Next Article in Journal
Surface-Enhanced Carboxyphenyl Diazonium Functionalized Screen-Printed Carbon Electrode for the Screening of Tuberculosis in Sputum Samples
Next Article in Special Issue
Graphene-Modified Co-B-P Catalysts for Hydrogen Generation from Sodium Borohydride Hydrolysis
Previous Article in Journal
Recent Progress of Nanogenerators for Green Energy Harvesting: Performance, Applications, and Challenges
Previous Article in Special Issue
Micro/Nano Energy Storage Devices Based on Composite Electrode Materials
 
 
Search for Articles:
Title / Keyword
Author / Affiliation / Email
Journal
Article Type
 
 
Advanced Search
 
Section
Special Issue
Volume
Issue
Number
Page
 
Journals
Nanomaterials
Volume 12
Issue 15
10.3390/nano12152550
nanomaterials-logo
Submit to this Journal Review for this Journal Propose a Special Issue
► Article Menu

Article Menu

share Share announcement Help format_quote Cite question_answer Discuss in SciProfiles thumb_up
...
Endorse textsms
...
Comment
first_page
settings
Order Article Reprints
Font Type:
Arial Georgia Verdana
Font Size:
Aa Aa Aa
Line Spacing:
Column Width:
Background:
Article

Bimetallic Pt-Ni Nanoparticles Confined in Porous Titanium Oxide Cage for Hydrogen Generation from NaBH4 Hydrolysis

by
Yuqian Yu
1,†,
Li Kang
1,†,
Lixian Sun
1,2,*,
Fen Xu
1,*,
Hongge Pan
3,*,
Zhen Sang
1,
Chenchen Zhang
1,
Xinlei Jia
1,
Qingli Sui
1,
Yiting Bu
1,
Dan Cai
1,
Yongpeng Xia
1,
Kexiang Zhang
1 and
Bin Li
1
1
Guangxi Key Laboratory of Information Materials, Guangxi Collaborative Innovation Center for Structure and Properties for New Energy and Materials, School of Material Science and Engineering, Guilin University of Electronic Technology, Guilin 541004, China
2
School of Mechanical & Electrical Engineering, Guilin University of Electronic Technology, Guilin 541004, China
3
School of New Energy Science and Technology, Xi’an Technological University, Xi’an 710021, China
*
Authors to whom correspondence should be addressed.
†
These authors contributed equally to this work.
Nanomaterials 2022, 12(15), 2550; https://doi.org/10.3390/nano12152550
Submission received: 29 June 2022 / Revised: 21 July 2022 / Accepted: 21 July 2022 / Published: 25 July 2022
(This article belongs to the Special Issue Nanostructured Electrodes for High-Performance Supercapacitors and Batteries)
Browse Figures
Versions Notes

Abstract

:
Sodium borohydride (NaBH4), with a high theoretical hydrogen content (10.8 wt%) and safe characteristics, has been widely employed to produce hydrogen based on hydrolysis reactions. In this work, a porous titanium oxide cage (PTOC) has been synthesized by a one-step hydrothermal method using NH2-MIL-125 as the template and L-alanine as the coordination agent. Due to the evenly distributed PtNi alloy particles with more catalytically active sites, and the synergistic effect between the PTOC and PtNi alloy particles, the PtNi/PTOC catalyst presents a high hydrogen generation rate (10,164.3 mL∙min−1∙g−1) and low activation energy (28.7 kJ∙mol−1). Furthermore, the robust porous structure of PTOC effectively suppresses the agglomeration issue; thus, the PtNi/PTOC catalyst retains 87.8% of the initial catalytic activity after eight cycles. These results indicate that the PtNi/PTOC catalyst has broad applications for the hydrolysis of borohydride.

1. Introduction

The overconsumption of traditional fossil fuels has brought in severe energy shortages and environmental pollution issues, such as the greenhouse effect [1]. To solve the above issues, hydrogen energy, as an efficient and sustainable energy, is considered to be a promising alternative to fossil energy [2,3]. The extensive development and use of hydrogen energy is conducive to the pursuit of carbon neutrality and emission peak. Hydrogen produced by the hydrolysis of sodium borohydride (NaBH4) has been regarded as one of the most promising hydrogen production methods due to the advantages of high theoretical hydrogen production density (10.8 wt%), low hydrogen release temperature, controllable reaction process, high hydrogen purity, and environmental friendliness [4]. However, the slow hydrolysis reaction limits the wide use of hydrogen.
In order to accelerate the reaction kinetics of hydrolysis NaBH4, a variety of catalysts such as Co [5,6,7,8], Ni [9,10,11], Rh [12], Pd [13], Ru [14,15], and Pt [16,17] have been comprehensively studied. Although Pt-based catalysts are one of the most active catalysts, the scarce storage and expensive price are the main obstacles to their large-scale application. Therefore, increasing the utilization efficiency of Pt remains the focus of the search. Previous studies have demonstrated that combining Pt with non-noble metals (such as Co [18,19], Ni [20,21,22], and Fe [23,24]) could significantly improve the utilization efficiency of the catalysts. For example, Shumin Han et al. synthesized a carbon nanosphere (CNS)-supported ultrafine bimetallic Pt-Co nanoparticle (CNSs@Pt0.1Co0.9) catalyst for NaBH4 catalysis. The as-prepared CNSs@Pt0.1Co0.9 catalyst exhibited excellent performance in kinetic and thermodynamic tests [25]. Younghun Kim et al. designed a magnetic core and multi-shelled silica/titania-supported bimetallic (Pt/Ni NPs Fe3O4@SiO2@TiO2) catalyst for catalyzing the hydrolysis of NaBH4 [20]. Jong-Sung Yu et al. uniformly deposited PtFe hydroxide by in situ hydrolysis of urea, followed by the preparation of a carbon-supported PtFe catalyst in ethylene glycol, and the catalyst exhibited excellent electrocatalytic performance [24].
Recently, Ni combined with precious metals, such as Pt-Ni and Ru-Ni, have been confirmed to be effective catalysts for hydrogen production from hydrolysis NaBH4 [26,27,28]. However, these catalysts exhibit poor catalytic activity due to the accumulation of metal nanoparticles (NPs) during the reaction. Strategies including structural and morphology control, as well as the addition of suitable carries can effectively inhibit the agglomeration problem [29,30,31]. In addition, the introduction of support material not only is conducive to the distribution of metal NPs but also improves the metal properties through geometric and electronic effects. Anelia Kakanakova-Georgieva et al., employing theoretical calculations, demonstrated that the porous structural material and the synergistic effect between metal NPs with support materials played an important role in the activity of the catalyst [32,33]. Porous hollow structures assembled from nanosheets with large surface areas could provide a unique microenvironment both on the inside and outside through species channels for guest shuttling [34]. Among numerous porous materials, metal-organic frameworks (MOFs) with tunable metal ions and organic ligands are extensively searched in the fields of energy storage and catalysis [35]. Furthermore, they also act as a self-sacrificing template in preparing the porous hollow materials. For example, pioneering studies used the Ti-MOFs as carriers to improve the catalytic performance of metal catalysts for hydrogen production [36,37]. Therefore, reasonably designed porous structural carries for the dispersion of metal NPs enables the achievement of a satisfactory catalytic performance.
Herein, PtNi NPs were confined in a porous titanium oxide cage (PTOC) derived from NH2-MIL-125 (Ti) by a facile hydrothermal method and used for the hydrogen production of hydrolysis NaBH4. The synthesized catalysts exhibit good catalytic activity with a high hydrogen generation rate (10,164.3 mL∙min−1∙g−1) and low activation energy (28.7 kJ∙mol−1). In addition, the robust porous structure of PTOC benefits from the distribution of PtNi alloy particles and suppresses the agglomeration issue; thus, the PtNi/PTOC nanocomposite catalyst retains 87.8% of the initial catalytic activity after eight cycles.

