 nm). The as-prepared MgH2 powders were doped with 10 wt% of the glassy powder and then cryo-milled for 25 h. The structural and morphological analysis indicated that the cryo-milling process succeeded in maintaining the short-range order structure of MG-Ti2Ni, and in reducing the MgH2 grain size to the nanolevel. The results showed that the as-prepared nanocomposite powders obtained after 25 h of cryo-milling decomposed at 283 °C, with an apparent activation energy of 87.3 kJ mol−1. The MgH2/10 wt% MG-Ti2Ni nanocomposite powders were cold rolled into thin strips, using a cold rolling technique. These cold rolled strips possessed excellent morphological characteristics, shown by the homogeneous distribution of the MgH2 spherical particles (10 nm in diameter) in the glassy Ti2Ni matrix. Furthermore, the hydrogenation/dehydrogenation kinetics measured at 225 °C were very fast, as indicated by the short time (400 s) required to uptake/release 5.7 wt% H2. At this temperature, the system possessed good life-time cycling performance – achieving 84 continuous cycles within 30 h without failure or degradation.
Despite these attractive properties, magnesium hydride (MgH2) in its pure form is very stable and has very slow hydrogenation/dehydrogenation kinetics at temperatures less than 350 °C.8,9 Such serious drawbacks are considered as major barriers preventing the use of such an attractive metal hydride material for potential use in fuel cell applications.10,11 Since the 1990s, enormous efforts have been dedicated for improving the hydrogenation/dehydrogenation behaviors of MgH2, using pure metal catalysts,12,13 intermetallic compounds,14 metal oxides,15,16 carbides17 and different families of composite and nanocomposite materials.18–21 Recently, Shinde et al.22 demonstrated that successful self-assembly of MgH2 nanoparticles in activated carbon led to the improvement of the physical and chemical behavior of the hydride phase for achieving reversible hydrogen storage.
In parallel, it has been indicated by several researchers that long-term ball milling leads to the formation of metastable γ-MgH2 that possesses better hydrogenation/dehydrogenation kinetics when compared with the stable β-MgH2 phase.23,24 Sulaiman et al.25 reported that MgH2-X wt% potassium hexafluoronickelate(IV) (K2NiF6, X = 5, 10, 15, 20, and 50) nanocomposite systems showed fast hydrogenation/dehydrogenation kinetics with a low decomposition temperature. Yahya and Ismail have recently used a strontium titanate (SrTiO3) compound to reduce the dehydrogenation temperature of MgH2 to 275 °C.26 Xiao et al. proposed milling MgH2 powders with lithium chloride as an effective method for preparing MgH2 containing a large mole fraction (18 wt%) of γ-MgH2.27 Using a carbon-wrapped transition metal [cobalt/carbon (Co/C), nickel/carbon (Ni/C)] nanoparticles was first proposed by Huang et al., when they used this composite as a catalyst in MgH2 system with ball milling to improve its de/rehydrogenation kinetics and to decrease the decomposition temperature.28 It has been found that adding a small mole fraction (3 wt%) of another metal hydride system (titanium hydride, TiH2) to MgH2, leads to an enhancement of the kinetic behavior of MgH2 and minimizes its decomposition temperature.29 More recently, it has been demonstrated by Valentoni et al. that doping MgH2 with vanadium niobium oxide (VNbO5), a ternary oxide in the range 5, 10 and 15 wt%, leads to a significant reduction of the desorption temperature from 330 °C for the un-doped sample to 235 °C for the VNbO5-doped sample.30
Apart from using crystalline (long-range order) materials for improving the behavior of MgH2, in this paper the possibility of using short-range order (noncrystalline) titanium nickel (Ti2Ni) for enhancing the uptake/release kinetics at low temperature, ranging from 150 °C to 225 °C, is reported. In addition, the performance of MgH2 upon subjecting it to long-term charging/releasing long cycles was also investigated. In addition, the present research presents an interesting approach to fabricating a bulk MgH2 nanocomposite system, using a simple method, which is used for the first time, as far as the author knows. The results are discussed from the point of view of structure, morphology, thermal stability, and kinetics.
