DOI:
10.1039/C4RA02476A
(Paper)
RSC Adv., 2014,
4, 20626-20631
Ammonia borane–metal alanate composites: hydrogen desorption properties and decomposition processes
Received
21st March 2014
, Accepted 25th April 2014
First published on 25th April 2014
Abstract
Hydrogen desorption properties and decomposition processes of NH3BH3–MAlH4 (M = Na, Li) composites were investigated by using thermogravimetry-differential thermal analysis-mass spectrometry (TG-DTA-MS), powder X-ray diffraction (XRD) and Fourier transform infrared spectroscopy (FTIR) analyses. We prepared the composites by ball-milling and the mixtures by hand-milling. The ball-milled composites desorbed 4–5 wt% hydrogen at three exothermic steps below 260 °C. The emissions of by-product gases, NH3, B2H6 and B3H6N3, were effectively suppressed. From XRD analysis, the formation of a mixed-metal (Na(Li), Al) amidoborane phase was suggested. Very different results were obtained using hand-milling. They showed only one exothermic reaction at 80–90 °C. The emission of by-product gases was not suppressed. By comparing the differences between ball-milled composites and hand-milled mixtures, the importance of mixed-metal amidoborane in this system was proposed.
1. Introduction
Hydrogen storage is a big challenge for a future hydrogen energy society. The U.S. Department of Energy (DOE) introduced a set of technical targets for on-board hydrogen storage systems in 2003.1 Then, these were revised to the new targets in 2009.2 Ultimate targets for system gravimetric and volumetric capacities of hydrogen were set to 7.5 wt% and 70 g L−1, respectively.2 These values are based on the tank-system, which takes into account the weight and volume of all of tank components. Therefore, capacities on a materials-basis should be much larger than those on a system-basis.3 Hereafter, hydrogen capacities on a materials-basis are described. Many kinds of candidate hydrogen storage materials have been investigated, such as interstitial metal hydrides, complex hydrides, chemical hydrides and adsorbents.4 For example, sodium alanate (NaAlH4) is one of complex hydrides and has a reversible hydrogen capacity of 5.6 wt%.4
Ammonia borane (NH3BH3, AB) is one of chemical hydrides and attracts much attention as hydrogen storage materials. AB has high hydrogen capacities (19.6 wt%, 145 g L−1, respectively) and desorbs hydrogen in a relatively low temperature range.5 Nevertheless, sluggish kinetics below 100 °C, poor recyclability, and emission of by-product gases during heating (e.g., ammonia (NH3), diborane (B2H6) and borazine (B3H6N3)) are disadvantages for practical applications.6–8 For instance, release of ammonia causes damage to the fuel cell performance even at trace levels.9 Also, NH3 and B2H6 are toxic materials for living things.10,11
To overcome these disadvantages, several approaches have been developed, such as infusion of AB in nanoscaffolds,12 doping with transition metals as catalysts,13 size and catalytic effects from graphitic carbon nitride,14 and chemical modification of AB by replacing one of H atoms with an alkali or alkaline earth metal to form metal amidoboranes.15 In previous reports, many kinds of AB–MH (Metal Hydride) composites, such as AB–LiH,15–20 AB–NaH,15–17,21,22 AB–KH,16,17,23 AB–MgH2,24–26 AB–CaH2,24 AB–LiNH2,27 AB–LiBH4,28 and AB–Li3AlH6,29 were synthesized and their dehydrogenation properties were investigated. Recently, AB–amine metal borohydride composites, which showed superior dehydrogenation properties, were also reported.30,31 In our previous report, we experimentally verified that AB–MAlH4 (M = Na, Li) composites, which were prepared based on the indicator we proposed, can suppress the emission of NH3, B2H6 and B3H6N3.32 However, their decomposition processes have not been clarified yet.
In this study, we investigated the decomposition processes of AB–MAlH4 (M = Na, Li) composites. We prepared the composites by ball-milling and the mixtures by hand-milling. We analysed the hydrogen desorption properties by thermogravimetry-differential thermal analysis-mass spectrometry (TG-DTA-MS) and performed phase identification by powder X-ray diffraction (XRD) and Fourier transform infrared (FTIR) spectroscopy. By comparing the ball-milled composites and hand-milled mixtures, the decomposition processes were proposed.