2. Materials and Methods

2.1. Materials

All chemicals were of analytical grade and used without further purification. 2-aminoterephthalic acid, sodium borohydride (NaBH4), and nickel nitrate hexahydrate (Ni(NO3)2·6H2O) with a purity of 99% were purchased from Alfa Aesar Co., Ltd. (Tianjin, China). Chloroplatinic acid hexahydrate (H2PtCl6·6H2O), titanium (IV) isopropoxide, L-alanine, and dimethylformamide (DMF)were purchased from Aladdin Reagent (Shanghai, China). All experiments were performed using DMF and anhydrous CH3OH as solvents.

2.2. Synthesis of NH2-MIL-125

The preparation of NH2-MIL-125 nanocrystals followed a previously reported process [38]. Using DMF and ethanol as organic reaction solvents, 2-aminoterephthalic acid (500 mg, 2.76 mmol) was dissolved in a mixture solvent (10 mL) of 1 mL of CH3OH (1 mL) and DMF (9 mL). Subsequently, 0.76 mmol of titanium isopropoxide was slowly added to the mixture under ultrasound. The solution was then placed in a 25 mL Teflon-lined reactor and heated at 150 °C for 72 h. After, the mixture was cooled to room temperature and the yellow powder was recovered by centrifugation. To remove impurities, the collected powder was washed sequentially with DMF, ethanol, and deionized water and dried at 80 °C for 12 h.

2.3. Synthesis of PTOC

NH2-MIL-125 (10 mg) was sonicated and dispersed in 5 mL of anhydrous ethanol. Next, 47.5 mg of L-alanine was added to the mixture and stirred for 6 h. The solution was then placed in a reaction vessel containing 25 mL of Teflon liner and heated at 176 °C for 36 h. The white precipitate was recovered by centrifugation, washed with ethanol, and dried under vacuum at 80 °C for 12 h.

2.4. Preparation of PtNi/PTOC

Amino acid molecules (generally a class of mild reducing agents) are used to prepare metal NPs. Herein, NH2-MIL-125 (10 mg) was sonicated and dispersed in 5 mL of anhydrous ethanol. Then, L-alanine (47.5 mg) was added into the mixture and stirred for 6 h. H2PtCl6·6H2O (1.0 mg, 2.3 µmol) and Ni(NO3)2·6H2O (3 mg, 10.3 µmol) were added sequentially and stirred for 1 h. Then, the mixture was placed in a 25 mL Teflon pan and heated at 176 °C for 36 h. After centrifugation, the mixture was dried with ethanol at 80 °C for 12 h. For the comparison, Ni(NO3)2·6H2O was not added in the preparation process of Pt/PTOC, and H2PtCl6·6H2O was not added to Ni/PTOC; the other steps were consistent with the preparation process of PtNi/PTOC.

2.5. Characterization

The morphology of the PtNi/PTOC catalyst was analyzed by scanning electron microscopy (SEM, Quanta 200, FEI, Hillsboro, OR, USA) under a vacuum environment and 30 kV AC voltage. The test sample was dispersed on conductive material and stuck on a small sample holder. Excess powder was blown off with gas to avoid contaminating the cavity. The morphology and elemental composition of the catalyst was analyzed using a transmission electron microscope (TEM, JEOL 2010, JEOL, Tokyo, Japan) and dispersive X-ray detector (EDX) with an informal resolution of 0.12 nm and a point resolution of 0.25 nm. The powder was put into an anhydrous ethanol solution, shaken well with ultrasonic waves, and dropped onto the microgrid support film to obtain the sample to be tested. The chemical structure of the catalyst was characterized by Fourier-transform infrared (FT-IR) spectroscopy (Nicolet 6700, Waltham, MA, USA) in the wavenumber range of 400–4000 cm−1. The fine powder of the sample was uniformly dispersed in potassium bromide in the ratio of 1:100 (mcatalyst:mKBr) and the transparent flakes were obtained by the tablet method at the pressure of 5 MPa for 30 s. The crystal structure was analyzed by X-ray diffraction (XRD, 1820, Philips, Amsterdam, The Netherlands), with a scan angle from 5° to 90°, a step size set to 0.02, a working voltage of 40 kV, and a working current of 40 mA. The sample preparation was carried out as follows: the powder sample was evenly distributed in the sample holder and compacted with the glass plate. The sample surface was required to be smooth and flush with the glass surface. The nitrogen-desorption isotherms of the PtNi/PTOC catalysts were investigated using a QuantachromeAutosorb-iQ2 adsorber. The specific surface area of PtNi/PTOC catalyst was determined using a fully automated ratio meter and porosity analyzer. The samples were degassed in a glass tube at 150 °C for 10 h and then analyzed in liquid nitrogen. The pore size of a pore of the PtNi/PTOC catalyst was determined by the BJH method. X-ray photoelectron spectroscopy (XPS; Thermo Electron ESCALAB 250, Waltham, MA, USA), was mainly used qualitatively and semi-quantitatively through the analysis of catalysts, the valence state, species class, and surface content. The sample was pressed on aluminum foil, the excitation light source was Al Kα (hv= 1486.6 eV), and the final XPS was calibrated by C 1s (284.8 eV).

