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Article

Hydrogen Storage Characteristics and Corrosion Behavior of Ti24V40Cr34Fe2 Alloy

1
School of Chemical and Metallurgical Engineering, Faculty of Engineering and Built Environment, University of the Witwatersrand, Johannesburg Private Bag 3, Wits 2050, South Africa
2
Department of Mechanical Engineering, Faculty of Engineering, Federal Polytechnic, Offa 24013, Nigeria
3
Department of Materials and Metallurgical Engineering, Faculty of Engineering and Technology, University of Ilorin, Ilorin 240003, Nigeria
4
BASF/Battery Materials-Ovonic, 2983 Waterview Drive, Rochester Hills, MI 48309, USA
*
Author to whom correspondence should be addressed.
Batteries 2017, 3(2), 19; https://doi.org/10.3390/batteries3020019
Submission received: 14 February 2017 / Revised: 19 May 2017 / Accepted: 8 June 2017 / Published: 14 June 2017
(This article belongs to the Special Issue Nickel Metal Hydride Batteries 2017)

Abstract

:
In this work, we investigated the effects of heat treatment on the microstructure, hydrogen storage characteristics and corrosion rate of a Ti34V40Cr24Fe2 alloy. The arc melted alloy was divided into three samples, two of which were separately quartz-sealed under vacuum and heated to 1000 °C for 1 h; one of these samples was quenched and the other furnace-cooled to ambient temperature. The crystal structures of the samples were studied via X-ray diffractometry and scanning electron microscopy. Hydrogenation/dehydrogenation characteristics were investigated using a Sievert apparatus. Potentiostat corrosion tests on the alloys were performed using an AutoLab® corrosion test apparatus and electrochemical cell. All samples exhibited a major body-center-cubic (BCC) and some secondary phases. An abundance of Laves phases that were found in the as-cast sample reduced with annealing and disappeared in the quenched sample. Beside suppressing Laves phase, annealing also introduced a Ti-rich phase. The corrosion rate, maximum absorption, and useful capacities increased after both heat treatments. The annealed sample had the highest absorption and reversible capacity. The plateau pressure of the as-cast alloy increased after quenching. The corrosion rate increased from 0.0004 mm/y in the as-cast sample to 0.0009 mm/y after annealing and 0.0017 mm/y after quenching.

