Charles W. Hamiltona, R. Tom Baker*b, Anne Staubitzc and Ian Manners*c
aLos Alamos National Laboratory, Inorganic, Isotope, and Actinide Chemistry, MS J582, Los Alamos, NM 87545, USA. E-mail: chamilton@lanl.gov; Fax: +1 505-667-3502; Tel: +1 505-665-4636
bDepartment of Chemistry, University of Ottawa, 10 Marie Curie, Ottawa, Ontario, Canada K1N 6N5. E-mail: rbaker@uottawa.ca; Tel: +1 613-562-5800 ext. 5698; +1 613-562-5800 ext. 5613
cUniversity of Bristol, School of Chemistry, Cantock’s Close, Bristol, UK BS8 1TS. E-mail: Ian.Manners@bristol.ac.uk; Fax: +44 (0)117 929 0509
First published on 26th November 2008
Hydrogen storage for transportation applications requires high volumetric and gravimetric storage capacity. B–N compounds are well suited as storage materials due to their light weight and propensity for bearing multiple protic (N–H) and hydridic (B–H) hydrogens. This critical review briefly covers the various methods of hydrogen storage, and then concentrates on chemical hydrogen storage using B–N compounds. The simplest B–N compound, ammonia borane (H3NBH3), which has a potential 19.6 wt% hydrogen storage capacity, will be emphasised (127 references).
Charles W. Hamilton | Charles Wayne Hamilton was born in Houston, Texas, USA. He received his BS in Chemistry from Texas A&M University in May of 2001. During his undergrad, he studied nuclear chemistry at the Cyclotron Institute under the direction of Prof. Joseph Natowitz. He then joined the laboratory of Prof. Joseph Sadighi at the Massachusetts Institute of Technology where he studied oxidation catalysis. He received his PhD in 2007, and subsequently accepted a post-doctoral position at Los Alamos National Laboratory where he currently resides. His current research interests include the formation of molecular catalysts for amine borane dehydrogenation. |
R. Tom Baker | R. Tom Baker received his BSc degree from UBC in 1975 and his PhD from UCLA in 1980 with M. Frederick Hawthorne. After a postdoctoral stint with Philip S. Skell at Penn State, he joined DuPont Central Research in Wilmington, DE, where he applied inorganic and organometallic chemistry and homogeneous catalysis to the nylon, fluoroproducts, and titanium dioxide businesses. He joined the Chemistry Division at Los Alamos National Laboratory in 1996 and worked on multifunctional catalysis approaches to low-temperature hydrocarbon functionalization and chemical hydrogen storage. In 2008, he became a chemistry professor at University of Ottawa and the director of the Centre for Catalysis Research and Innovation. |
Anne Staubitz | Anne Staubitz obtained a diploma in biochemistry from the University of Tübingen, Germany. For her diploma thesis she worked in the group of Prof. Paul Knochel at the University of Munich with novel Grignard reagents applied to the synthesis of heterocycles. She then did her PhD with Prof. Varinder Aggarwal at the University of Bristol, working on a natural product synthesis. In Ian's group she is working as a postdoctoral fellow on the catalytic dehydrogenation of group 13–group 15 adducts. |
Ian Manners | Ian Manners received his PhD from the University of Bristol in 1985 in the area of transition metal chemistry. After completing postdoctoral work in Germany in main group chemistry and the USA on polymeric materials, he joined the University of Toronto, Canada in 1990. After 15 years he returned to his Alma Mater to take up a Chair in Inorganic, Macromolecular and Materials Chemistry. His research interests focus on the development of new synthetic reactions in inorganic chemistry and their applications in molecular synthesis, polymer and materials science, supramolecular chemistry, and nanoscience. |
The transportation sector represented 31(28)% of the EU(US) energy use in 2005(2006) and accounted for 21(34)% of CO2 emissions.2,3 For stationary energy applications, CO2 can be potentially sequestered.4 For portable energy, however, this is impractical and an alternative energy carrier must be used.
Hydrogen has the potential to be a clean, source-independent, energy carrier.5 It has a high energy content per mass compared to petroleum (120 MJ kg−1 for hydrogen versus 44 MJ kg−1 for petroleum). Also, hydrogen can be readily used to run a fuel cell, which greatly increases efficiency over internal combustion engines (∼32% efficiency for diesel-electric; 90% potential efficiency for fuel cell with heat capture, 85% for electric motor, 77% overall efficiency) while eliminating formation of carbon particulates and sulfur and nitrogen oxides.6 Unfortunately, hydrogen has a poor energy content per volume (0.01 kJ L−1 at STP and 8.4 MJ L−1 for liquid hydrogen vs. 32 MJ L−1 for petroleum).
For transportation applications, an energy carrier should have a high energy content in as small a volume as possible to not intrude on passenger space, and as small a mass as possible to maintain fuel efficiency. The US Department of Energy has established a series of targets for hydrogen storage materials so that a vehicle can travel >500 km on a single hydrogen fill.5 Included with this are stringent system volumetric (5.4 MJ L−1 2010, 9.72 MJ L−1 2015) and gravimetric targets (6 wt% 2010, 9 wt% 2015). Evaluation of a hydrogen storage system includes all associated components (tank, valves, regulators, piping, mounting brackets, insulation, added coolants, etc.).