2.6. Hydrogen Production Testing

The catalytic hydrogen generation experiments were measured on a self-built hydrogen generation device [39]. The volume of hydrogen produced was determined by the equivalent displacement of water. First, 0.1 g of catalyst was added in a 125 mL conical flask. Next, 10 mL of the solution containing 1.5 wt% NaBH4 and 5 wt% NaOH was injected into the conical flask. The produced gas was collected in a container filled with water after flowing through a condenser and dryer to remove water vapor. The volume of produced H2 was measured by the water displacement method. The water was displaced into a 1 L flask through a tube connected with a gas-gathering container and weighted by an electronic balance (UX2200H, Shimadzu Corporation, Kyoto, Japan). A computer connected to the electronic balance was used to record water quality automatically. The hydrogen released per gram of catalyst per unit time (HGR) was calculated through the display on the computer. After one hydrolysis test was completed, the catalyst was immediately washed and dried for 12 h. Subsequently, a fresh 10 mL of the 1.5 wt% NaBH4 and 5 wt% NaOH solution was added to repeat the above measurements.
The hydrogen generation rate (HGR) was calculated according to the following equation:
H G R = V H 2 0 ( mL ) t ( min ) × m ( g )
where V H 2 0 is the volume of drained water, m is the total mass of the catalyst, and t is the total reaction time in minutes [40].

3. Results and Discussion

3.1. Catalyst Characterization

In this paper, PtNi/PTOC was synthesized by a simple hydrothermal method and wet-reduction method. Figure 1 shows a schematic diagram of the preparation of PtNi/PTOC (PTOC). First, a round cake of NH2-MIL-125 (Ti) was obtained using 2-aminoterephthalic acid as organic ligands and titanium (IV) isopropoxide as a metal precursor. Then, PTOC with a porous hollow structure was formed into an alcoholic thermal process at 176 °C under auxiliary amino acid molecules L-alanine. Lastly, PtNi precursors were reduced to Pt3Ni NPs by the L-alanine. The formation of PTOC involved the Kirkendall effect of Ti ion dissolution and recrystallization. The Ti(iv) ions were firstly dissolved from NH2-MIL-125(Ti) nanocrystals by coordination of Ti(iv) with amino acids (l-alanine), leading to the formation of sheet-like titanium oxide NPs on the NH2-MIL-125(Ti) nanocrystals. With this continuous transformation, successive shells of titanium oxides were generated and transferred into the completed porous cages.
The morphology of NH2-MIL-125 and PTOC were characterized by SEM; as can be seen in Figure 2a,b, the NH2-MIL-125 exhibits a round cake with a smooth surface, and the size is around 300–500 nm. After the auxiliary of the amino acid molecule L-alanine under hydrothermal circumstances, the cage structure of PTOC remains, with multi-channel interlacing on the surface (Figure 2c,d). Due to the alcoholization of NH2-MIL-125, the nanosheets were assembled into a cage structure. L-alanine is commonly used as a mild reducing agent for the preparation of metal NPs [41,42]. After the hydrothermal reaction, PtNi precursors were reduced to Pt3Ni NPs and confined in PTOC. As shown in Figure 2e,f, compared with the PTOC sample, Pt-Ni/PTOC still retained the unique “nanocage” structure.
As shown in Figure 3, HRTEM analysis showed that PtNi NPs were uniformly distributed in the PTOC nanocages with average particle sizes of 1.68 nm (Figure 3b). Further, high-resolution HRTEM analysis revealed that the d-spacing of 0.223 nm is between the (111) crystal faces of Pt (0.227 nm) and Ni (0.204 nm), indicating the formation of PtNi alloy NPs (Figure 3c) [43]. The HAADF-STEM image also confirmed the formation of uniformly distributed PtNi NPs (Figure 3d). EDX analysis showed that the as-prepared nanocomposites consisted of Ti, N, Pt, and Ni (Figure 3e–h). These results indicate that the 3D structure of PtNi NPs encapsulated by PTOC nanocages have been successfully prepared.
FT-IR measurements (Figure 4a) were carried out to detect the functional groups of the as-prepared catalysts. The experimental results showed that all the prepared catalysts contained benzene rings and amino groups (the characteristic peaks at 3428 cm−1 and 1630 cm−1). The existence of amino groups stably binds the metal NPs due to the strong chelation/complexation effect between the metal and amine groups [44]. Therefore, our results indicate that PTOC precursors are beneficial for the distribution of metal NPs. The XRD spectrum (Figure 4b) had four peaks at 2θ = 25°, 48°, 55°, and 62°, which corresponded to the (101), (200), (211), and (213) crystal planes of anatase TiO2 (PDF, No. 21-1272). The diffraction peaks of layered titanate H2Ti8O17 also appeared (PDF No. 36-0656), indicating that the PTOC had a two-component titanium oxide porous cage. In addition, the reflected signals of the Pt/PTOC and Ni/PTOC samples matched well with metallic Pt (PDF No. 87-0647) and Ni (PDF No. 65-0380), respectively. The diffraction peaks of PtNi alloy laid between the corresponding characteristic peaks of Pt and Ni, which further reflected the well-alloyed PtNi nanoparticles [45].
The surface interactions and electronic state of PtNi/PTOC were investigated using XPS. Figure 5a shows the whole XPS pattern of PtNi/PTOC. The signals generated by the PTOC corresponded to C 1s, N 1s, O 1s, Ti 2p, Pt 4f, and Ni 2p. The narrow range spectra of Ti 2p is depicted in Figure 5b, which also proves the presence of PTOC. In Figure 5c, it can be seen that the Pt 4f region of core level binding energies is deconvoluted into two sets of spin-orbit doublet peaks. The Pt 4f spectrum exhibited two peaks at 71.4 and 74.7 eV and were assigned to Pt 4f7/2 and Pt 4f5/2, respectively, suggesting the presence of Pt0. Two peaks at 71.9 and 75.3 eV corresponded to the satellite peaks of Pt. The binding energy located at 855.6 and 873.4 eV belonged to the Ni 2p3/2, and Ni 2p1/2, respectively. The binding energies at 861.38, 868.92, and 873.4 eV corresponded to the satellite peaks. In addition, the binding energy around 852.05 eV is attributed to the Ni0 peak, which confirmed the existence of metallic Ni in PtNi/PTOC (Figure 5d). The strong interaction between Pt and Ni within the catalyst may lead to an increased oxidation resistance, which is beneficial to the catalysis activity and durability [46].
As shown in Figure 6a, PtNi/PTOC exhibited a typical IV-type isotherm with obvious hysteresis loops with a high specific surface area of approximately 206.2 m2·g−1. In addition, PTOC showed that similar isotherms with the specific surface area decreased from 206.2 m2·g−1 to 145.8 m2·g−1, which is due to the addition of PtNi NPs. From the IV-type isotherms with obvious hysteresis loops, the main pore size distribution of two materials is mesopores. Pore-size distribution curves showed that the size of the pore in PtNi/PTOC ranged from 3.5 nm to 10.0 nm (Figure 6b). The rich mesopores are conducive to the penetration of the electrolyte and the transport of electrons, thereby enhancing the catalytic activity of the material.