1. Introduction

Ti-V-Cr body-centered-cubic (BCC) solid solution alloys are very promising for the storage of a large quantity of hydrogen at room temperature [1,2,3]. Some of the identified shortcomings of these alloys include poor pressure-composition-temperature (PCT) plateau characteristics, low hydrogen desorption capacities, and long activation times [4,5,6,7]. In an attempt to improve on these shortcomings, controlled quantities of additives such as Fe, Zr, and Mn have been found to be effective in lowering cost and enhancing the overall performance of the alloy [8,9,10,11]. The effects of substituting Fe for Cr on the hydrogen storage property of the Ti0.32Cr0.43V0.25 alloy showed that the desorption plateau pressure increased without decrease in effective hydrogen capacity, suggesting the possibility of using ferrovanadium as a substitute for the expensive pure vanadium [12]. Increasing the V content in Vx–(Ti–Cr–Fe)100−x (Ti/(Cr+Fe) = 1.0, Cr/Fe = 2.5, x = 20–55) alloys led to an increase in both the hydrogen absorption capacity and desorption capacity, but decreased the plateau pressure [13]. Miao et al. [14] found that all of the alloys Ti0.8Zr0.2V2.7Mn0.5Cr0.8−xNi1.25Fex(x = 0.0–0.8) mainly consisted of two phases, the C14 Laves phase with a three-dimensional network and the dendritic V-based solid solution phase. Further, the lattice parameters of the two phases and the maximum discharge capacity decreased with an increase in Fe content, but the cyclic stability and the high rate dischargeability increased first and then decreased with increasing x. Liu et al. [15] found that Ce addition favored the chemical homogeneity of the BCC phase and, therefore, improved the hydrogen storage properties of the (Ti0.267Cr0.333V0.40)93Fe7Cex (x = 0, 0.4, 1.1 and 2.0 at%) alloys. To increase the hydrogen storage capacity and the plateau pressure of the Ti0.32Cr0.43V0.25 alloy, Yoo et al. [16] replaced a fraction of the Cr with Mn or a combination of Mn and Fe. When Mn was used alone, the effective hydrogen storage capacity increased to about 2.5 wt% though the plateau pressure showed no significant change. However when Fe was added with Mn, both the effective hydrogen storage capacity and the plateau pressure increased.
Further efforts include assessing the effects of heat treatment on hydrogen absorption properties; Okada et al. [1] found that moderate heat treatment, specifically annealing at 1573 K for 1 min, enhanced the storage capacity and flattened the desorption plateau of Ti25Cr40V35 alloy. Liu et al. [17] reported that heat treatment effectively improved the flatness of the plateau and improved the hydrogenation capacity of Ti32Cr46V22 alloy by lowering the oxygen concentration and homogenizing the composition and microstructure. A hydrogen desorption capacity of 2.3 wt % was achieved when Ti32Cr40V25 was annealed at 1653 K for 1 min. [18]. Chuang et al. [19] found that annealing atomized powder of Ti-Zr based alloy at 1123 K for 4 h greatly enhanced the discharge capacity. Hang et al. [20] heat-treated Ti10V77Cr6Fe6Zr alloy at a relatively lower temperature, but elongated the soaking time by annealing at 1523 K for 5 min and at 1373 K for 8 h, and found that the sample annealed at 1523 K for 5 min had the best overall hydrogen storage properties, with a desorption capacity of 1.82 wt % and a dehydriding plateau pressure of 0.75 MPa.
Although BCC solid solution alloys have very high gaseous phase hydrogen storage capacities, they suffer from severe capacity degradation during electrochemical applications due to the leaching of Vanadium (V) into the KOH electrolyte [21,22]. The preferential leaching of V in the negative electrode material has been previously identified [23], and V-free Laves phase alloys have been adopted to mitigate the consequent cycle life and self-discharge issues originating from V-corrosion [24,25].
Metal corrosion mainly occurs through electrochemical reactions at the interface between the metal and electrolyte [26]. The basic process of metallic corrosion in an aqueous solution consists of the anodic dissolution of metals and the cathodic reduction of oxidants present in the solution:
Mm → M2+aq +2em anodic oxidation
2OX aq +2em → 2Red(eredox)aq cathodic oxidation
In the formulae, Mm is the metal in the state of metallic bonding; M2+aq is the hydrated metal ion in an aqueous solution; em is the electron in the metal; Oxaq is an oxidant; Red(eredox)aq is a reductant; and eredox is the redox electron in the reductant. The overall corrosion reaction is then written as follows:
Mm +2Oxaq → M2+aq +2Red(eredox)aq
These reactions are charge-transfer processes that occur across the interface between the metal and the aqueous solution, hence they are dependent on the interfacial potential that essentially corresponds to what is called the electrode potential of metals in electrochemistry terms. In physics terms, the electrode potential represents the energy level of electrons, called the Fermi level, in an electrode immersed in electrolyte. For normal metallic corrosion, in practice, the cathodic process is carried out by the reduction of hydrogen ions and/or the reduction of oxygen molecules in an aqueous solution. These two cathodic reductions are electron transfer processes that occur across the metal–solution interface, whereas anodic metal dissolution is an ion transfer process across the interface.
The rate of the reaction is evaluated in terms of the corrosion current. The natural logarithm of the absolute value of the corrosion current versus the potential value is plotted as a Tafel curve. The corrosion current values can be transformed to corrosion rate (CR) values (e.g., mm/y) using Equation (1) [27]:
C R   = K   i c o r r ρ E W
where K is a constant that depends on the unit of corrosion rate; K = 3272 for mm/y (mmpy), or = 1.288 × 105 for milli-inches/y (mpy), icorr = corrosion current density (μA·Cm−2), ρ = alloy   density     ( g · C m 3 ) , EW = Equivalent weight = 1/electron equivalent (Q) where:
Q =   n i f i W i
where ni = the valence if ith element of the alloy, fi = the mass fraction of the ith element in the alloy, Wi = the atomic weight of the ith element in the alloy.
By combining Equations (1) and (2), the penetration rate (CR and mass loss, ML) of an alloy is given by:
C R   = K 1   i c o r r   ρ n i f i W i
M L =   K 2 i c o r r E W
The equations above give values of 0.1288 if the unit of CR is m/y and 0.03272 if the unit of CR is mm/y [28]. This work investigates the influence of heat treatment on hydrogen storage capacity and corrosion rate of Ti34V40Cr24Fe2 in standard KOH electrolyte. V-based hydrogen storage alloys are often used as the anode in NiMH batteries [29].
Cho et al. [29] identified a composition region in the Ti-V-Cr phase diagram as having the highest hydrogen uptake. This informed the choice of the base alloy Ti25V40Cr35, which falls within the region. The choice to use Fe as the additive was made because of its relatively low cost. Literature has shown that in the ternary Ti-V-Cr system [12,13,14,15,16,30], Fe substituted Cr or V and FeV was used in place of expensive V. Thus, research gap is noted, as the effect of substituting Fe at the Ti site on hydrogen storage and corrosion behavior of Ti25V40Cr35 has not yet been investigated. The present work on substituting an equal quantity of Fe for Cr and Ti on the hydrogen storage and corrosion behavior of Ti25V40Cr35 therefore fills this gap.