There are currently four leading methods to store hydrogen: physical means, sorbents, metal hydrides, and so-called chemical hydrides. All four will be briefly summarised, and then chemical hydrides with B–N bonds will be discussed in greater detail. Details of the potential of ammonia borane as a hydrogen storage material have been presented recently.7
While liquid hydrogen has a higher density than compressed gas, maintaining the low temperatures requires extra components that adversely affect system volumetric and gravimetric storage capacity. Boil-off control is also a significant problem, with tanks losing approximately 1% per day. Finally, significant energy needs to be input to liquefy hydrogen (30% of the lower heating value for hydrogen).5
Carbon-based materials such as nanotubes, nanofibres, solid foams, and activated carbon have been extensively studied. There was initially some confusion about the hydrogen uptake potential of these materials due to the various methods of measuring hydrogen uptake. Recently, the results have been more consistent, with several methods being employed in the same study.11 The maximum adsorption is ∼5 material wt% hydrogen at 77 K; with addition of tanks and cooling systems, the system storage capacity will be much lower.
Zeolite structures have also been examined.12 Zeolites are microporous structures of hydrated aluminate and silicate that are more easily prepared than nanotubes and offer greater control over pore size. However, they consist of atoms that are heavier than carbon, which limits gravimetric capacity. An emerging field is using zeolite structures as a template to form carbon networks.13 Templating carbon onto zeolites is difficult because zeolite structures can be disordered. Nonetheless, recent results demonstrated hydrogen uptake for zeolite-like carbon materials of 6.9 wt% at 77 K and 20 bar.
Organic polymers with intrinsic microporosity (PIMs) are another alternative.14 PIMs are made of rigid monomers to maintain microporosity (Fig. 1a), yielding gravimetric storage capacity of up to 3.0 wt% at 77 K and 15 bar.15 Increasing pore size (and thus surface area) should result in a higher storage capacity.
Fig. 1 (a) Some examples of PIMs made up of rigid monomers. (b) Different linkers result in different pore sizes for MOFs.17 |
Metal–organic frameworks (MOFs) have also recently come into focus as potential hydrogen storage materials.16 These are three-dimensional polymers of metal atoms linked by bridging ligands (Fig. 1b).17 MOFs are readily synthesised by solution methods and then activated by heating to remove solvent molecules. Pore sizes can be rationally designed by choosing the metal and the linker. However, with large linkers, these tend to form interpenetrated structures which can decrease pore size. Similar to carbon nanotubes, MOFs rely primarily on physisorption to bind hydrogen and low temperatures (typically 77 K) are required.
To make these materials more practical, the temperature of effective adsorption must be raised (ideally to ambient temperatures). By adding in metal atoms or other materials capable of chemisorption, the energy of binding can be adjusted. This combination of chemisorption and physisorption could potentially increase the temperature of effective uptake. There are several recent examples of increasing the enthalpy of hydrogen adsorption for zeolites,18 MOFs,19 and carbon materials.20 However, the inclusion of extra elements decreases material gravimetric capacity.
One way to achieve higher gravimetric capacity is by including lighter main-group elements. These complex metal hydrides, such as alanates, amide, and borohydride compounds, have been evaluated as reversible hydrogen storage materials.21 One of the early examples is titanium-doped sodium alanate (NaAlH4), which can reversibly release hydrogen to give a maximum material gravimetric capacity of 5.5 wt% (although 3–4 wt% is typically obtained). Chen et al. found that Li3N can add roughly two equivalents of hydrogen to form lithium amide (LiNH2) and two equivalents of lithium hydride at elevated temperatures (200–250 °C) to give a 9.3 wt% uptake of hydrogen (Scheme 1).22 Under vacuum and at temperatures below 200 °C, 6.3 wt% of hydrogen desorbs. The remaining 3 wt% could be removed by heating above 320 °C.
Scheme 1 Reactions of some complex hydrides. |
Calcium borohydride can be heated to 400 °C to release 9.6 wt% hydrogen (Scheme 1).23 Upon addition of catalytic amounts of the dopants, TiCl3 and Pd, the ‘spent fuel’ can be rehydrogenated at 700 bar and 400–440 °C in 60% yield.
Recent effort has concentrated on mixtures of complex metal hydrides as potential hydrogen storage systems. Yang and Sudik found that ternary mixtures of MgH2, LiNH2 and LiBH4 have increased rates and extent of hydrogen release compared to binary mixtures of these components.24 At elevated temperatures (∼350 °C), 8–11 wt% hydrogen is released depending on the amount of MgH2 in the mixture. At lower temperatures, hydrogen release is reversible (2.8 wt% at 140 °C). Soloveichik and co-workers reported the decomposition of a compound that contains borohydride and amines, Mg(BH4)·2NH3.25 This compound has a maximum storage capacity of 16.0 wt%. Though hydrogen loss is observed at 150 °C, even heating to 400 °C results in a net loss of only 13.1 wt% hydrogen. Rehydrogenation has not yet been realised, but loss of hydrogen is reported to be endothermic, indicating that direct rehydrogenation may be possible.