The Cu wheel frequency was 70 Hz, where the difference of pressure for injection was 200 mbar. The distance from the crucible to the wheel was about 0.5 mm. The injection temperature was 1450 °C. The as-prepared Ti2Ni ribbons were simply snipped into small pieces (∼4–18 mm length), as shown in Fig. 1c.
For the purpose of the present research, 5 g of as-prepared snipped ribbons were sealed in chromium (Cr)-steel vial (80 ml in diameter) together with five Cr-steel balls (8 mm in diameter) under a helium (He) atmosphere in a glove box, using a ball-to-powder weight ratio of 10 to 1. The vial was then mounted on a cryo mill (Retsch, Germany). The cryo-milling process was operated under a continuous flow of liquid nitrogen with a constant milling frequency of 25 Hz (Fig. 1d). After 6 h of cryo-milling, the vial was released from the mill and opened in the glove box to discharge the milled composite powders.
The deformed tube obtained after 30 passes was opened in the glove box, where the cryo-milled materials were removed. The cold rolling process led to the formation of short strips, with irregular edges and lengths. The strips were trimmed to have near net lengths of ∼6.5 cm, when the crumbled irregular edges were cut away. This process was repeated 10 times in order to obtain 30 g. The strips were then placed between two SUS304 sheets and gently cryo-milled 10 times (Fig. 1g) to ensure the weldability of the MgH2 particles with the amorphous matrix of Ti2Ni. Fig. 1h presents the typical final product of cryo-milled nanocomposite strips prepared in this present study.
The HRTEM image of the as-prepared ion sliced Ti2Ni ribbon is shown in Fig. 3a together with the corresponding selected area diffraction (SAED) pattern. The image revealed a homogeneous structure with maze-like contrast without contrast related to precipitations of any crystalline phases (Fig. 3a). Furthermore, the SAED pattern displayed the typical halo-diffraction of an amorphous phase, as presented in Fig. 3b. The absence of sharp rings and/or spots indicated the absence of any unprocessed Ti2Ni crystalline phase in the prepared amorphous ribbons.
The field effect-scanning electron (FE-SEM) micrograph of the snipped Ti2Ni ribbons (Fig. 1c) cryo-milled for 6 h under a flow of liquid nitrogen (Fig. 1d) is presented in Fig. 3c. The amorphous powders obtained after this stage of milling possessed spherical-like morphology with a particle size distribution in the range of 0.5 μm to 3 μm in diameter, as displayed in Fig. 3(d). It should be emphasised that the cryo-milling process was able to maintain the short-range order of α-Ti2Ni ribbons without crystallization. This is shown by the featureless morphology of the amorphous powders (Fig. 3d) and the presence of a halo electron diffraction pattern (inset of Fig. 3d).
The XRD pattern of MgH2 powders obtained upon reactive ball RBM of hcp-Mg powders under 50 bar pressure of H2 for 6 h is displayed in Fig. 4(a). Pronounced sharp Bragg peaks corresponding to β-MgH2 phase (PDF file # 00-012-0697) co-existed with a small volume fraction of metastable γ-MgH2 phase31 presented together with marginal fraction of unreacted hcp-Mg phase (PDF file # 00-004-0770), as shown in Fig. 4a. At this stage of RBM, the major β-MgH2 phase consisted of large equiaxed grains with a grain size distribution lying in the range of 35 nm to 98 nm, as presented in Fig. 5a. The fast Fourier transform (FFT) image of Zone I oriented to [001] confirmed the formation of β-MgH2, as shown in Fig. 5b.