3.2. Effect of Different Types of Catalysts

The effect of different catalysts on the hydrolysis of NaBH4 under alkaline conditions was investigated. As shown in Figure 7, PtNi/PTOC exhibited optimal performance with hydrogen release rate (HGR) of 10,164.3 mL·min−1 at 25 °C, which is higher than Pt/PTOC and Ni/PTOC. Compared to most of the previously reported results, PtNi/PTOC also exhibited a good catalytic activity (Table 1) [25,47,48,49,50,51,52]. According to Figure 7b, the magnitude of the catalytic performance was PtNi/PTOC > Pt/PTOC > Ni/PTOC, while PTOC and NH2-MIL-125 had no catalytic activity. The experimental results show that the synergistic effect between Pt and Ni enhanced the catalytic activity more than the single Pt or Ni-based catalyst, thereby promoting the rapid release of hydrogen from NaBH4. Furthermore, the evenly distributed PtNi alloy particles with more catalytically active sites simultaneously enhanced the hydrolysis activity.
In order to measure the activation energy (Ea) of the hydrolysis reaction, hydrolysis tests were carried out using different temperatures with the other parameters unchanged, controlling the reaction temperature from 15 to 55 °C (Figure 8a) with a gradient of 10 °C. As expected, all of the tests reached the theoretical hydrogen quantity, and the hydrogen release rate increased with the increase in reaction temperature, which belongs to the first-order reaction [53,54,55]. According to the Arrhenius slope calculation, the activation energy of Pt-Ni/PTOC is 28.7 kJ∙mol−1 (Figure 8b), which was lower than most of the catalysts that have been reported (Table 1). The synergistic effect between PtNi NPs and PTOC may be the main factor for the decrease in the Ea value. The small particle size of the PtNi NPs is well supported on the pores of PTOC, thus avoiding excessive losses and agglomeration during hydrolysis. Moreover, the porous hollow structure promotes the interaction mass transfer between the catalyst and NaBH4 in the pores. Therefore, these results show that PtNi/PTOC has good kinetic properties for catalyzing NaBH4 hydrogen release.

3.3. Stability of PtNi/PTOC

The stability of the catalyst is a key index to the actual application of hydrogen generation from NaBH4 hydrolysis. Figure 9 shows that the PtNi/PTOC catalyst was tested eight times under conventional conditions (25 °C). The catalytic activity of the hydrogen evolution of NaBH4 decreased slightly and maintained the initial catalytic activity of 87.8% after eight cycles. The excellent cycling performance may be related to the hollow porous structure of PTOC, not only providing a large surface area for the distribution of PtNi alloy particles but also suppressing the agglomeration issues.
To verify the structural stability of the PtNi/PTOC catalyst, TEM (Figure 10a) and XRD characterizations were carried out after the cyclability test (Figure 10b). The TEM images of PtNi/PTOC after cycle tests show that the material maintained the nanocage structure with numerous sheets, indicating the stable structural integrity of the catalyst. In addition, compared to the original PtNi/PTOC sample, there was no significant agglomeration, which is favorable for the catalytic reaction. The XRD spectra of the obtained products showed that two XRD spectra were well-matched, and the peak of the catalyst became sharp after cycle tests, indicating the increased crystallinity of the catalyst. According to the Scherrer formula, (D = Kλ/βCosθ), the size of PtNi/PTOC catalyst increased from 1.68 to 2.32 nm after eight cycle tests, which was one of the reasons for the decay of catalytic activity. The stable structure and high catalytic activity of metal NPs are promising for the hydrolysis of borohydride.

4. Conclusions

In this work, ultra-small PtNi NPs were confined in a porous titanium oxide cage (PTOC) derived from NH2-MIL-125 (Ti) by a facile hydrothermal method and used for the hydrogen production of hydrolysis NaBH4. At a room temperature of 25 °C, the hydrogen production rate of PtNi/PTOC reached 10,164.3 mL·min−1·gM−1, and the activation energy was 28.7 kJ∙mol−1. After eight cycles of testing, 87.8% of the initial test performance was maintained. Such excellent performance can be attributed to the following: (i) The porous and hollow structure of PTOC creates a unique microenvironment between its interior and exterior, which provides more reaction channels. (ii) PTOC with a high surface area enables the even distribution of PtNi alloy particles, thus exhibiting a large number of active sites. (iii) The synergistic effect between PTOC and PtNi alloy particles can improve the reactivity. (iv) The robust porous structure maintains the integrity of the catalyst and suppresses the aggregation of nanoparticles. The catalyst has the advantages of a simple operation and economic efficiency and shows promise for producing hydrogen for fuel-cell vehicles.

Author Contributions

Conceptualization, Y.Y. and L.K.; methodology, Y.Y. and L.K.; software, Y.Y., L.K., Z.S. and C.Z.; validation, Y.Y. and L.K.; formal analysis, C.Z., L.S. and F.X.; investigation, Y.Y., L.K., L.S. and F.X.; resources, L.S. and F.X.; data curation, Y.Y., L.K., Z.S. X.J., Q.S., Y.B., D.C., Y.X., K.Z. and B.L.; writing—original draft preparation, Y.Y., L.K. and C.Z; writing—review and editing, L.S., F.X. and H.P.; visualization, Y.Y. and L.K.; supervision, L.S., F.X. and H.P; project administration, L.S. and F.X.; funding acquisition, L.S. and F.X. All authors have read and agreed to the published version of the manuscript.

Funding

This work was supported by the National Key Research and Development Program of China (2018YFB1502103 and 2018YFB1502105), the National Natural Science Foundation of China (51971068, U20A20237 and 51871065), the Scientific Research and Technology Development Program of Guangxi (AA19182014, AD17195073 and AA17202030-1), Guangxi Bagui Scholar Foundation, Guangxi Collaborative Innovation Centre of Structure and Property for New Energy and Materials, Guangxi Advanced Functional Materials Foundation and Application Talents Small Highlands, Chinesisch-Deutsche Kooperationsgruppe (GZ1528), Science research and Technology Development project of Guilin (20210216-1) and Science Research and Technology Development Project of Guilin (20210102-4).

Institutional Review Board Statement

Not applicable.

Informed Consent Statement

Not applicable.

Data Availability Statement

Not applicable.