Most potential chemical hydrogen storage materials suffer from reaction enthalpies that are too endothermic or exothermic for reversible hydrogen release. Reaction kinetics can also be a significant problem. Indeed, for many years, the only known examples of hydrogen activation under mild conditions by non-metals involved complexes only isolable in matrices.26 However, there have been several recent examples of isolable non-metal compounds that add hydrogen under mild conditions. Power and co-workers demonstrated addition of two hydrogen molecules to a digermyne compound (Scheme 2).27 This was followed by the discovery of facile hydrogen addition across two diaryltin molecules.27 The reverse reaction, the conversion of two E–H bonds to hydrogen and an E–E bond, has been demonstrated by Himmel and co-workers for a B–H species.28 Bertrand, Schoeller, and co-workers designed N-heterocyclic carbene analogues, with an N-aryl group substituted with a carbon group, which add hydrogen under mild heating.29 Stephan and co-workers reported the reversible heterolysis of hydrogen over a phosphinoborane species [1,4-(R2P)C6F4(BR2)] to make a phosphonium-borate zwitterionic compound.30 Finally, mixtures of Lewis acids (BR3) and Lewis bases (PR′3,31N-heterocyclic carbenes,31,32 and NR′333) that are typically too sterically encumbered to form a dative bond (frustrated Lewis pairs) are capable of adding hydrogen under mild conditions to form borate salts. The ease of hydrogen addition depends on the sterics and electronics of the frustrated Lewis pairs. All of these systems have very low gravimetric capacity, but studying the basic reactions of hydrogen addition to non-metal systems can garner insight into the design of reversible systems with higher storage capacity.
Scheme 2 Non-metal compounds that add hydrogen under mild conditions. |
Cyclic organic molecules have also been evaluated as potential hydrogen storage materials.34 Dehydrogenation of organic molecules is typically too endothermic for hydrogen release at moderate temperatures. However, incorporation of fused rings and heteroatoms (O and especially N) can lower the heat requirements for hydrogen release.35 Due to the large kinetic barriers, a catalyst (typically noble metal-based) is also used to aid dehydrogenation and rehydrogenation. For instance, in a recent patent, Pez and co-workers reported that N-ethylcarbazole can be hydrogenated over Ru/LiAlO2 at 1000 psi of hydrogen and 160 °C. The hydrogen can then be released over Pd/LiAlO2 at 199 °C to give 5.6 wt% hydrogen (Scheme 3). More importantly, the system can be cycled 5 times with no detectable degradation of the N-ethylcarbazole.
Scheme 3 Reversible dehydrogenation of N-ethylcarbazole. |
There are several systems that rely on hydrolysis of active metals36 or chemical hydrides to produce hydrogen. Thorn and co-workers reported that a C–H in the 2-position of benzimidazoles is sufficiently hydridic to be protonated by a variety of acids including water over a Pd catalyst to produce hydrogen.37 Hydrolysis of another chemical hydride, sodium borohydride, has also been investigated. Although it can be stabilised in basic aqueous solutions, the addition of catalysts or acids can be used to initiate a controlled release of hydrogen by hydrolysis.38 Unfortunately, efficiently regenerating the BO2− to BH4− is difficult due to the stability of B–O bonds.
Under the current technology, chemical hydrides with high storage capacity will require off-board regeneration, which adds to the complexity of the hydrogen storage system. However, these compounds could offer advantages for the fuel distribution system. Current fuel distribution is based on transporting liquid hydrocarbons; converting this system to transport compressed or liquid hydrogen will be an expensive endeavour (potentially costing trillions of dollars).39 A stable chemical hydride could circumvent this problem, allowing for transportation of hydrogen using the existing infrastructure.
Scheme 4 Synthesis of hydrazine bis(borane) and hydrazine monoborane. |
Ammonium hydrotriborate ([NH4][B3H8]) has also been synthesised by treatment of pentaborane with ammonium hydroxide.48 Surprisingly, this is a stable, colourless, crystalline solid in pure form, and no decomposition was evident on heating the solid at 60 °C for 70 hours. It is apparently stable in water and alcohols and slowly decomposes to form H3N–B3H7 and H2 when treated with benzene or ether. This is in stark contrast to [NH4][BH4]49 which decomposes at temperatures above −40 °C. Ammonium hydrotriborate has a potential hydrogen storage capacity of 13.9 wt% (assuming loss of 4 eq. H2). Hydrogen loss from alkylammonium hydrotriborate salts has been realised by addition of metallic Si or Al (Scheme 6).50 When [NH3Me][B3H8] is treated with Si, 5 eq.51 of hydrogen gas are released giving 9.9 wt% H2.
Scheme 6 Synthesis of ammonium hydrotriborate and dehydrogenation of alkylammonium salts. |
Guanidinium hydrotriborate, [C(NH2)3][B3H8], has been prepared by treating di(guanidinium) sulfate with sodium hydrotriborate.52 At ∼100 °C, this compound violently decomposes to form 6.2 eq. H2 (by MS), which provides 12.3 material wt%. It was noted that some decomposition was evident if the compound was stored at 20 °C for ∼2 months. Also, triaminoguanidinium hydrotriborate, [C(NHNH2)3][B3H8] was synthesised by treatment of pentaborane with triaminoguanidine.53 A decomposition point was not reported, but a melting point of 72–78 °C was determined. The potential hydrogen storage capacity is 11.0 wt% (assuming loss of 8 eq. H2).
It is important to note that these polyborane compounds are likely to be explosive, as many related compounds have been used as rocket propellants.
In a theoretical study, Nguyen, Matus, and Dixon investigated the heats of formation of several ammonium salts of polyboranes.57 They found that formation of [B12H12][NH4]2 from H2 (10 eq.), BN (2 eq.), and B (10 eq.) has a heat of formation of only 10 to 12 kcal mol−1 (the reverse reaction would result in loss of 8.8 wt% of H2 from [B12H12][NH4]2). In a recent DOE progress report, Hawthorne and co-workers investigated a series of anionic polyborane compounds for hydrogen storage applications.58 Ammonium salts of (B11H14)−, (B12H12)2−, and (B10H10)2− were all synthesised and hydrolyzed in the presence of a metal catalyst to yield hydrogen, ammonium borate, and boric acid (Scheme 7).