Fig. 4 XRD patterns of the as-prepared (a) MgH2 powders, obtained after 6 h of RBM, and (b) nanocomposite MgH2/10 wt% MG-Ti2Ni powders obtained after 25 h of cryo-milling time. |
The XRD pattern of MgH2 doped with 10 wt% of MG-Ti2Ni powders and then cryo-milled for 25 h is presented in Fig. 4b. It was plainly seen that the Bragg peaks related to β-MgH2 became broad and had a lower intensity when compared with the corresponding diffraction lines shown in Fig. 4a, implying the formation of ultrafine MgH2 powders after short cryo-milling time (25 h). It should be emphasised that particle size refinement was conducted upon ball milling with hard spherical MG-Ti2Ni powders, which acted as micro/nano milling media. It is also worth noting the absence of diffracted lines related to the crystalline fcc-Ti2Ni phase. This implies that the cryo-milling step maintained the short range order of Ti2Ni without crystallization. The Bragg peaks of β-MgH2 lines were overlapped with a diffuse halo pattern relating to the MG-Ti2Ni phase (Fig. 4d), suggesting that nanocomposite powders had been formed.
The FE-HRTEM image and the corresponding nanobeam diffraction pattern (NBDP) of the nanocomposite MgH2/10 wt% MG-Ti2Ni powders obtained after 25 h of cryo-milling are displayed in Fig. 5c and d, respectively. The cryo-milled powders consisted of a fine featureless light-grey matrix hosting segregated dark grey particles (Fig. 5c) having an average diameter size of 9 nm. The NBD of a crystalline zone (Zone II) oriented to [311] confirmed the presence of a crystalline β-MgH2 phase overlapped with the first and second halo rings of the MG-Ti2Ni phase (Fig. 5d).
The thermal stabilities of MG-Ti2Ni, MgH2, and nanocomposite MgH2/10 wt% MG-Ti2Ni powders were examined, using DSC. The DSC curve obtained at a heating rate of 10 °C min−1 of the as-prepared cryomilled MG-Ti2Ni powders revealed two opposite events, as shown in Fig. 6a. The first was an endothermic reaction which happened because of a glass transformation reaction at an onset temperature (Tg) of 467 °C, as shown in Fig. 6b. The Tg, which referred to the solid amorphous–liquid amorphous phase transformation, was followed by a single sharp exothermic reaction achieved at an onset temperature of 549 °C (Fig. 6b).
The XRD pattern of the sample heated up to 735 °C in the DSC (not shown here) revealed Bragg peaks corresponding to the fcc-Ti2Ni crystalline phase. This implied that the exothermic peak shown in Fig. 6(a) was related to the crystallization of the MG-Ti2Ni phase at a Tx of 569 °C (Fig. 6a). This binary MG system shows a rather wide supercooled liquid region (ΔTx = Tx − Tg) extended to 82 °C, as displayed in Fig. 6b.
In order to avoid undesired pre-and/or crystallization of the MG-Ti2Ni phase, the maximum applied DSC temperature was 400 °C, which was far below the Tx. Each measurement revealed single endothermic decomposition reaction peaks which appeared at different peak temperatures, as presented in Fig. 6d. The Ea calculation, based on an Arrhenius approach, showed a lower value (87.3 kJ mol−1) when compared with the corresponding Ea of MgH2 powders obtained after 6 h of RBM (141.6 kJ mol−1).
The HRTEM image of MgH2/10 wt% MG-Ti2Ni powders milled for 25 h and heated up to 400 °C in DSC is displayed in Fig. 7a. The sample consisted of nanoparticle (∼5 nm to 20 nm in diameter) embedded in a fine featureless matrix. The atomic resolution TEM image taken from the indexed red zone shown in Fig. 7a is presented together with the corresponding NBDP shown in the inset of Fig. 7b. The TEM image revealed a moiré fringe image corresponding to interplanar spacing, d = 0.2439 nm for Mg(100). The NBDP shown in Fig. 7b revealed bright spots related to the hcp-Mg crystal oriented to the zone axis [111]. These spots were clearly overlapped with the first and second halo rings of MG-Ti2Ni, as shown in Fig. 7b. Based on the current TEM resolution, neither MgH2 nor fcc-Ti2Ni could be detected for the sample heated up to 400 °C. This suggests full decomposition of the MgH2 phase, where the MG-Ti2Ni matrix maintained its original amorphous structure without crystallization.