Conflicts of Interest

The authors declare no conflict of interest.

References

  1. Chen, M.; Xiao, X.; Wang, X.; Lu, Y.; Zhang, M.; Zheng, J.; Chen, L. Self-templated carbon enhancing catalytic effect of ZrO2 nanoparticles on the excellent dehydrogenation kinetics of MgH2. Carbon 2020, 166, 46–55. [Google Scholar] [CrossRef]
  2. Zhang, M.; Xiao, X.; Luo, B.; Liu, M.; Chen, M.; Chen, L. Superior de/hydrogenation performances of MgH2 catalyzed by 3D flower-like TiO2@C nanostructures. J. Energy Chem. 2020, 46, 191–198. [Google Scholar] [CrossRef]
  3. Chen, W.; Xiao, X.; He, J.; Dong, Z.; Wang, X.; Chen, M.; Chen, L. A dandelion-like amorphous composite catalyst with outstanding performance for sodium borohydride hydrogen generation. Int. J. Hydrogen Energy 2021, 46, 10809–10818. [Google Scholar] [CrossRef]
  4. Zhu, Y.; Ouyang, L.; Zhong, H.; Liu, J.; Wang, H.; Shao, H.; Huang, Z.; Zhu, M. Closing the Loop for Hydrogen Storage: Facile Regeneration of NaBH4 from its Hydrolytic Product. Angew. Chem. Int. Ed. 2020, 59, 8623–8629. [Google Scholar] [CrossRef]
  5. Huang, Y.; An, C.; Zhang, Q.; Zang, L.; Shao, H.; Liu, Y.; Yuan, H.; Wang, C.; Wang, Y. Cos-effective mechanochemical synthesis of highly dispersed supported transition metal catalysts for hydrogen storage. Nano Energy 2021, 80, 105535. [Google Scholar] [CrossRef]
  6. Min, J.; Jeffery, A.; Kim, Y.; Jung, N. Electrochemical Analysis for Demonstrating CO Tolerance of Catalysts in Polymer Electrolyte Membrane Fuel Cells. Nanomaterials 2019, 9, 1425. [Google Scholar] [CrossRef] [PubMed] [Green Version]
  7. Bu, Y.; Liu, J.; Chu, H.; Wei, S.; Yin, Q.; Kang, L.; Luo, X.; Sun, L.; Xu, F.; Huang, P.; et al. Catalytic Hydrogen Evolution of NaBH4 Hydrolysis by Cobalt Nanoparticles Supported on Bagasse-Derived Porous Carbon. Nanomaterials 2021, 11, 3259. [Google Scholar] [CrossRef]
  8. Ren, Y.; Wang, J.; Hu, W.; Wen, H.; Qiu, Y.; Tang, P.; Chen, M.; Wang, P. Hierarchical Nanostructured Co-Mo-B/CoMoO4−x Amorphous Composite for the Alkaline Hydrogen Evolution Reaction. ACS Appl. Mater. Interfaces 2021, 13, 42605–42612. [Google Scholar] [CrossRef]
  9. Shao, H.; Huang, G.; Liu, Y.; Guo, Y.; Wang, Y.N. Thermally stable Ni MOF catalyzed MgH2 for hydrogen storage. Int. J. Hydrogen Energy 2021, 46, 37977–37985. [Google Scholar] [CrossRef]
  10. Gao, H.; Shao, Y.; Shi, R.; Liu, Y.; Zhu, J.; Liu, J.; Zhu, Y.; Zhang, J.; Li, L.; Hu, X. Effect of Few-Layer Ti3C2Tx Supported Nano-Ni via Self-Assembly Reduction on Hydrogen Storage Performance of MgH2. ACS Appl. Mater. Interfaces 2020, 12, 47684–47694. [Google Scholar] [CrossRef]
  11. Liu, W.; Zhi, H.; Yu, X. Recent progress in phosphorus based anode materials for lithium/sodium ion batteries. Energy Storage Mater. 2019, 16, 290–322. [Google Scholar] [CrossRef]
  12. Larichev, Y.V.; Netskina, O.V.; Komova, O.V.; Simagina, V.I. Comparative XPS study of Rh/Al2O3 and Rh/TiO2 as catalysts for NaBH4 hydrolysis. Int. J. Hydrogen Energy 2010, 35, 6501–6507. [Google Scholar] [CrossRef]
  13. Liu, S.; Chen, X.; Wu, Z.J.; Zheng, X.C.; Peng, Z.K.; Liu, P. Chitosan-reduced graphene oxide hybrids encapsulated Pd (0) nanocatalysts for H2 generation from ammonia borane. Int. J. Hydrogen Energy 2019, 44, 23610–23619. [Google Scholar] [CrossRef]
  14. Konuş, N.; Karataş, Y.; Gulcan, M. In situ formed ruthenium (0) nanoparticles supported on TiO2 catalyzed hydrogen generation from aqueous ammonia-borane solution at room temperature under air. Synth. React. Inorg. Met. Org. Chem. 2016, 46, 534–542. [Google Scholar] [CrossRef]
  15. Zhang, J.; Lin, F.; Yang, L.; He, Z.; Huang, X.; Zhang, D.; Dong, H. Ultrasmall Ru nanoparticles supported on chitin nanofibers for hydrogen production from NaBH4 hydrolysis. Chin. Chem. Lett. 2020, 31, 2019–2022. [Google Scholar] [CrossRef]
  16. Dai, P.; Zhao, X.; Xu, D.; Wang, C.; Tao, X.; Liu, X.; Gao, J. Preparation, characterization, and properties of Pt/Al2O3/cordierite monolith catalyst for hydrogen generation from hydrolysis of sodium borohydride in a flow reactor. Int. J. Hydrogen Energy 2019, 44, 28463–28470. [Google Scholar] [CrossRef]
  17. Ro, G.; Kim, Y. H2 generation using Pt nanoparticles encapsulated in Fe3O4@SiO2@TiO2 multishell particles. Colloids Surf. A 2019, 577, 48–52. [Google Scholar] [CrossRef]
  18. Chen, J.; Gu, Y.; Kong, D.; Xiang, S.; Wang, P.; Zhang, H.; Zhang, S. Preparation of Colloidal Pt/Co Bimetallic Nanoparticle Catalysts and Their Catalytic Activity for Hydrogen Generation from Hydrolysis Reaction of NaBH4. Rare Met. Mater. Eng. 2014, 43, 2209–2214. [Google Scholar]
  19. Kotkondawar, A.V.; Rayalu, S. Enhanced H2 production from dehydrogenation of sodium borohydride over the ternary Co0.97Pt0.03/CeOx nanocomposite grown on CGO catalytic support. RSC Adv. 2020, 10, 38184–38195. [Google Scholar] [CrossRef]
  20. Ro, G.; Hwang, D.K.; Kim, Y. Hydrogen generation using Pt/Ni bimetallic nanoparticles supported on Fe3O4@SiO2@TiO2 multi-shell microspheres. J. Ind. Eng. Chem. 2019, 79, 364–369. [Google Scholar] [CrossRef]
  21. Guo, H.; Chen, C.; Chen, K.; Cai, H.; Chang, X.; Liu, S.; Wang, C. High performance carbon-coated hollow Ni12P5 nanocrystals decorated on GNS as advanced anodes for lithium and sodium storage. J. Mater. Chem. A 2017, 5, 22316–22324. [Google Scholar] [CrossRef]
  22. Aranishi, K.; Singh, A.K.; Xu, Q. Dendrimer-Encapsulated Bimetallic Pt-Ni Nanoparticles as Highly Efficient Catalysts for Hydrogen Generation from Chemical Hydrogen Storage Materials. Chem. Cat. Chem. 2013, 5, 2248–2252. [Google Scholar] [CrossRef]
  23. Li, W.; Zhao, W.; Zhou, W.; Zhou, X.; Sun, L.; Zhang, H.; Lu, L.; Zhang, S. Fabrication and catalytic activity of Pt/Ni/Fe trimetallic nanoparticles for hydrogen generation from NaBH4. Chem. J. Chin. Univ. Chin. 2014, 35, 2164–2169. [Google Scholar]
  24. Yang, D.S.; Kim, M.S.; Song, M.Y.; Yu, J.S. Highly efficient supported PtFe cathode electrocatalysts prepared by homogeneous deposition for proton exchange membrane fuel cell. Int. J. Hydrogen Energy 2012, 37, 13681–13688. [Google Scholar] [CrossRef]