Scheme 7 Hydrolysis of ammonium polyborane salts. |
Alkylamine borane | Melting point/°C | Decomp. point/°C |
---|---|---|
a Table adapted from ref. 59. | ||
H3NBH3 | 104 | ∼100 |
H2MeNBH3 | 56 | 70 |
H2EtNBH3 | 19 | 30–40 |
H2nPrNBH3 | 45 | 50–70 |
H2iPrNBH3 | 65 | 90–100 |
H2nBuNBH3 | −48 | 10–15 |
H2tBuNBH3 | 96 | 120–140 |
HMe2NBH3 | 37 | 150 |
HEt2NBH3 | −18 | 200 |
HnPr2NBH3 | 30 | 140 |
HiPr2NBH3 | 23 | 250 |
HnBu2NBH3 | 15 | 120 |
HiBu2NBH3 | 19 | 150 |
Hawthorne reported that B-substituted amine boranes can be prepared by reduction of alkylboroxines [(BOR)3] using lithium aluminium hydride in the presence of trimethylamine.61 The majority of the Me3NBRH2 (R = nPr, iPr, nBu, 2-Bu, iBu, tBu, n-pentyl, and n-hexyl) compounds are liquids at room temperature with the exception of R = cyclohexyl (mp = 40–41 °C) and benzyl (mp = 58–60 °C). Treatment of these compounds with excess ammonia in the presence of catalytic ammonium chloride at 100–150 °C affords B-substituted borazines, [HNBR]3, in moderate to good yield (65–91%).62
In a theoretical study, Manners, Harvey and co-workers investigated the effect of B- and N-substituents on the ΔG and ΔH of dehydrogenation of HR2NBR′2H.63 Loss of hydrogen from amine boranes normally is too exergonic for reversibility (see the section: Thermal dehydrogenation of amine boranes). By altering the substituents (R and R′) on HR2NBR′2H, however, the ΔG of dehydrogenation can be made more neutral. A strong dative N–B σ-bond in the reactant (HR2NBR′2H) and a weak dative N–B π-bond in the product (R2NBR′2) results in a less exergonic dehydrogenation. In general, the σ-bond plays a more important role in determining the overall energetics, so HR2NBR′2H compounds with electron donating groups on nitrogen (resulting in a more Lewis-basic amine) and electron withdrawing groups on boron (resulting in a more Lewis-acidic borane) are best suited for reversible dehydrogenation. Evaluation of a series of cyclic amines indicates that four- and five-membered rings exhibit very similar dehydrogenation enthalpies, whereas mechanisms involving six-membered rings are more endothermic. This appears to be an effect of added ring strain going from an sp3- to an sp2-hybridised nitrogen centre.
Hydrogen loss from amine boranes is typically effected by solvolysis (including acid- and metal-catalysed variants) or thermolysis, in which the product distribution depends on the reaction conditions and presence of additives or catalysts. The easiest way to evaluate the extent of hydrogen loss is by measuring the amount of hydrogen gas generated by either Toepler pump or GC/MS methods. Gas burette and thermogravimetric analysis (TGA) may also be used, but other gaseous products may also contribute to the volume measured without a method for direct identification or quantification. Temperature-programmed desorption (TPD) provides a means to analyze the volatile products by MS. If soluble products are formed, NMR spectroscopy (especially 1,2H, 11B, and 14,15N)64 can also give a good indication of the extent of dehydrogenation by both the chemical shift and multiplicity of peaks formed (Fig. 2). The wide chemical shift range for 15N NMR is particularly useful, with sp2-hybridised N in substituted borazines from −230 to −280 ppm and sp3-hybridised N in alkylamine boranes from −340 to −375 ppm.65 Many of these nuclei are quadrupolar and observed line widths will depend on the electric field gradient at the nucleus and the nuclear correlation time. Large molecules with low symmetry (around the quadrupolar nucleus) in viscous solvents will thus give rise to broad resonances. The increased molecular motion and decreased viscosity at higher temperatures can often be used to reduce linewidths in solution NMR experiments. Conversely, cooling the sample effectively ‘decouples’ the quadrupolar interaction to adjacent nuclei thus reducing line widths of, for example, 1H and 13C NMR signals in alkylboranes. Finally, double rotation experiments or use of high magnetic fields allows for useful information to be obtained for quadrupolar nuclei in the solid state as well.66
Scheme 8 Acid catalysed hydrolysis of ammonia borane. |
Amine borane | Catalyst | Solvent | Eq. of H2 released | Temp/°C | Time | Ref. | |
---|---|---|---|---|---|---|---|
1 | H2tBuNBH3 | 10% Pd/C (50%wet) | MeOH | Approx 3 | 30 | 100 min | 71, 72 |
Me3NBH3 | 20 h | ||||||
2 | Various | 10% Pd/C (50%wet) | H2O, various alcohols | High efficiency | 20 | 5 min (MeOH) to 190 min (tBuOH) | 73 |
Raney Ni (5 mol%) | |||||||
3 | H3NBH3 | Pt (20% on C) (2 mol%) | H2O | Approx 3 | 20 | 2 min | 74 |
[Rh(1,5-cod)(μ-Cl)]2 (2 mol%) | Approx 2.7 | 20 min | |||||
Pd (2 mol%) | Approx 2.5 | 250 min | |||||
4 | H3NBH3 | Dowex (12 wt%) | H2O | Approx 2.8 | 20 | 8 min | 70 |
CO2 | No AB left | 7 days | |||||
5 | H3NBH3 | Co (10% on C) (2 mol%) | H2O | Approx 2.9 | 20 | 60 min | 75 |
Ni (10% on γ-Al2O3) (2 mol%) | Approx 2.9 | 60 min | |||||