Fig. 7 HRTEM and NBDP images for nanocomposite sample taken after a DSC experiment operated at 10 °C min−1 are shown in (a) and (b), respectively. |
Fig. 8(a) displays the bright field image (BFI) of the cross-sectional view for an ion-sliced MgH2/10 wt% MG-Ti2Ni nanocomposite sheet obtained after the cold rolling process (Fig. 1h). The cold rolled material showed excellent morphological characterization, indicated by the segregation of MgH2 particles that had uniform spherical shapes and narrow particle size distribution (∼10 nm in diameter, Fig. 8a). As a result of the cold rolling process, the MgH2 powders were deeply embedded into the fine amorphous matrix to form a typical nanocomposite system, as displayed in Fig. 8a.
The XRD pattern related to nanocomposite strip sample is presented in Fig. 8b. The sample revealed a diffuse halo pattern related to the MG-Ti2Ni phase, which co-existed with broad and low intensity Bragg peaks corresponding to β- and γ-MgH2 phases, as shown in Fig. 8b. The absence of a crystalline phase related to fcc-Ti2Ni may suggest the capability of the MG-Ti2Ni matrix to withstand the mechanical imperfections introduced by the cryo-milling process. In addition, the significant reduction in MgH2 particle size resulted because of the powder disintegration which the particle underwent with the cryo-milling process.
To investigate the degree of homogeneity and elemental distribution for the cryo-milled strip sample, an STEM/EDS approach was used. The STEM/dark field image (DFI) of the cold rolled strip sample consisted of nanocrystalline grains with an average particle diameter size of 6.8 nm as shown in Fig. 9a. These spherical-like grains were related to MgH2 powders, as indicated by the EDS-mapping of Mg-Kα1–2 (Fig. 9b). The EDS-mapping for the alloying elements (Ti and Ni) of the amorphous matrix were fairly distributed over the whole matrix without compositional fluctuations or degradation, as shown in Fig. 9c and d. This showed that the chemical composition uniformity of α-Ti2Ni was beyond the nanoscale level. The average EDS compositional analysis taken from 25 individual zones, using a 5 nm beam diameter for Mg, Ti and Ni elements was 90.85 wt% Mg and 9.15 wt% Ti2Ni. This value was very close to the nominal composition of the starting material MgH2/10 wt% MG-Ti2Ni.
Fig. 9 STEM-DFI of nanocomposite strip sample is displayed in (a) together with EDS-elemental mapping for (b) MgKα1–2, (c) Ti-Kα, and (d) Ni-Kα. |
Fig. 10a presents the hydrogenation kinetics of the cold rolled strip conducted at different temperatures under 10 bar of H2. At low temperatures of 150 °C, and 175 °C, the sample absorbed about 3.5 and 4.8 wt% of H2, respectively, within 100 s, as shown in Fig. 10a. At a medium temperature range of 200 °C and 225 °C, the hydrogen concentrations absorbed after 100 s were 4.9 and 5.1 wt% H2, respectively. The amount of hydrogen absorbed for the samples examined at 150 °C after 300 s was 4.9 wt% (Fig. 10a). This value increased monotonically with increase of the applied absorption time and tended to become saturated at 5.5 wt% after 479 s, as shown in Fig. 10a.
The sample measured at 175 °C showed better hydrogenation kinetics, as indicated by the shorter time (444 s) required to absorb 5.5 wt% H2. A moderate improvement on the hydrogenation kinetics was attained for the sample measured at 200 °C, as suggested by the short time (356 s) necessary to upload 5.5 wt% H2 (Fig. 10a).