  25. Zhang, H.; Zhang, L.; Rodríguez-Pérez, I.A.; Miao, W.; Chen, K.; Wang, W.; Han, S. Carbon nanospheres supported bimetallic Pt-Co as an efficient catalyst for NaBH4 hydrolysis. Appl. Surf. Sci. 2021, 540, 14829. [Google Scholar] [CrossRef]
  26. Qi, X.; Li, X.; Chen, B.; Lu, H.; Wang, L.; He, G. Highly active nanoreactors: Patchlike or thick Ni coating on Pt nanoparticles based on confined catalysis. ACS Appl. Mat. Interfaces 2016, 8, 1922–1928. [Google Scholar] [CrossRef] [PubMed]
  27. Ghosh, S.K.; Mandal, M.; Kundu, S.; Nath, S.; Pal, T. Bimetallic Pt-Ni nanoparticles can catalyze reduction of aromatic nitro compounds by sodium borohydride in aqueous solution. Appl. Catal. A Gen. 2004, 268, 61–66. [Google Scholar] [CrossRef]
  28. Hannauer, J.; Demirci, U.B.; Geantet, C.; Herrmann, J.M.; Miele, P. Transition metal-catalyzed dehydrogenation of hydrazine borane N2H4BH3 via the hydrolysis of BH3 and the decomposition of N2H4. Int. J. Hydrogen Energy 2012, 37, 10758–10767. [Google Scholar] [CrossRef]
  29. Zhang, H.; Feng, X.; Cheng, L.; Hou, X.; Li, Y.; Han, S. Non-noble Co anchored on nanoporous graphene oxide, as an efficient and long-life catalyst for hydrogen generation from sodium borohydride. Colloids Surf. A 2019, 563, 112–119. [Google Scholar] [CrossRef]
  30. Xia, G.; Zhang, L.; Fang, F.; Sun, D.; Guo, Z.; Liu, H.; Yu, X. General synthesis of transition metal oxide ultrafine nanoparticles embedded in hierarchically porous carbon nanofibers as advanced electrodes for lithium storage. Adv. Funct. Mater. 2016, 26, 6188–6196. [Google Scholar] [CrossRef] [Green Version]
  31. Song, Q.; Wang, W.D.; Hu, X.; Dong, Z. Ru nanoclusters confined in porous organic cages for catalytic hydrolysis of ammonia borane and tandem hydrogenation reaction. Nanoscale 2019, 11, 21513–21521. [Google Scholar] [CrossRef] [PubMed]
  32. Kakanakova-Georgieva, A.; Gueorguiev, G.; Sangiovanni, D.; Suwannaharn, N.; Ivanov, I.; Cora, I.; Pécz, B.; Nicotra, G.; Giannazzo, F. Nanoscale phenomena ruling deposition and intercalation of AlN at the graphene/SiC interface. Nanoscale 2020, 12, 19470–19476. [Google Scholar] [CrossRef] [PubMed]
  33. Freitas, R.; Brito Mota, F.; Castilho, C.; Kakanakova-Georgieva, A.; Gueorguiev, G. Spin-orbit-induced gap modification in buckled honeycomb XBi and XBi3 (X = B, Al, Ga, and In) sheets. J. Phys.-Condens. Matter 2015, 27, 485306. [Google Scholar] [CrossRef] [Green Version]
  34. Chen, Y.; Shi, J. Chemistry of mesoporous organosilica in nanotechnology: Molecularly organic-inorganic hybridization into frameworks. Adv. Mater. 2016, 28, 3235–3272. [Google Scholar] [CrossRef] [PubMed]
  35. Li, Y.; Xie, L.; Li, Y.; Zheng, J.; Li, X. Metal-Organic-Framework-Based Catalyst for Highly Efficient H2 Generation from Aqueous NH3BH3 Solution. Chem. Eur. J. 2009, 15, 8951–8954. [Google Scholar] [CrossRef]
  36. Yan, Y.; Li, C.; Wu, Y.; Gao, J.; Zhang, Q. From isolated Ti-oxo clusters to infinite Ti-oxo chains and sheets: Recent advances in photoactive Ti-based MOFs. J. Mater. Chem. A 2020, 8, 15245–15270. [Google Scholar] [CrossRef]
  37. Karthik, P.; Shaheer, A.M.; Vinu, A.; Neppolian, B. Amine Functionalized Metal-Organic Framework Coordinated with Transition Metal Ions: D-d Transition Enhanced Optical Absorption and Role of Transition Metal Sites on Solar Light Driven H2 Production. Small 2020, 16, 1902990. [Google Scholar] [CrossRef] [PubMed]
  38. Gu, Z.; Chen, L.; Wang, H.; Guo, Y.; Xu, M.; Zhang, Y.; Duan, C. Light control of charge transfer in metal/semiconductor heterostructures for efficient hydrogen evolution: Optical transition versus SPR. Int. J. Hydrogen Energy 2017, 42, 26713–26722. [Google Scholar] [CrossRef]
  39. Xu, F.; Zhang, X.; Sun, L.; Yu, F.; Li, P.; Chen, J.; Wu, Y.; Cao, L.; Xu, C.; Yang, X.; et al. Hydrogen generation of a novel Al-NaMgH3 composite reaction with water. Int. J. Hydrogen Energy 2017, 42, 30535–30542. [Google Scholar] [CrossRef]
  40. Yang, F.; Zou, Y.; Xiang, C.; Xu, F.; Sun, L. Synthesis of “needle-cluster” NiCo2O4 carbon nanofibers and loading of Co-B nanoparticles for hydrogen production through the hydrolysis of NaBH4. J. Alloys Compd. 2022, 911, 165069. [Google Scholar] [CrossRef]
  41. Zhou, H.; Kang, M.; Xie, B.; Wen, P.; Zhao, N. L-Alanine mediated controllable synthesis: Ultrathin Co3O4 nanosheets@ Ni foam for high performance supercapacitors. J. Alloys Compd. 2021, 874, 160030. [Google Scholar] [CrossRef]
  42. Shen, Y.; Zhu, C.; Chen, B.; Chen, J.; Fang, Q.; Wang, J. Novel photocatalytic performance of nanocage-like MIL-125-NH2 induced by adsorption of phenolic pollutants. Environ. Sci. Nano 2020, 7, 1525–1538. [Google Scholar] [CrossRef]
  43. Wang, W.; Hong, X.; Yao, Q.; Lu, Z.H. Bimetallic Ni-Pt nanoparticles immobilized on mesoporous N-doped carbon as a highly efficient catalyst for complete hydrogen evolution from hydrazine borane. J. Mater. Chem. A 2020, 8, 13694–13701. [Google Scholar] [CrossRef]
  44. Georgieva, J.; Valova, E.; Mintsouli, I.; Sotiropoulos, S.; Tatchev, D.; Armyanov, S.; Malet, L. Pt (Ni) electrocatalysts for methanol oxidation prepared by galvanic replacement on TiO2 and TiO2-C powder supports. J. Electroanal. Chem. 2015, 754, 65–74. [Google Scholar] [CrossRef]
  45. Liu, Y.; Chen, H.; Tian, C.; Geng, D.; Wang, D.; Bai, S. One-Pot Synthesis of Highly Efficient Carbon-Supported Polyhedral Pt3Ni Alloy Nanoparticles for Oxygen Reduction Reaction. Electrocatalysis 2019, 10, 613–620. [Google Scholar] [CrossRef]
  46. Li, M.; Zhu, Y.; Song, N.; Wang, C.; Lu, X. Fabrication of Pt nanoparticles on nitrogen-doped carbon/Ni nanofibers for improved hydrogen evolution activity. J. Colloid Interface Sci. 2018, 514, 199–207. [Google Scholar] [CrossRef]
  47. Huff, C.; Quach, Q.; Long, J.M.; Abdel-Fattah, T.M. Nanocomposite catalyst derived from ultrafine platinum nanoparticles and carbon nanotubes for hydrogen generation. ECS. J. Solid State Technol. 2020, 9, 101008. [Google Scholar] [CrossRef]