6 | H3NBH3 | Ni0.88Pt0.12 hollow sphere (2 mol%) | H2O | Approx 3 | 20 | 30 min | 79 |
7 | H3NBH3 | Rh colloids (1 mol%) | H2O | Approx 2.8 | 20 | 40 s | 76 |
Ir colloids (1 mol%) | Approx 3 | 105 min | |||||
Co colloids (1 mol%) | Approx 3 | 60 min | |||||
8 | H3NBH3 | RuCl3 (0.5 mol%) | MeOH | Approx 3 | 20 | 5 min | 77 |
9 | H3NBH3 | Amorphous Fe nanoparticles | H2O | Approx 3 | 20 | 8 min | 80 |
10 | H3NBH3 | Various Co, Ni, Cu nanoparticles | H2O | Approx 3 | 20 | 20–300 min | 78 |
Scheme 9 Mechanism of BH3 catalysed AB dehydrogenation. |
In the condensed phase, thermolysis of amine boranes such as AB and methylamine borane (H2MeNBH3, MeAB) have been shown to proceed by an intermolecular mechanism that involves initial formation of a diaminoboronium borohydride salt (Scheme 10). Further reaction of this salt with additional amine borane molecules builds up aminoborane chains with formation of a new B–N bond for each hydrogen molecule released. Computational investigations of presumed linear polyaminoborane products, H3N(BH2NH2)nBH3, showed that low energy coiled and helical conformations are favoured that feature B–H⋯H–N dihydrogen bonding.84
Scheme 10 Formation of the diaminoboronium borohydride salt. |
Dehydrogenation of amine boranes typically yields a variety of oligomeric products depending on conditions and methods unless they are sterically blocked (Fig. 2, for AB). Dixon and co-workers calculated the thermodynamics of the formation of smaller oligomers [BxNxHy (x = 2, 3)] in both the gas and condensed phase.85 Larger oligomeric products were evaluated in the condensed phase by Miranda and Ceder.86 These products result from both a polymeric ammonia borane cycle (AB to PAB to PIB; see Fig. 2 for structures) and a cyclic oligomeric pathway (AB to CTB, borazine or 1,4-polyborazylene). While the overall reaction enthalpies depend on the products formed, all reactions in the study are estimated to be mildly exothermic [−1.6 to −20 kcal mol−1 AB]. If one considers that the entropic term contributes ∼8 kcal mol−1 H2, it is clear that direct rehydrogenation will not be possible under practical conditions and that amine boranes will need to be regenerated in a chemical process. A few products, such as borazine, are volatile. Loss of these products leads to contamination of the hydrogen stream (potentially poisoning the fuel cell), and material loss (limiting regeneration efficiency).
Fig. 2 Some products of dehydrogenation from AB, and 11B NMR shifts. |
The parent, ammonia borane, decomposes in three distinct steps (Scheme 11).89 The first commences at ∼100 °C and peaks between 107 and 117 °C with an initial weight loss of ∼1.1 eq. of dihydrogen (∼7.2 wt%). The second equivalent is lost over a much broader temperature range, with a maximum rate at ∼150 °C, and the rest released at much higher temperatures.90 Since all steps are exothermic, the high temperature requirement is a reflection of the significant kinetic barriers. The decomposition temperatures and products of dehydrogenation are dependent on the rate that the temperature is elevated. Lower temperature ramping rates result in a higher decomposition temperature. Analysis (IR and MS) of the volatile thermolysis products for the first dehydrogenation step revealed traces of B2H6, H2NBH291 and borazine accompanying the evolved hydrogen.92 Subsequent detailed 11B solid state NMR studies at high field showed that formation of a new AB mobile phase preceded formation of the diammoniate of diborane (DADB, [BH2(NH3)2][BH4]). DADB, formed from two AB molecules by a hydride transfer, actually initiates hydrogen loss and concomitant B–N bond formation.93 A similar intermediate was proposed for the thermal decomposition of MeAB.88 The second hydrogen-releasing step produces cyclic iminoborane oligomers (including borazine and B–N linked borazines, polyborazylene) whose proposed graphitic structure is reminiscent of hexagonal and rhombohedral phases of boron nitride.94
Scheme 11 Thermolysis of ammonia borane. |
The dehydrogenation rate can be increased by the inclusion of additives or by intercalation of AB in a solid scaffold. Benedetto and co-workers found that AB samples doped or milled with Pt (ca. 1%) had a greater extent of H2 release at low temperatures (23% increase in H2 release at 140 °C).95 Autrey and co-workers found that a nanocomposite of mesoporous silica and AB (1 : 1 by weight) releases hydrogen at 50 °C with a half-reaction time of 85 min compared to a half-reaction time of 290 min at 80 °C for neat ammonia borane.96 The peak dehydrogenation temperature was lowered from ∼110 °C to ∼98 °C when a heating rate of 1 °C min−1 was used. Encapsulation of AB in a 24 wt% carbon cryogel97 decreased the peak dehydrogenation temperature to ∼90 °C, and there was no further decomposition at higher temperatures. Volumetric measurements indicated a 9 wt% loss of hydrogen, and no borazine formation was detected (MS).