2. Experimental
The starting materials NH3BH3, NaAlH4, LiAlH4 (purity 97%, 90%, 95%, respectively) were purchased from Sigma Aldrich Co. Ltd. These materials were used as-received without any purification. All samples were handled in an argon-filled glovebox to prevent sample oxidation. AB–MAlH4 (M = Na, Li) composites were prepared by ball-milling of AB and MAlH4 (M = Na, Li) with a molar ratio of 1
:
1 under a 1.0 MPa H2 atmosphere with 300 rpm for 5 min. Ball-milling was performed by using a planetary ball-mill apparatus (Fritsch Pulverisette 7) with 20 stainless steel balls (7 mm in diameter) and 300 mg samples (ball: powder ratio = 70
:
1, by mass). We also prepared the mixtures by hand-milling. Hand-milled mixtures were prepared by mixing AB and MAlH4 (M = Na, Li) in an agate mortar in the glove box for 90 seconds. Hand-milling over 120 seconds is dangerous because it often causes gas eruptions. The hydrogen desorption properties were examined by thermal desorption mass spectrometry measurements (TDMS, ULVAC, BGM-102) combined with thermogravimetry and differential thermal analysis (TG-DTA, Bruker, 2000SA). The heating rate was 5 °C min−1 and the helium gas flow rate was 300 mL min−1. Powder X-ray diffraction (XRD, PANalytical, X'Pert Pro with Cu Kα radiation) measurements were performed to observe the phases of composites. The samples used for XRD measurements were placed on a greased glass plate in an argon-filled glovebox and then sealed with a polyimide sheet (Kapton, The Nilaco Co. Ltd.) to avoid oxidation during measurement. Fourier transform infrared spectrometry (FT-IR, Spectrum One, Perkin-Elmer) measurements were performed using a diffuse reflection cell to investigate chemical bonds in the composites. All the samples were diluted with KBr to a mass ratio of 5
:
95 (sample: KBr).
3. Results and discussion
3.1 Hydrogen desorption properties of ball-milled composites
TG-DTA-MS results of ball-milled AB–MAlH4 (M = Na, Li) composites are shown in Fig. 1. As shown in Fig. 1(a), exothermic peaks were observed at 66, 127, and 164 °C in DTA profile of AB–NaAlH4 composite. These peaks correspond to H2 desorption peaks in mass spectra. The composite did not desorb NH3, B2H6, and B3H6N3 at all within the accuracy of our apparatus. From TG profile, the amount of desorbed H2 was estimated at 5 wt%. AB–LiAlH4 composite showed similar H2 desorption properties as those of AB–NaAlH4 composite. Three exothermic peaks (53, 117 and 131 °C) were observed in DTA profile. The composite did not desorb NH3, B2H6 and B3H6N3. The suppression of by-product gas emission was also found in AB–Li3AlH6 composite.29 The amount of desorbed H2 was about 4 wt% for AB–LiAlH4 composite. These results were quite different from the TG-DTA-MS results of AB6 or MAlH4
33 (M = Na, Li) itself, suggesting the reactions between AB and MAlH4 during milling and heating. Theoretical hydrogen capacities of AB–NaAlH4 and AB–LiAlH4 composites are 11.9 wt% and 14.6 wt%, respectively. H2 desorption during ball-milling and M(BH4) formation during heating resulted in a reduction in the amount of desorbed H2 by TG experiments (see Section 3.2). Each exothermic peak of AB–LiAlH4 composite was lower than the corresponding peak of AB–NaAlH4 composite. This would be correlated with the lower thermal stability of LiAlH4 than that of NaAlH4.34
 |
| | Fig. 1 TG-DTA-MS profiles of ball-milled AB–MAlH4 composites; (a) AB–NaAlH4 composite, (b) AB–LiAlH4 composite. The heating rate was 5 °C min−1. | |
3.2 Structure and phase analyses of ball-milled composites