At 225 °C, the sample had significant fast absorption kinetics, characterized by the very short time (194 s) required to upload 5.5 wt% H2. Increasing the absorption time to 400 s allowed the sample to absorb a greater amount of hydrogen (5.7 wt% H2), where it became saturated at this value with a longer absorption time (500 s), as shown in Fig. 10a.
The STEM image and XRD pattern of the sample obtained after a hydrogenation time of 500 s at 225 °C, are shown in Fig. 10b and c, respectively. The hydrogenated sample possessed a typical nanostructure, characterized by the presence of spherical nanoparticles (∼11–20 nm in diameter) embedded in an MG-Ti2Ni fine matrix as shown in Fig. 10b. The XRD pattern of the as-prepared hydrogenated sample revealed Bragg peaks corresponding to β- and γ-MgH2 phases co-existing with unprocessed hcp-Mg (Fig. 10c).
The dehydrogenation kinetic behavior of cold rolled MgH2/10 wt% α-Ti2Ni nanocomposite strips was examined under 200 mbar H2 at three different temperatures. The sample measured at a low temperature (175 °C) showed poor dehydrogenation kinetics, characterized by a very long time (1331 s) taken to desorb −3 wt% H2 (Fig. 10d). This sample required a desorption time of 3611 s to release −5.2 wt% H2, as indicated in Fig. 10d. In contrast to this, the sample measured at a moderate temperature of 200 °C possessed very fast dehydrogenation kinetics, shown by the very short time (353 s) taken to release −3 wt% H2 (Fig. 10d).
After only 922 s, the sample was able to release −5.5 wt% H2. No remarkable change in the amount of released H2 could be obtained even after processing for 2411 s, suggesting completion of desorption process, as shown in Fig. 10d. Superior dehydrogenation kinetics was obtained with a small increase of the desorption temperature to 225 °C. At this temperature, the sample was able to desorb −3 wt% H2 in a very short time (105 s), as displayed in Fig. 10d. Increasing the time to 333 s caused the sample to desorb its full hydrogen storage capacity (−5.7 wt% H2), where there was no remarkable change in this value even if a longer desorption time (1224 s) was used, as shown in Fig. 10d.
Fig. 10(e) presents the XRD pattern of the sample heated at 225 °C and taken after complete release of H2. The sample revealed very sharp Bragg peaks related to the hcp-Mg overlap with minor diffraction lines from the undecomposed β-MgH2 phase, as shown in Fig. 10e.
The cycle-life-time test is one of the most important and fundamental characterization approaches used to examine the performance of metal hydrides. In the present study, the cold-rolled strip nanocomposite was examined at 225 °C under H2 pressures varying from 200 mbar (desorption) to 10 bar (absorption). The test was repeated in a cyclic fashion for 30 h, and the results are shown in Fig. 11a. In order to maintain the short-range order of the MG-Ti2Ni matrix and to avoid its potential crystallization, the nanocomposite strip was not activated. The sample shows good cyclic performance, characterized by the near hydrogen storage values (5.48 wt% H2) and closed uptake/release kinetics during the cycle-life-time extended to 30 h (Fig. 11a).
The low magnification BFI of the sample taken after the cycle-life-test is shown in Fig. 11b. Obviously, the Mg particles obtained after the cycle test were segregated and maintained their nano spherical-like morphology (∼9 nm in diameter), as shown in Fig. 11b. Furthermore, they were uniformly embedded in the matrix, which indicated the homogeneity of chemical composition. The corresponding SAED pattern exhibited primary and secondary haloes related to the MG-Ti2Ni phase (matrix), as shown in Fig. 11c. These haloes overlapped with sharp spots (Fig. 11c) corresponding to the Mg crystals embedded in the matrix with different orientations. A pressure–composition–temperature (PCT) test was used to examine the cyclability and performance of pure MgH2 powders obtained after 6 h of RBM.