The mechanism(s) by which the solid scaffolds increase the rate may be similar for both cases. It is possible that the observed effect may be a function of increasing the surface area of AB, as it is intercalated in nano-scale pores, which is known to lower the phase transition temperature and thereby presumably the dehydrogenation temperature. Another possibility is that dehydrogenation of AB is catalysed by the exposed functional groups (SiOH for silica and carboxylic acid for carbon cryogel) on the nanocomposite. Acid catalysed dehydrogenation of AB is well known (see below). Both mechanisms are consistent with the observation that smaller pore sizes reduce the decomposition temperature.
Scheme 12 A Lewis-acidic [H2BNH3]+ molecule interacts with ammonia borane to lose hydrogen and form a new compound that is capable of attack at two positions. |
Catalyst (mol%) | Substrate | Conditions | Products | Eq. of H2 | Ref. | |
---|---|---|---|---|---|---|
a Inferred from reported TOF values.b CTB is cyclotriborazane.c NR is “not reported.”d Yield of products not quantified; other products possible.e Isolated yields, actual yield will be higher but other products detected.f κ3-2,6-[OP(t-Bu)2]2C6H3.g Enders’ carbene: (1,3,4-triphenyl-4,5-dihydro-1H-1,2,4-triazol-5-ylidene).h IDipp is 1,3-bis(2,6-diisopropylphenyl)-1,3-dihydro-2H-imidazol-2-ylidene. | ||||||
1 | Cp2TiMe2 (0.5%) | HMe2NBH3 | 16 h, 25 °C | No reaction | 0 | 106 |
2 | Cp2Ti (2%) | HMe2NBH3 | 4 h, 20 °C | (Me2NBH2)2 | 1 | 110 |
3 | Cp2Ti (2%) | H(i-Pr)2NBH3 | 1 h, 20 °C | iPr2NBH2 | 1 | 110 |
4 | {[Cp(SiMe3)2]2Ti}N2 (2%) | HMe2NBH3 | 7 min, 23 °Ca | (Me2NBH2)2 | 1 | 111 |
5 | {[Cp(SiMe3)2]2Ti}N2 (2%) | H3NBH3 | 161 h, 65 °Ca | CTBb, borazine | NRc | 111 |
6 | [indenyl-(SiMe3)2]2Zr | HMe2NBH3 | 147 h, 65 °Ca | (Me2NBH2)2 | 1 | 111 |
7 | [P(iPr)3]2Br2(CH3CN)(NO)Re (1%) | HMe2NBH3 | 4 h, 85 °C | (Me2NBH2)2 | 1 | 105 |
8 | Ru3(CO)12 (0.2%) | H3NBH3 | 85 h, 60 °C | BN1.13H4.7 (elemental analysis) | NR | 103 |
9 | Ru3(CO)12 (0.1%) | Me3NBH3, PrNH2 | 32 h, 60 °C | [–N(Pr)B(H)–]3 (57%) | NR | 103 |
10 | Ru3(CO)12 (0.1%) | Me3NBH3, MeNH2 | 9.5 h, 60 °C | [–B(NMeH)N(Me)–]3, B(NHMe)3d | NR | 103 |
11 | trans-RuMe2(PMe3)4 (0.5%) | HMe2NBH3 | 16 h, 25 °C | (Me2NBH2)2 | 1 | 106 |
12 | FeH(PMe2CH2)(PMe3)3 (9%) | H3NBH3 | 96 h, 25 °C | CTB, borazine, polyborazylened | NR | 108 |
13 | [Rh(1,5-cod)(μ-Cl)]2 (0.5%) | HMe2NBH3 | 8 h, 25 °C | (Me2NBH2)2 | 1 | 106 |
14 | [Rh(1,5-cod)(μ-Cl)]2 (5%) | HMe2NBH3 | <2 h, 25 °C | (Me2NBH2)2 | 1 | 106 |
15 | RhCl3 (0.5%) | HMe2NBH3 | 22.5 h, 25 °C | (Me2NBH2)2 (90%) | 0.9 | 106 |
16 | HRh(CO)(PPh3)3 (0.5%) | HMe2NBH3 | 160 h, 25 °C | (Me2NBH2)2 (5%) | 0.05 | 106 |
17 | [Cp*Rh(μ-Cl)Cl]2 (0.5%) | HMe2NBH3 | 112 h, 25 °C | (Me2NBH2)2 | 1 | 106 |
18 | [Rh(1,5-cod)(μ-Cl)]2 (0.5%) | H(1,4-C4H8)NBH3 | 24 h, 25 °C | [(1,4-C4H8)NBH2]2 (73%)e | NR | 106 |
19 | [Rh(1,5-cod)(μ-Cl)]2 (0.5%) | HMe(PhCH2)NBH3 | 24 h, 25 °C | [Me(PhCH2)NBH2]2 (79%)e | NR | 106 |
20 | [Rh(1,5-cod)(μ-Cl)]2 (1%) | H2MeNBH3 | ∼60 h, 45 °C | (MeNBH)3 (40%)e | NR | 106 |
21 | [Rh(1,5-cod)(μ-Cl)]2 (0.6%) | H2PhNBH3 | 16 h, 45 °C | (PhNBH)3 (56%)e | NR | 106 |
22 | [Rh(1,5-cod)(μ-Cl)]2 (0.6%) | H3NBH3 | ∼60 h, 45 °C | Borazine (10%),e PIB, polyborazylene | NR | 106 |
23 | [Rh(1,5-cod)(μ-Cl)]2 (1%) | HiPr2NBH3 | 24 h, 25 °C | (iPr)2NBH2 (49%)e | NR | 106 |
24 | [Ir(1,5-cod)(μ-Cl)]2 (0.5%) | HMe2NBH3 | 136 h, 25 °C | (Me2NBH2)2 (95%) | 0.95 | 106 |
25 | (POCOPf)Ir(H)2 (0.5%) | H3NBH3 | 14 min, 20 °C | Cyclopentaborazane | 1 | 113 |
26 | Ni(1,5-cod)2, 2 NHCg (9%) | H3NBH3 | 3 h, 60 °C | Polyborazylened | 2.8 | 108 |
27 | Pd/C | HMetBuNBH3 | 1 h, 120 °C | [MetBuNBH2]2 | 1 | 104 |
28 | Pd/C (0.5%) | HMe2NBH3 | 68 h, 25 °C | (Me2NBH2)2 (95%) | 0.95 | 106 |
29 | (IDipp)hCuCl (12.5%) | HMe2NBH3 | 24 h, 20 °C | (Me2NBH2)2d | NR | 108 |