The pressure increase due to H2 desorption was observed during ball-milling, which suggested the mixed-metal amidoborane formed by the reaction between NaAlH4 and AB. NH3, B2H6, and B3H6N3 desorption was not observed during ball-milling. One of the driving forces for the reaction would be the affinity of Hδ− in NaAlH4 and Hδ+ in NH3 of AB. Fig. 2 shows the XRD profiles of ball-milled AB–MAlH4 (M = Na, Li) composites after heating to each temperature. Broad diffraction peaks at around 20° and 27° in all profiles originate from the polyimide film and grease to prevent sample oxidation. In AB–NaAlH4 composite, both AB and NaAlH4 phases were observed at room temperature (RT). Besides, small unknown peaks appeared in the range of 15–30°. These peaks don't match with any diffraction pattern of decomposition products of starting materials or mono-metal amidoborane, suggesting the formation of mixed-metal (Na, Al) amidoborane phase during ball-milling. After heating to 80 °C, the peak intensities of mixed-metal amidoborane became stronger compared to RT. The reaction between AB and NaAlH4 proceeded further to form the mixed-metal amidoborane, resulting in the H2 desorption at 66 °C as shown in Fig. 1(a). After heating to 140 °C, the mixed-metal amidoborane phase disappeared, indicating its decomposition. It is interesting that NaBH4 phase appeared at 140 °C. After heating to 170 °C, strong peak intensities of NaBH4 were observed, while most of NaAlH4 phase disappeared. The formation process of NaBH4 will be described in Section 3.3. Furthermore, a new set of peaks were observed in the range of 10–25°. This could be another mixed-metal amidoborane formed by the reaction between Na3AlH6 and AB. After heating to 260 °C, this unknown phase decomposed and only NaBH4 and Al phases were observed. In case of AB–LiAlH4 composite, similar results were obtained as AB–NaAlH4 composite. At RT, unknown peaks, which were considered as mixed-metal (Li, Al) amidoborane, were observed in the range of 10–25°. After heating to 170 °C, further new peaks were observed in the range of 10–40°. The peak positions of AB–Li3AlH6 composite reported by Xia et al. were also shown as reference in Fig. 2(b).29 The positions of observed peaks were similar to the reference, suggesting the formation of mixed-metal (Li, Al) amidoborane. Though borohydride phase was not observed in the XRD profiles of AB–LiAlH4 composite, the FTIR spectra (Fig. 3(b)) showed the strong B–H stretching. This indicated that the amorphous LiBH4 formed during heating.
 |
| | Fig. 2 XRD profiles of ball-milled AB–MAlH4 composites after heating to each temperature; (a) AB–NaAlH4 composite, (b) AB–LiAlH4 composite. | |
 |
| | Fig. 3 In situ FTIR spectra of ball-milled AB–MAlH4 composites at each temperature; (a) AB–NaAlH4 composite, (b) AB–LiAlH4 composite. AB and MAlH4 (M = Na, Li) spectra was presented for comparison. The heating rate was 5 °C min−1. | |
Fig. 3 shows the in situ FTIR spectra of ball-milled AB–MAlH4 (M = Na, Li) composites during heating. The spectra of AB and MAlH4 (M = Na, Li) at RT were also shown as references. In AB–MAlH4 (M = Na, Li) composites, peak intensities corresponding to N–H stretching between 3150 and 3500 cm−1 decreased as temperature increased, whereas peaks corresponding to B–H stretching between 2200 and 2400 cm−1 were remained after heating to 260 °C in both composites. This phenomenon was also observed in other metal amidoboranes.21,24,25,28,29 A new compound containing nitrogen would be formed during H2 desorption.
3.3 Comparison with hand-milled mixtures
To clarify the reaction process in detail, we prepared the mixtures by hand-milling and investigated their H2 desorption properties and phases. Interestingly, results were quite different from the ball-milled composites. Fig. 4 shows TG-DTA-MS results of hand-milled AB–MAlH4 (M = Na, Li) mixtures. Sharp exothermic peaks were observed at 90 °C (AB–NaAlH4) and 84 °C (AB–LiAlH4) in DTA profiles. The weight losses of about 30 wt% (AB–NaAlH4) and 50 wt% (AB–LiAlH4) were also observed. From the mass spectra, H2, NH3, B2H6 and B3H6N3 peaks were observed in both mixtures. Except this exothermic reaction, any reactions were not observed up to 260 °C.
 |
| | Fig. 4 TG-DTA-MS profiles of hand-milled AB–MAlH4 mixtures; (a) AB–NaAlH4 mixture, (b) AB–LiAlH4 mixture. The heating rate was 5 °C min−1. | |
Fig. 5 shows the XRD profiles of hand-milled AB–MAlH4 (M = Na, Li) mixtures before and after heating to 260 °C. Before heating, AB and MAlH4 (M = Na, Li) were observed. Unknown peaks were not observed in the range of 10–30°, which was different from the results of ball-milled composites. After heat treatment, NaBH4 was observed in the AB–NaAlH4 mixture, which was similar to the results of ball-milled composites.