  48. Wu, C.; Zhang, J.; Guo, J.; Sun, L.; Ming, J.; Dong, H.; Yang, X. Ceria-induced strategy to tailor Pt atomic clusters on cobalt–nickel oxide and the synergetic effect for superior hydrogen generation. ACS. Sustain. Chem. Eng. 2018, 6, 7451–7457. [Google Scholar] [CrossRef]
  49. Lu, L.; Shu, H.; Ruan, Z.; Ni, J.; Zhang, H. Preparation of Graphene-supported Pt-Pd Catalyst and Its Catalytic Activity and Mechanism for Hydrogen Generation Reaction. Chem. J. Chin. Univ. Chi. 2018, 39, 949–955. [Google Scholar]
  50. Lale, A.; Wasan, A.; Kumar, R.; Miele, P.; Demirci, U.B.; Bernard, S. Organosilicon polymer-derived mesoporous 3D silicon carbide, carbonitride and nitride structures as platinum supports for hydrogen generation by hydrolysis of sodium borohydride. Int. J. Hydrogen Energy 2016, 41, 15477–15488. [Google Scholar] [CrossRef]
  51. Li, K.; Ma, M.; Xie, L.; Yao, Y.; Kong, R.; Du, G.; Sun, X. Monolithically integrated NiCoP nanosheet array on Ti mesh: An efficient and reusable catalyst in NaBH4 alkaline media toward on-demand hydrogen generation. Int. J. Hydrogen Energy 2017, 42, 19028–19034. [Google Scholar] [CrossRef]
  52. Li, X.; Zeng, C.; Fan, G. Ultrafast hydrogen generation from the hydrolysis of ammonia borane catalyzed by highly efficient bimetallic RuNi nanoparticles stabilized on Ti3C2X2 (X = OH and/or F). Int. J. Hydrogen Energy 2015, 40, 3883–3891. [Google Scholar] [CrossRef]
  53. Pornea, A.M.; Abebe, M.W.; Kim, H. Ternary NiCoP urchin like 3D nanostructure supported on nickel foam as a catalyst for hydrogen generation of alkaline NaBH4. Chem. Phys. 2019, 516, 152–159. [Google Scholar] [CrossRef]
  54. Wang, Y.; Li, G.; Wu, S.; Wei, Y.; Meng, W.; Xie, Y.; Zhang, X. Hydrogen generation from alkaline NaBH4 solution using nanostructured Co-Ni-P catalysts. Int. J. Hydrogen Energy 2017, 42, 16529–16537. [Google Scholar] [CrossRef]
  55. Zhou, Y.; Fang, C.; Fang, Y.; Zhu, F.; Liu, H.; Ge, H. Hydrogen generation mechanism of BH4− spontaneous hydrolysis: A sight from ab initio calculation. Int. J. Hydrogen Energy 2016, 41, 22668–22676. [Google Scholar] [CrossRef]
Nanomaterials 12 02550 g001 550
Figure 1. The illustration of the synthetic route of PtNi/PTOC.
Figure 1. The illustration of the synthetic route of PtNi/PTOC.
Nanomaterials 12 02550 g001
Nanomaterials 12 02550 g002 550
Figure 2. SEM images of (a,b) NH2-MIL-125; (c,d) PTOC and (e,f) PtNi/PTOC catalyst.
Figure 2. SEM images of (a,b) NH2-MIL-125; (c,d) PTOC and (e,f) PtNi/PTOC catalyst.
Nanomaterials 12 02550 g002
Nanomaterials 12 02550 g003 550
Figure 3. TEM images of (a,b) PtNi/PTOC catalyst; (c) HRTEM; (d) HADDF-STEM (e–h); EDX images of PtNi/PTOC.
Figure 3. TEM images of (a,b) PtNi/PTOC catalyst; (c) HRTEM; (d) HADDF-STEM (e–h); EDX images of PtNi/PTOC.
Nanomaterials 12 02550 g003
Nanomaterials 12 02550 g004 550
Figure 4. (a) FTIR spectra of catalysts. (b) XRD patterns of catalysts.
Figure 4. (a) FTIR spectra of catalysts. (b) XRD patterns of catalysts.
Nanomaterials 12 02550 g004
Nanomaterials 12 02550 g005 550
Figure 5. X-ray photoelectron spectra of Pt-Ni/PTOC catalyst (a) full spectrum; (b) Ti 2p; (c) Pt 4f; (d) Ni 2p.
Figure 5. X-ray photoelectron spectra of Pt-Ni/PTOC catalyst (a) full spectrum; (b) Ti 2p; (c) Pt 4f; (d) Ni 2p.
Nanomaterials 12 02550 g005
Nanomaterials 12 02550 g006 550
Figure 6. N2 desorption/adsorption isotherm (a) and pore-size distributions (b) for PTOC and PtNi/PTOC.
Figure 6. N2 desorption/adsorption isotherm (a) and pore-size distributions (b) for PTOC and PtNi/PTOC.
Nanomaterials 12 02550 g006
Nanomaterials 12 02550 g007 550
Figure 7. Hydrogen volume versus time (a) and HG rate bar chart of NH2-MIL-125, PTOC, Pt/PTOC, Ni/PTOC, and (b) PtNi/PTOC (reaction conditions: batch system, 25 °C, 1.5 wt% NaBH4 + 5 wt% NaOH, 0.1 g catalyst).
Figure 7. Hydrogen volume versus time (a) and HG rate bar chart of NH2-MIL-125, PTOC, Pt/PTOC, Ni/PTOC, and (b) PtNi/PTOC (reaction conditions: batch system, 25 °C, 1.5 wt% NaBH4 + 5 wt% NaOH, 0.1 g catalyst).
Nanomaterials 12 02550 g007
Nanomaterials 12 02550 g008 550
Figure 8. (a) Hydrogen generation kinetics curves and (b) Arrhenius plot obtained using 1.5 wt% NaBH4 and 1.0 wt% NaOH solution and employing PtNi/PTOC as a catalyst at different solution temperatures.
Figure 8. (a) Hydrogen generation kinetics curves and (b) Arrhenius plot obtained using 1.5 wt% NaBH4 and 1.0 wt% NaOH solution and employing PtNi/PTOC as a catalyst at different solution temperatures.
Nanomaterials 12 02550 g008
Nanomaterials 12 02550 g009 550
Figure 9. (a) Reusability of PtNi/PTOC with 0.1 g catalyst and 1.5 wt% NaBH4 + 5 wt% NaOH solution at 25 °C; (b) HG rate bar chart of catalyst used 8 times.
Figure 9. (a) Reusability of PtNi/PTOC with 0.1 g catalyst and 1.5 wt% NaBH4 + 5 wt% NaOH solution at 25 °C; (b) HG rate bar chart of catalyst used 8 times.
Nanomaterials 12 02550 g009
Nanomaterials 12 02550 g010 550
Figure 10. (a) TEM images of the PtNi/PTOC catalyst after 8 cycles; (b) XRD patterns of the PtNi/PTOC catalyst before cycling and after 8 cycles.
Figure 10. (a) TEM images of the PtNi/PTOC catalyst after 8 cycles; (b) XRD patterns of the PtNi/PTOC catalyst before cycling and after 8 cycles.
Nanomaterials 12 02550 g010
Table
Table 1. Comparison of catalyst systems, reaction temperatures, HGR, Ea values, and number of cycles for NaBH4 hydrolysis catalyzed by various catalysts.
Table 1. Comparison of catalyst systems, reaction temperatures, HGR, Ea values, and number of cycles for NaBH4 hydrolysis catalyzed by various catalysts.
SampleTempera-ture (°C)HG Rate
(mL·min−1·gM−1)		Ea
(kJ·mol–1)		Number of CyclesCyclic StabilityRef.
CNSs@Pt0.1Co0.9308943.038.0585.2%[25]
Pt/MWCNTs3016.946.2580.0%[47]
Pt/CeO2-Co7Ni2Ox257834.847.4585.0%[48]
PtPd/GO253940.029.4460.0%[49]
Pt/Si3N48013,000.035.2582.5%[50]
NiCoP NA/Ti303016.852.7870.0%[51]
RuNi/Ti3C2×2301649.034.7450%[52]
PtNi/PTOC2910,164.328.7887.8%This work
Publisher’s Note: MDPI stays neutral with regard to jurisdictional claims in published maps and institutional affiliations.