2. Experimental Setup

The raw materials for this work were sourced from Metrohm, South Africa, including iron (325–290 mesh, 99% purity, 0.01% C and 0.015% P and S); chromium (<0.3mm, 99.8% purity); vanadium (−325 mesh, 99.5% purity); and titanium (−325 mesh, 99.5% purity). A 10-g sample of Ti34V40Cr24Fe2 alloy was prepared in a water-cooled, copper-crucible arc melting furnace under argon atmosphere. The ingot was turned over and remelted three times to ensure homogeneity. After melting, the ingot was divided into three pieces. Two cut samples were vacuum-sealed in separate silica glass tubes in preparation for heat treatment.
The two quartz-sealed specimens were loaded in a heat treatment furnace and heated to 1000 °C for 1 h. One tube was immediately removed and broken in cold water to quench the alloy, thereby locking the microstructure, while the second sample was slowly furnace-cooled to room temperature.
The crystal structure and lattice parameters in the as-cast and heat-treated samples were determined by X-ray diffraction (XRD) analysis, using a Bruker D2_Phaser X-ray® diffraction instrument (Bruker AXS, Inc., Madison, WI, USA) with Cu-Kα radiation from 2θ = 10° to 80°. Xpert High Score® phase identification software produced by Philips analytical B.V. Almelo Netherlands was used to identify the phases from the XRD data. Elemental compositions of the phases were determined using an FEI Nova NanoSEM 200® scanning electron microscope (SEM) (FEI, Hillsboro, OR, USA) fitted with EDAX® advanced microanalysis solution (EDAX Inc., Mahwah, NJ, USA). The amount of phases was determined by image analysis using the ImageJ freeware (National Institute of Mental Health, Bethesda, MD, USA).
Pottentiostatic corrosion tests on the alloys were performed using an AutoLab® corrosion test apparatus (Metrohm Autolab B.V., Utrecht, The Netherlands) and an electrochemical cell consisting of a tri-electrode (a platinum reference electrode, Ag/AgCl counter electrode, and 0.14 cm2 test alloy as the working electrode). An aqueous solution of 6 mol·L−1 KOH was used as the electrolyte. The alloys were cut into rectangles and a copper wire of suitable length was attached to one side of the specimen with aluminum tape. The sample was then covered in cold-resin for 24 h to enable curing, while leaving only the test surface exposed. When cured, the test surface was ground to 1200 grit. The corrosion experiments were performed at 25 °C and Tafel curves were recorded from −1.4V to −0.2 V with a scanning rate of 1 mV·sec−1.
Measurement of the Pressure Composition Temperature, PCT isotherms was performed using a Suzuki-Shokan multi-channel PCT (Suzuki Shokan, Tokyo, Japan) system. Samples were crushed into particles <75 µm in size, and 1 g of each alloy was sealed into a stainless steel reactor and heated to 573 K. Next, 3 MPa of hydrogen pressure was introduced into the apparatus for 30 min, followed by slow cooling to room temperature in a hydrogen atmosphere. The alloys absorbed most of the hydrogen and were pulverized in this step. After the hydrogenation process, the samples were heated to 573 K and chamber was evacuated for 1 h with a mechanical pump to completely dehydrogenate the samples for PCT measurements at 303, 333, and 363 K successively.