Under the heavily reducing conditions of amine borane dehydrogenation, the metal complex catalyst precursor will often undergo changes. Frequently, the active species is much different than the precatalyst. Manners and co-workers found that [Rh(1,5-cod)(μ-Cl)]2 catalyses the dehydrogenation of a variety of amine boranes at room temperature or with mild heating (Table 3; 13, 14, 18–23).106 The analogous Ir precursor or Rh precursors with different supporting ligands exhibited much lower activity for HMe2NBH3 (DMAB) dehydrogenation (Table 3; 15–17, 24). The dehydrogenation of DMAB using [Rh(1,5-cod)(μ-Cl)]2 exhibits an induction period, during which a black, opaque suspension forms. TEM analysis indicated Rh aggregation; the UV-Vis spectrum was similar to the spectrum of Rh colloids; addition of Hg (either at the onset, or during the reaction progress) resulted in complete loss of activity; and although the dark powder isolated from catalysis still had activity, the solution after filtration had almost no activity. These observations all point to Rh(0) colloids as the catalytically-active species. However, subsequent in situ EXAFS (extended X-ray absorption fine structure) analysis found that the same catalytic precursor, under different conditions, may form soluble Rh clusters that also catalyse this reaction.107 These Rh4–6 clusters, observed in solution during the reaction, eventually precipitate, likely due to a ligand exchange process with the formed products. The clusters can be redissolved by treatment with DMAB. The process of forming colloids or clusters can be complicated, and minor variations in conditions can have a profound influence on metal species development. However, it is clear in both cases that the precatalyst is drastically altered during the reaction.
Minor alterations to supporting ligands can also greatly influence the catalytic activity. Baker and co-workers measured the relative catalytic activity of N-heterocyclic carbene (NHC) complexes of Ni.108 The Enders’ carbene Ni complex was found to be 11.5 times faster than the IDipp complex and 8.8 times faster than the IMes complex.109 Also, the Enders’ Ni complex was 4.1 times faster than a Rh(NHC) complex and 1.9 times faster than a Ru(NHC) complex. The Enders’ carbene Ni complex has the largest extent of dehydrogenation yet seen (>2.5 eq.) but requires mild heating. Initially, a minor amount of borazine is formed. However, borazine reacts further by crosslinking reactions to form polyborazylene. Using borazine as the substrate under similar catalytic conditions to AB results in almost no activity, indicating that AB either activates the catalyst or is involved in the crosslinking reactions. During the course of the reaction a dark, homogeneous maroon solution forms. Hg addition results in no loss of activity, which is indicative that metal colloids are not the active catalyst. A kinetic isotope effect (KIE) is observed for D3NBH3, H3NBD3, and D3NBD3 (2.3, 1.7, and 3.0, respectively) indicating that both N–H and B–H bond cleavage are involved in the turnover limiting step or that N–H and B–H bond cleavage steps have similar rates.
Solvent and substrate can also play a significant role. An example of this was noted in the titanocene-based dehydrogenation of amine boranes initially reported by Manners and co-workers (Table 3; 2, 3)110 and extended by Chirik and co-workers to include other Cp-based ligands and Zr (Table 3; 4–6).111 Chirik and co-workers noted that {[η5-C5H3(SiMe3)2]2Ti}N2 has a TOF of >420 h−1 in benzene-d6 and 0.29 h−1 in THF for the dehydrogenation of DMAB. Also, AB was found to have a much slower rate than DMAB (Table 3; 4 and 5).
Finally, the catalyst identity controls the extent of dehydrogenation. Heinekey, Goldberg and co-workers reported that (POCOP)IrH2112 is an extremely active catalyst for AB dehydrogenation (Table 3; 25).113 Unfortunately, only a single equivalent of hydrogen is released per equivalent of AB. During the course of the reaction, an insoluble colorless precipitate is formed. The X-ray powder diffraction and IR data agree closely with that previously reported for cyclopentaborazane, [H2NBH2]5.114 However, Manners et al. found that alkylamine boranes, and mixtures of alkylamine boranes and AB under similar conditions gave soluble aminoborane polymers.115 The measured wide angle X-ray scattering pattern and the IR for the white precipitate from the (POCOP)IrH2 catalysed dehydrogenation of AB were different from that reported for [H2NBH2]5. They suggested that the white precipitate may be polymeric in nature similar to the products formed from alkylamine borane dehydrogenation. Although the actual nature of the precipitate has not yet been completely established, it is clear from the solid state 11B NMR data (−18 ppm) and the measured amount of hydrogen released that an [H2NBH2]n product is formed.