The PCT experiment was conducted at 300 °C under 70 bar of H2 pressure for 100 continuous cycles, as shown in Fig. 11d. However, the first cycle, showed a high H2 storage capacity of 6.8 wt%, and the following cycles (2 to 100) revealed a seriously steep degradation of this value (Fig. 11d). After 50 cycles, the hydrogen storage capacity decreased to 5.7 wt%, where it then decreased to 5.3 wt% after processing for 100 cycles, as shown in Fig. 11d.
The morphological characteristics of the MgH2 sample obtained after processing for 100 cycles in the PCT test were investigated using TEM analysis (Fig. 11e). The sample revealed a single phase of Mg metal, as indicated by the sharp spots corresponding to Mg[023] presented in Fig. 11f. The Mg metal obtained after the PCT test suffered from an extreme agglomeration effect, which resulted in a formation of very large powder particles with an apparent size of 10 μm, as shown in Fig. 11e.
During the last stage of milling, the MgH2 powder sizes reached a level (less than 1 μm in diameter) in which the ball-milling media could not introduce effective “trap and nipping” of the powders, which are required for further grain refining. Increasing the ball milling time led also to the “migration” of a large volume fraction of the abrasive MG powders through the cavities and micro-channels created in the body of the MgH2 particles to be located close to the grains. Thus, they broke up the large MgH2 grains (Fig. 12c) along their weak grain boundary zones (Fig. 12d) to form finer powders with a large volume fraction of nanostructured MgH2 grains co-existing with the MG-Ti2Ni particles (Fig. 12e).
It was found that the cold rolling of cryo-milled nanocomposite powders for 30 passes (Fig. 12f) had a beneficial effect on achieving further grain refining of the MgH2 powder upon the introduction of severe plastic deformation on the MgH2 grains.
In addition, this led to the consolidation of the powders into bulk nanocomposite strips with a good distribution of MgH2 powders into the noncrystalline MG powder-matrix (Fig. 12g). Because the H2 diffusion is much faster along the grain boundaries when compared with grains inside, the hydrogenation/dehydrogenation kinetic behaviors of MgH2 were gradually improved with increase of the number of “liberated” grains.
Table 1 summarizes the results of H2 storage properties obtained in the present work in comparison with some of other systems. For this purpose, abrasive catalytic powders, such as metal oxides, carbides and intermetallic compounds were chosen. As is clearly shown from the results shown in Table 1, the hydrogenation/dehydrogenation kinetics of the present system is very fast when compared, for example, with metal oxides [10 wt% niobium(V) oxide (Nb2O5), aluminium oxide (Al2O3) and silicon carbide (SiC)]. Whereas the gas uptake and release of the present system were achieved at a rather low temperature (225 °C), higher temperatures were always required for most of the other systems, as shown in Table 1. However, the results of a recent study34 showed that a MgH2/10 wt% Nb2O5 system possessed very fast hydrogenation and dehydrogenation kinetics for absorption/desorption of 5 wt% H2 at 225 °C within 1200 s/700 s.