 |
| | Fig. 5 XRD profiles of hand-milled AB–MAlH4 mixtures at RT and after heating to 260 °C; (a) AB–NaAlH4 mixture, (b) AB–LiAlH4 mixture. | |
The reaction observed in the hand-milled mixture was quite similar to the solid state reaction of MAlH4 (M = Na, Li) with NH4Cl. In this reaction, MCl and [H4Al·NH4] is formed and soon [H4Al·NH4] decomposes to [HAlNH] and H2, accompanied by a large exothermic heat.35 The previous study showed diammoniate of diborane (DADB), [(NH3)2BH2]+[BH4]−, an ionic isomer of AB, is formed during the induction period before H2 desorption occurs.36 MAlH4 was also confirmed to be an ionic compound, consisting of M+ cation and AlH4− anion.37 Considering the reaction between DADB and NaAlH4, the reaction between BH4− anion and Na+ cation would cause the formation of NaBH4. On the one hand, the reaction between [(NH3)2BH2]+ and AlH4− would cause the H2 and by-product gas emissions. However, the ball-milled composites showed the different results from the hand-milled mixtures. This would be attributed to the formation of mixed-metal amidoborane. Though this phase was not observed in the hand-milled mixtures, it was observed in the ball-milled composites at not only RT but also other temperatures (e.g., 170 °C). The interaction between metal amidoborane and AB like LiNH2BH3·NH3BH3 showed the significantly low H2 desorption temperature.19,20 Similarly, the interaction between mixed-metal amidoborane and AB could occur in the ball-milled composites. Mixed-metal amidoborane would stabilize the reaction between Al–H bonds and N–H bonds, resulting in the suppression of by-product gases. Thus, it is suggested that mixed-metal amidoborane plays an important role in suppressing the emission of by-product gases.
4. Conclusions
AB–MAlH4 (M = Na, Li) composites were successfully synthesized by ball-milling and their hydrogen desorption properties and decomposition processes were investigated. The composites desorbed 4–5 wt% hydrogen below 260 °C, accompanied by H2 desorption. They did not desorb NH3, B2H6, and B3H6N3 at all. They showed three exothermic reactions below 260 °C, accompanied by H2 desorption. The first reaction is ascribed to the formation of mixed-metal amidoborane phase. The second reaction is ascribed to the decomposition of mixed-metal amidoborane. In the last, the reactions described as below occurred. One is the reaction between AB and MAlH4 (M = Na, Li), which result in the formation of MBH4 (M = Na, Li). The other is the reaction between M3AlH6 (M = Na, Li) and AB, which result in the formation of another mixed-metal amidoborane. The hand-milled mixtures showed quite different results from the ball-milled composites. They showed only one exothermic reaction at 80–90 °C. The emission of by-product gases was not suppressed. By comparing the results of the ball-milled composites with those of the hand-milled mixtures, the importance of the mixed-metal amidoborane as a barrier against by-product gas emission in this system was proposed. These results would be helpful for clarifying reaction mechanisms of AB–MH composites.
Notes and references
- S. Satyapal, J. Petrovic, C. Read, G. Thomas and G. Ordaz, Catal. Today, 2007, 120, 246–256 CrossRef CAS PubMed.
- http://www1.eere.energy.gov/hydrogenandfuelcells/storage/pdfs/targets_onboard_hydro_storage_explanation.pdf.
- J. Yang, A. Sudik, C. Wolverton and D. J. Siegel, Chem. Soc. Rev., 2010, 39, 656–675 RSC.
- U. Eberle, M. Felderhoff and F. Schüth, Angew. Chem., Int. Ed., 2009, 48, 6608–6630 CrossRef CAS PubMed.
- F. H. Stephens, V. Pons and R. T. Baker, Dalton Trans., 2007, 2613–2626 RSC.
- G. Wolf, J. Baumann, F. Baitalow and F. P. Hoffmann, Thermochim. Acta, 2000, 343, 19–25 CrossRef CAS.
- F. Baitalow, J. Baumann, G. Wolf, K. J. RÖβler and G. Leitner, Thermochim. Acta, 2002, 391, 159–168 CrossRef CAS.
- J. Baumann, F. Baitalow and G. Wolf, Thermochim. Acta, 2005, 430, 9–14 CrossRef CAS PubMed.
- N. Rajalakshmi, T. T. Jayanth and K. S. Dhathathreyan, Fuel Cells, 2004, 3, 177–180 CrossRef CAS.
- International Chemical Safety Cards, ICSC number: 0414.
- International Chemical Safety Cards, ICSC number: 0432.
- A. Gutowska, L. Li, Y. Shin, C. M. Wang, X. S. Li, J. C. Linehan, R. S. Smith, B. D. Kay, B. Schmid, W. Shaw, M. Gutowski and T. Autrey, Angew. Chem., Int. Ed., 2005, 44, 3578–3582 CrossRef CAS PubMed.
- B. L. Conley, D. Guess and T. J. Williams, J. Am. Chem. Soc., 2011, 133, 14212–14215 CrossRef CAS PubMed.
- Z. Tang, X. Chen, H. Chen, L. Wu and X. Yu, Angew. Chem., Int. Ed., 2013, 52, 5832–5835 CrossRef CAS PubMed.