3. Results and Discussion

3.1. Microstrcuture

The XRD pattern in Figure 1 shows mainly a BCC (V) phase and some minor peaks from secondary phases. Phase analysis indicated that both C14 and C15 phases co-existed in the as-cast sample and transformed into an α-Ti phase after annealing (Table 1). Changes in the lattice parameters of the BCC main phase and the α-Ti secondary phase with the different preparation methods are negligible. The annealed sample showed the least amount of α-Ti.
Figure 2 shows the representative back scattering electron (BSE) images of the as-cast and heat-treated (both slow cooled and quenched) Ti34V40Cr24Fe2. The microstructure of the alloy was a primary, light grey phase (C) with some darker intergranular phases (D and E) in all three samples. The primary light grey phase corresponds to the main peak of BCC (V) phase, while the black intergranular and the dark phases were the Laves and Ti-rich secondary phases. X-ray energy dispersive spectroscopy (EDS) was used to measure compositions in the areas of interest, and the results are summarized in Table 2. The EDS technique measures the average composition within 1–2 microns volume (depending on the primary electron energy) due to the nature of electron scattering in the solid. The secondary phases in this study are either below or about that range, and therefore EDS result can only indicate relative change in composition. In the as-cast sample, areas D and E have relatively higher Ti-contents with a smaller atomic weight, which resulted in a darker contrast. Areas D and E are assigned to C14 and C15 from the combined results of the XRD and EDS measurements. In the annealed sample, C15 phase transformed into C14 phase (area D) and a Ti-rich phase (area E) started to appear. We believe this Ti-rich phase can be assigned to the α-Ti phase found in the XRD analysis. The α-Ti phase only has a very small solubility of Cr and V [31]. The high V and Cr contents found in the EDS data in Table 2 can be explained by either the small grain size of Ti-phase, which is below the sampling volume of the EDS technique, or a mixture of microcrystalline Ti/C15 that occurred as the product of a Eutectic solidification at 667 °C [32]. Quenching introduced twinning in the secondary phase, as shown inside the circle (F). The addition of Fe into the TiVCr solid solution is known to promote the secondary Laves phase [33,34,35], which is considered to be a catalyst that facilitates hydrogenation/dehydrogenation kinetics [36]. The reduction in the Laves phase abundance by thermal annealing was reported before with a Laves phase-related BCC TiZrV-based alloy [37].
Table 2 shows that the BCC (V) in all three samples contained 17–22 at% Ti, 40–44 at% V, and ~36 at% Cr. The black intergranular E areas in Figure 2b,c contained 23–66 at% Ti, 18–41 at% V, and 14–36 at% Cr. The heat treatment reduced the Laves phase abundance from 21.5 to 18% and the quenching totally removed it. The Ti/Cr ratio in the BCC phase is almost equal in all three samples. However, the ratio of the darker areas (containing Laves phase and Ti-phase) increased from 0.6 to 4.4 after annealing and to ~2 after quenching.

3.2. Gaseous Phase Hydrogen Storage

Table 3 shows that both heat treatment processes increased the reversible hydrogen storage capacity (RHSC); the capacity increased from 0.44 to 1.26 wt % after annealing and to 0.65 wt % in the quenched sample. Literature indicates that annealing increases hydrogen capacity [13,14]. The BCC phase enhances hydrogen capacity [11,22,29]; an increase in its unit cell volume implies the availability of more hydrogen absorption sites or spaces, leading to an increase in storage capacity. The Laves phase is detrimental to storage capacity [10,38,39,40], and alloys with larger Laves unit cell volumes or high Laves proportions are known to exhibit lower hydrogen capacity. Therefore, the observed increase in useful capacity after heat treatment was due to the increase in the BCC unit cell volume. The abundance of catalytic Laves phase in the as-cast sample reduced after annealing; this suggests another reason for the higher hydrogen capacity observed in the annealed sample.
Table 3 also shows that the desorption plateau pressure reduced after annealing the alloy at 1000 °C for 1 h, while it rose after quenching. Specifically, the pressure of the desorption plateau decreased from 1.32 to 0.68 MPa after annealing and increased to 2.34 MPa after quenching. The plateau properties are affected by both the homogeneity and oxygen content in Ti-V based hydrogen storage alloys [10]. Inhomogeneity of microstructure can be minimized by heat treatment at higher temperatures for a short time [41]. The observed reduction in the plateau pressure after annealing suggests a homogenized microstructure; in addition, the sample was annealed in a vacuum-sealed quartz tube, thereby preventing oxygen intake. The quenched sample was exposed to oxygen in the quenching medium; therefore, the rise in plateau pressure suggests the presence of a higher oxygen content.
In Figure 3a, the PCT isotherms for both the as-cast and heat-treated alloys were steep, an indication of high plateau pressure. However, the isotherm for the annealed sample showed a flatter and wider plateau, indicating a reduction in plateau pressure, and the wider plateau also indicated higher hydrogen capacity.
In Figure 4, the maximum absorption capacity decreased with increasing isotherm temperatures, similar to what has been previously described in the literature [42]. For the as-cast sample, the maximum absorption capacity was 0.86 wt % at 30 °C, and the capacity declined to 0.69 and 0.62 wt % as the temperature rose to 333 and 363 K, respectively. Similar trends were observed for the annealed and quenched samples. The kinetic energy of gas increased with increasing temperatures; a low kinetic energy is associated with lower temperatures, while increased temperature leads to high kinetic energy. Hydrogen gas atoms with a low kinetic energy are more easily absorbed than those with high kinetic energy because gases with higher kinetic energy move faster, thus requiring additional force to attract to the surface of the adsorbate. This explains the observed higher capacity at low temperatures and lower capacity at high temperatures.
The stability of the current alloy can be improved with the addition of Ni to promote other secondary phases, such as TiNi [43] and Ti2Ni [44]. The synergetic interaction between the main storage phase (BCC) and secondary phases can reduce the equilibrium plateau pressure of the BCC phase and make them available for electrochemical storage purposes [45].