Share and Cite

MDPI and ACS Style

Yu, Y.; Kang, L.; Sun, L.; Xu, F.; Pan, H.; Sang, Z.; Zhang, C.; Jia, X.; Sui, Q.; Bu, Y.; et al. Bimetallic Pt-Ni Nanoparticles Confined in Porous Titanium Oxide Cage for Hydrogen Generation from NaBH4 Hydrolysis. Nanomaterials 2022, 12, 2550. https://doi.org/10.3390/nano12152550

AMA Style

Yu Y, Kang L, Sun L, Xu F, Pan H, Sang Z, Zhang C, Jia X, Sui Q, Bu Y, et al. Bimetallic Pt-Ni Nanoparticles Confined in Porous Titanium Oxide Cage for Hydrogen Generation from NaBH4 Hydrolysis. Nanomaterials. 2022; 12(15):2550. https://doi.org/10.3390/nano12152550

Chicago/Turabian Style

Yu, Yuqian, Li Kang, Lixian Sun, Fen Xu, Hongge Pan, Zhen Sang, Chenchen Zhang, Xinlei Jia, Qingli Sui, Yiting Bu, and et al. 2022. "Bimetallic Pt-Ni Nanoparticles Confined in Porous Titanium Oxide Cage for Hydrogen Generation from NaBH4 Hydrolysis" Nanomaterials 12, no. 15: 2550. https://doi.org/10.3390/nano12152550

Note that from the first issue of 2016, this journal uses article numbers instead of page numbers. See further details here.

Article Metrics

Back to TopTop