- Z. Xiong, C. K. Yong, G. Wu, P. Chen, W. Shaw, A. Karkamkar, T. Autrey, M. O. Jones, S. R. Johnson, P. P. Edwards and W. I. F. David, Nat. Mater., 2008, 7, 138–141 CrossRef CAS PubMed.
- A. T. Luedtke and T. Autrey, Inorg. Chem., 2010, 49, 3905–3910 CrossRef CAS PubMed.
- Y. Zhang and C. Wolverton, J. Phys. Chem. C, 2012, 116, 14662–14664 Search PubMed.
- K. Shimoda, K. Doi, T. Nakagawa, Y. Zhang, H. Miyaoka, T. Ichikawa, M. Tansho, T. Shimizu, A. K. Burrell and Y. Kojima, J. Phys. Chem. C, 2012, 116, 5957–5964 CAS.
- C. Wu, G. Wu, Z. Xiong, W. I. F. David, K. R. Ryan, M. O. Jones, P. P. Edwards, H. Chu and P. Chen, Inorg. Chem., 2010, 49, 4319–4323 CrossRef CAS PubMed.
- C. Wu, G. Wu, Z. Xiong, X. Han, H. Chu, T. He and P. Chen, Chem. Mater., 2010, 22, 3–5 CrossRef CAS.
- K. J. Fijałkowski and W. Grochala, J. Mater. Chem., 2009, 19, 2043–2050 RSC.
- K. Shimoda, Y. Zhang, T. Ichikawa, H. Miyaoka and Y. Kojima, J. Mater. Chem., 2011, 21, 2609–2615 RSC.
- H. V. K. Diyabalanage, T. Nakagawa, R. P. Shrestha, T. A. Semelsberger, B. L. Davis, B. L. Scott, A. K. Burrell, W. I. F. David, K. R. Ryan, M. O. Jones and P. P. Edwards, J. Am. Chem. Soc., 2010, 132, 11836–11837 CrossRef CAS PubMed.
- Y. Zhang, K. Shimoda, H. Miyaoka, T. Ichikawa and Y. Kojima, Int. J. Hydrogen Energy, 2010, 35, 12405–12409 CrossRef CAS PubMed.
- X. Kang, L. Ma, Z. Fang, L. Gao, J. Luo, S. Wang and P. Wang, Phys. Chem. Chem. Phys., 2009, 11, 2507–2513 RSC.
- J. Luo, Z. Kang and P. Wang, Energy Environ. Sci., 2013, 6, 1018–1025 CAS.
- K. R. Graham, T. Kemmitt and M. E. Bowden, Energy Environ. Sci., 2009, 2, 706–710 CAS.
- J. Luo, H. Wu, W. Zhou, X. Kang, Z. Fang and P. Wang, Int. J. Hydrogen Energy, 2012, 37, 10750–10757 CrossRef CAS PubMed.
- G. Xia, Y. Tan, X. Chen, Z. Guo, H. Liu and X. Yu, J. Mater. Chem. A, 2013, 1, 1810–1820 CAS.
- Y. Tan, Q. Gu, J. A. Kimpton, Q. Li, X. Chen, L. Ouyang, M. Zhu, D. Sun and X. Yu, J. Mater. Chem. A, 2013, 1, 10155–10165 CAS.
- X. Chen, F. Yuan, Q. Gu and X. Yu, Dalton Trans., 2013, 42, 14365–14368 RSC.
- Y. Nakagawa, S. Isobe, Y. Ikarashi and S. Ohnuki, J. Mater. Chem. A, 2014, 2, 3926–3931 CAS.
- T. Zhang, S. Isobe, Y. Wang, H. Oka, N. Hashimoto and S. Ohnuki, J. Mater. Chem. A, 2014, 2, 4361–4365 CAS.
- T. Matsunaga, F. Buchter, K. Miwa, S. Towata, S. Orimo and A. Züttel, Renewable Energy, 2008, 33, 193–196 CrossRef CAS PubMed.
- H. Zhang, Y. S. Loo, H. Geerlings, J. Lin and W. S. Chin, Int. J. Hydrogen Energy, 2010, 35, 176–180 CrossRef CAS PubMed.
- A. C. Stowe, W. J. Shaw, J. C. Linehan, B. Schmid and T. Autrey, Phys. Chem. Chem. Phys., 2007, 9, 1831–1836 RSC.
- H. W. Brinks and B. C. Hauback, J. Alloys Compd., 2003, 354, 143–147 CrossRef CAS.
|
| This journal is © The Royal Society of Chemistry 2014 |
Click here to see how this site uses Cookies. View our privacy policy here.