3.3. Corrosion Behavior

The corrosion behavior of Ti34V40Cr24Fe2 alloys in 30% KOH aqueous solution was studied by Tafel curve measurements, and the results are plotted in Figure 5a. No significant change was observed in the corrosion potential (Ecorr) for the as-cast alloy after annealing. However, a decrease from −0.80 to −0.867 mV was observed after quenching. Both heat treatment processes increased the corrosion rate of the alloy (Figure 5b). The rate increased from 0.0004 in the as-cast alloy to 0.0009 mm/y after annealing and to 0.0017 mm/y after quenching.
Cr is known to improve the corrosion resistance of an alloy [40,41]. Samples containing high at % Cr are expected to have low corrosion rates and vice versa. Therefore, an increase in the corrosion rate of heat-treated samples could be a result of a reduction in Cr content in the secondary phase. The phase structure and oxide layer are among the factors that determine the corrosion rate of an alloy. The Laves structure has been reported to have a thinner oxide layer than the BCC structure [42], and this oxide layer is known for passivation of corrosion [43,44,45]. It is therefore implied that for a dual phase alloy, such as the alloys being investigated in this research, the corrosion rate will increase when the proportion of the Ti-rich phase with a thinner oxide layer increases. The Ti-rich phase is more easily corroded than the BCC phase [46].

4. Conclusions

The influence of heat treatment on the microstructure and hydrogen storage capacity of Ti34V40Cr24Fe2 at% alloys was investigated. The main phase of all alloys under different preparations is a BCC phase, while the secondary phase shifted from a Laves phase to a Ti-rich phase with annealing. Heat treatment was beneficial with regard to hydrogen capacity, but detrimental to corrosion behavior. Though both heat treatment processes enhanced useful hydrogen capacity, the annealed sample had superior storage characteristics. Although both annealing and quenching increased the corrosion rate of the alloy, the rate of corrosion was found to be highest in the quenched sample with the highest amount of Ti-rich phase.

Acknowledgments

The work is supported by African Material Science and Engineering Network, AMSEN, and the National Research Found NRF Thuthuka programme.

Author Contributions

Jimoh Mohammed Abdul and Lesley Hearth Chown designed the experiments and analyzed the results. Jamiu K. Odusote and Jean Nei conducted the corrosion and PCT measurements, respectively, and Kwo-Hsiung Young and Woli Taiye Olayinka, assisted in data analysis and manuscript preparation.

Conflicts of Interest

The authors declare no conflict of interest.

Abbreviations

BCCBody-centered-cubic
PCTPressure-concentration-temperature
CRCorrosion rate
icorrCorrosion current density
EWEquivalent weight
MLMass loss
XRDX-ray diffractometer
SEMScanning electron microscopy
BSEBack-scattering electron
EDSEnergy dispersive spectroscopy
RHSCReversible hydrogen storage capacity
EcorrCorrosion potential