Catalyst | Hydrogenation/dehydrogenation properties | Ref. |
---|---|---|
10 wt% MG-Ti2Ni | Absorption/5.7 wt% H2/10 bar/225 °C/400 s, desorption/5.7 wt% H2/200 mbar/225 °C/400 s, cycle-life-time: 30 h (84 cycles) | Present work |
5 wt% Nb2O5 | Absorption/5.2 wt% H2/10 bar/300 °C/400 s,dDesorption/6 wt% H2/0.1 kPa/300 °C/400 s | 32 |
10 wt% Nb2O5 | Absorption/5.8 wt% H2/5 bar/300 °C/30 min, desorption/5.8 wt% H2/0.1 bar/300 °C/350 min | 33 |
10 wt% Nb2O5 | Absorption/5.0 wt% H2/10 bar/225 °C/1200 s, desorption/5.0 wt% H2/0.02 bar/225 °C/700 s | 34 |
10 wt% Al2O3 | Absorption/4.09 wt% H2/15 bar/300 °C/110 min, desorption/NA | 35 |
10 wt% Al2O3 | Absorption/4.22 wt% H2/12 bar/320 °C/10 min/max storage capacity: 5.2 wt%, desorption/NA | 36 |
15 wt% VNbO5 | Absorption/5.5 wt% H2/20 bar/160 °C/10 min, absorption/desorption 50 cycles/275 °C | 37 |
10 wt% SiC | Absorption/3.7 wt% H2/10 bar/350 °C/140 s, desorption/2.5 wt% H2/0.02 bar/350 °C/2000 s | 38 |
10 wt% V0.75Ti0.05Cr0.20 | Absorption/3 wt% H2/1 bar/25 °C/75 min/max storage capacity: 6.1 wt%, desorption/5.5 wt% H2/0.01 bar/240 °C/5 min | 39 |
14 wt% TiAl | Absorption/4 wt% H2/1 bar/25 °C/100 min/max storage capacity: 5 wt%, desorption/4 wt% H2/0.1 bar/240 °C/7 min | 40 |
7 wt% Mn3.6Ti2.4 | Absorption/5.3 wt% H2/10 bar/275 °C/2 min, desorption/5.3 wt% H2/0.02 bar/275 °C/8 min, cycle-life-time: 1400 h (1000 cycles) | 41 |
10 wt% ZrNi5 | Absorption/5.3 wt% H2/10 bar/275 °C/1 min, desorption/5.3 wt% H2/0.02 bar/275 °C/12 min, cycle-life-time: 568 h (600 cycles) | 42 |
10 wt% big-cube Zr2Ni | Absorption/5.1 wt% H2/10 bar/250 °C/100 s, desorption/5.1 wt% H2/0.02 bar/250 °C/613 s, cycle-life-time: 1250 h (2546 cycles) | 43 |
It has recently been found that the MgH2/15 wt% vanadium niobium oxide (VNbO5) system possessed excellent kinetics behavior.37 This was indicated by the low temperature (160 °C) necessary to absorb 5.5 wt% H2 within 10 min (Table 1). However, the dehydrogenation process of MgH2/15 wt% VNbO5 system when compared with our system, had taken place at a higher temperature (275 °C).
The MgH2/10 wt% V0.75Ti0.05Cr0.20 system can absorb 3 wt% H2 at normal pressure and temperature within 75 min.39 The dehydrogenation kinetics, however, showed that at 240 °C to 5.5 wt% was released in 5 min.39 Better H2 storage capacity (4 wt%) can be achieved within 100 min at normal pressure and temperature upon doping MgH2 with 14 wt% titanium aluminide (TiAl) powders.40 Likewise in the MgH2/V0.75Ti0.05Cr0.20 system, the dehydrogenation process required a longer time (7 min) and higher temperature (240 °C) to be complete.40 In addition, some new systems such as MgH2/Mn3.6Ti2.4, MgH2/ZrNi5 and MgH2/big-cube Zr2Ni41–43 have shown promising results, indicated by fast uptake/release kinetics at moderate temperatures (250–275 °C), long cycle-life-time (600–2546 cycles), as shown in Table 1.
In contrast to pure metal catalysts, the catalytic agents presented in Table 1 are heterogeneous catalysts which do not react with Mg/MgH2 to form intermediate compounds. Until now, the mechanism of this group of catalysts including MG-Ti2Ni powders was not clear. It was agreed that doping MgH2 with hard abrasive particles led to a dramatic disintegration of the MgH2 powders to form finer powders.32–43 They also play an important part in the splitting/recombination of hydrogen molecules during the hydrogenation/dehydrogenation processes.41,42 This led to enhancement of the kinetics behavior of MgH2 and lowering of the apparent activation energy.37
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