The mechanisms of metal-catalysed dehydrogenation have been investigated by computational methods for the titanocene system reported by Manners, the (POCOP)IrH2 system reported by Goldberg and Heinekey, and the Ni(NHC)2 system reported by Baker. Although the relative energies of intermediates are different, the overall reaction pathways are similar. In the initial step, B–H coordinates to the metal complex. In the titanocene case, the N–H is activated followed by hydride transfer from B–H (Scheme 13).116 Two mechanisms were evaluated in the (POCOP)IrH2 case. The first follows generation of monovalent (POCOP)Ir with a concerted B–H and N–H bond activation at the IrI centre. The second one involves a concerted B–H and N–H bond activation at trivalent (POCOP)IrH2 (Scheme 14). In the second mechanism, a hydride ligand acts as a proton acceptor yielding pentavalent (POCOP)IrH4.117 In the Ni(NHC)2 case, N–H deprotonation is proposed to occur at the Ni-bound NHC carbon, forming a coordinated imidazolium-type ligand (Scheme 15).118 The imidazolium subsequently protonates the Ni centre and hydrogen formation follows. The proposed mechanism is not consistent with the observed KIE, so further investigation is warranted.
Scheme 13 Mechanism of TiCp2 catalysed dehydrogenation of Me2HNBH3 as proposed by Luo and Ohno.116 Gibbs free energies corrected for toluene (CPCM). |
Scheme 15 Simplified partial mechanism for NHC2Ni catalysed dehydrogenation of AB. (i) Protonation of an NHC ligand. (ii) Transfer of a proton to metal centre. (iii) Formation of hydrogen. |
All mechanisms proposed to date are focused on the initial loss of hydrogen from amine boranes. Establishing the role of the metal complex in subsequent oligomerisation and loss of the second equivalent of hydrogen will also be very important.
Scheme 16 Solvolysis and subsequent regeneration of ammonia borane. |
The method mentioned above by Ramachandran and co-workers could potentially be used to regenerate ammonia borane. However, the generation of strong B–O bonds in the reaction pathway will likely limit overall efficiency. Alternatively, Sneddon and co-workers102 and Mertens and co-workers119 have independently developed reduction schemes that form B–Br and B–Cl bonds, respectively.
Sneddon and co-workers reported that spent BNHx fuel was successfully digested using HBr/AlBr3 (super-acid) in CS2 to form H2, NH4Br, BBr3 as well as [H2NBBr2]3. The relative ratio of BBr3 to [H2NBBr2]3 depends on the material being digested. Mertens and co-workers treat a THF solution of spent fuel with an ether solution of HCl to generate BCl3, NH4Cl and H2. Both aminoborane [(BH2NH2)x] and iminoborane [(BHNH)x] materials were successfully digested. Unfortunately, the yields of BCl3 were low due to decomposition in THF. Switching to a similar super-acid solution that Sneddon and co-workers used increases the yield of BCl3 to >60%. BCl3 is difficult to directly hydrodechlorinate and reduction by hydrogen requires high temperatures (600–700 °C) to yield the partially reduced product, BHCl2 (which must be removed from the side-product HCl and can subsequently disproportionate into BCl3 and B2H6). However, addition of a Lewis-base such as NMe3 reduces the hydrodechlorination temperature to 200 °C (but still requires high pressures of 2000 atm).120 Unfortunately, these conditions are energetically costly, and the yield is poor (25%). However, a similar concept can be used for reduction of BX3 compounds by chemical hydrides. Another advantage offered by a Lewis-base is that it eliminates formation of B2H6, a hazardous material. Thus, Sneddon and co-workers treat BBr3 with N,N′-diethylaniline, which yields a compound easily reduced by triethylsilane under mild conditions. Mertens and co-workers found that stronger bases such as NEt3, inhibit the reduction of BCl3 by triethylsilane and MgH2. Addition of a weaker base, NPh3, allows for the complete reduction of Ph3NBCl3 by MgH2 after 20 minutes at 80 °C. The final step is displacement of R3N with ammonia, to yield H3NBH3.
In a DOE progress report regarding Los Alamos National Laboratory’s effort toward BNHx-spent fuel processing, effective digestion of polyborazylene with 1,2-benzenedithiol was demonstrated to form ammonia adducts of dithioboron compounds.121 These compounds contain relatively weak B–S bonds that are readily reduced by Sn–H. Optimisation of reaction conditions and energy efficiency are still being developed, but this is an intriguing result.
Burrell and co-workers synthesised Ca(NH2BH3)2 by addition of AB to CaH2 in THF.124 A THF adduct is formed, but the THF can be removed in vacuo. While this compound is reported to lose hydrogen at 90 °C, only <0.3 equivalents of H2 are released. Slowly ramping the temperature to 170 °C results in 3.6 equivalents of H2 released (corresponding to 7.2 material wt%) with <0.1% ammonia and borazine released.
In addition to expanding the range of metals used in metal amidoborane complexes, the role of dopants or catalysts in controlling dehydrogenation, and possibly rehydrogenation, needs to be explored.
Scheme 17 Calculated energy of dehydrogenation for 1,2-azaboracyclohexane. |
Footnotes |
† Part of the renewable energy theme issue. |
‡ Dedicated to Prof. M. Frederick Hawthorne on the occasion of his 80th birthday. |
This journal is © The Royal Society of Chemistry 2009 |