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Figure 1. XRD patterns of the as-cast and heat-treated Ti34V40Cr24Fe2 alloys.
Figure 1. XRD patterns of the as-cast and heat-treated Ti34V40Cr24Fe2 alloys.
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Figure 2. SEM BSE micrographs of (a) the as-cast, (b) annealed, and (c) quenched Ti34V40Cr24Fe2.
Figure 2. SEM BSE micrographs of (a) the as-cast, (b) annealed, and (c) quenched Ti34V40Cr24Fe2.
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Figure 3. PCT desorption curves of the as-cast and heat-treated Ti34V40Cr24Fe2 alloys at (a) 303, (b) 333, and (c) 363 K.
Figure 3. PCT desorption curves of the as-cast and heat-treated Ti34V40Cr24Fe2 alloys at (a) 303, (b) 333, and (c) 363 K.
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Figure 4. Influence of isotherm temperatures on maximum hydrogen capacity.
Figure 4. Influence of isotherm temperatures on maximum hydrogen capacity.
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Figure 5. (a) Tafel curves and (b) corrosion rates of the as-cast and heat-treated Ti34V40Cr24Fe2.
Figure 5. (a) Tafel curves and (b) corrosion rates of the as-cast and heat-treated Ti34V40Cr24Fe2.
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Table 1. XRD crystallographic parameters of the as-cast and heat-treated Ti34V40Cr24Fe2.
Table 1. XRD crystallographic parameters of the as-cast and heat-treated Ti34V40Cr24Fe2.
Crystallographic Description
SamplePhasesSpace Group (No.)AcUnit Cell Volume (Å3)
As-castBCC (V) I m 3 ¯ m (229)3.0027.08
C14 (Laves) P 6 3 / m m c (194)4.857.94161.7
C15 (Laves)Fd 3 ¯ m (227)6.943334.69
AnnealedBCC (V) I m 3 ¯ m (229)3.0127.37
α-Ti P 6 3 / m m c (194)2.984.7336.24
QuenchedBCC (V) I m 3 ¯ m (229)3.0127.37
α-Ti P 6 3 / m m c (194)2.984.7336.24
Table 2. EDS results of the as-cast and heat-treated Ti34V40Cr24Fe2.
Table 2. EDS results of the as-cast and heat-treated Ti34V40Cr24Fe2.
Composition (at%) Phase Proportion (% Area)
SampleLocationTiVCrFeTi/Cr RatioPhase Identification
As-castC17.7 (1.1)43.5 (1.6)36.5 (2.2)2.3 (0.7)0.5BCC78.5
D24.7 (0.8)37.8 (0.7)34.0 (0.4)3.5 (0.3)0.7C141.3
E23.0 (3.7)41.4 (2.4)35.5 (1.4)2.0 (0.2)0.6C1520.2
Annealed
C17.7 (1.9)43.5 (1.3)36.5 (2.9)2.3 (0.2)0.5BCC82.0
E65.9 (5.2)18.6 (2.8)14.9 (2.2)0.6 (0.2)4.4α-Ti/BCC12.0
QuenchedC21.8 (1.5)40.0 (1.3)35.6 (1.2)2.6 (1.7)0.6BCC80.5
E47.3 (3.7)21.6 (2.5)24.7 (1.4)6.4 (0.5)1.9α-Ti/BCC19.5
Table 3. Effect of heat treatment on H storage properties of Ti34V40Cr24Fe2 alloy.
Table 3. Effect of heat treatment on H storage properties of Ti34V40Cr24Fe2 alloy.
SampleAbsorption Capacity (wt %)Capacity Remaining (wt %)RHSC (wt %)Plateau Pressure (MPa)
As-cast0.860.420.441.32
Annealed1.540.281.260.68
Quenched1.040.390.652.34

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Mohammed Abdul, J.; Hearth Chown, L.; Kolawole Odusote, J.; Nei, J.; Young, K.-H.; Taiye Olayinka, W. Hydrogen Storage Characteristics and Corrosion Behavior of Ti24V40Cr34Fe2 Alloy. Batteries 2017, 3, 19. https://doi.org/10.3390/batteries3020019

AMA Style

Mohammed Abdul J, Hearth Chown L, Kolawole Odusote J, Nei J, Young K-H, Taiye Olayinka W. Hydrogen Storage Characteristics and Corrosion Behavior of Ti24V40Cr34Fe2 Alloy. Batteries. 2017; 3(2):19. https://doi.org/10.3390/batteries3020019

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Mohammed Abdul, Jimoh, Lesley Hearth Chown, Jamiu Kolawole Odusote, Jean Nei, Kwo-Hsiung Young, and Woli Taiye Olayinka. 2017. "Hydrogen Storage Characteristics and Corrosion Behavior of Ti24V40Cr34Fe2 Alloy" Batteries 3, no. 2: 19. https://doi.org/10.3390/batteries3020019

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