Alejandra
Gomez-España
ab,
Jorge L.
Lopez-Morales
a,
Belinda
Español-Sanchez
a,
Pilar
García-Orduña
a,
Fernando J.
Lahoz
a,
Manuel
Iglesias
a and
Francisco J.
Fernández-Alvarez
*a
aDepartamento de Química Inorgánica – Instituto de Síntesis Química y Catálisis Homogénea (ISQCH). Universidad de Zaragoza. Facultad de Ciencias 50009, Zaragoza, Spain. E-mail: paco@unizar.es
bUniversidad Pedagógica Nacional Francisco Morazán-UPNFM, 11101, Tegucigalpa, Honduras
First published on 26th April 2023
The iridium(III) complexes [Ir(H)(Cl)(κ2-NSitBu2)(κ2-bipyMe2)] (2) and [Ir(H)(OTf)(κ2-NSitBu2)(κ2-bipyMe2)] (3) (NSitBu2 = {4-methylpyridine-2-yloxy}ditertbutylsilyl) have been synthesized and characterized including X-ray studies of 3. A comparative study of the catalytic activity of complexes 2, 3, [Ir(H)(OTf)(κ2-NSitBu2)(coe)] (4), and [Ir(H)(OTf)(κ2-NSitBu2)(PCy3)] (5) (0.1 mol%) as catalysts precursors for the solventless formic acid dehydrogenation (FADH) in the presence of Et3N (40 mol%) at 353 K has been performed. The highest activity (TOF5 min ≈ 3260 h−1) has been obtained with 3 at 373 K. However, at that temperature the FTIR spectra show traces of CO together with the desired products (H2 and CO2). Thus, the best performance was achieved at 353 K (TOF5 min ≈ 1210 h−1 and no observable CO). Kinetic studies at variable temperature show that the activation energy of the 3-catalyzed FADH process is 16.76 kcal mol−1. Kinetic isotopic effect (5 min) values of 1.6, 4.5, and 4.2 were obtained for the 3-catalyzed dehydrogenation of HCOOD, DCOOH, and DCOOD, respectively, at 353 K. The strong KIE found for DCOOH and DCOOD evidenced that the hydride transfer from the C–H bond of formic acid to the metal is the rate-determining step of the process.
To the best of our knowledge, the first studies on the potential of the catalytic formic acid dehydrogenation (FADH) to supply hydrogen to fuel cells were independently reported by Beller et al.3 and Laurenczy et al.4 in 2008. Since then, many examples of catalytic systems active for the FADH have been published.1,2 The most active catalytic systems for FADH so far reported are based on water soluble Ir–Cp* species with functionalized bipyridine or biimidazoline derivatives as ligands.5–9 Among them, the species [IrClCp*(2,2′-bi-2-imidazoline)]Cl (TOF ≈ 487500 h−1),6 the iridium-bipyridine catalysts described by Fujita and Himeda et al. (TOF ≈ 228
000 h−1),5 and the DMSO soluble Ir–Cp* species reported by Albrecht el al. (TOF ≈ 300
000 h−1)10 stand out.
On the other hand, one of the aims of our research group is to study the potential of iridium(III) complexes with pyridine-2-yloxy-silyl ligands (Ir-NSi) as homogenous catalysts.11–13 These species have been successfully used as CO211 or formamide12a hydrosilylation catalysts. Ir-NSi complexes are characterized by their short Ir–Si bond distances (in the range 2.25–2.28 Å),14 which has been explained by assuming a significant ionic contribution to the covalent bond,12b,15 and the strong trans effect exerted by the silicon atom. Theoretical calculations have shown that the presence of the silicon play a key role in the reactivity of iridium-formate intermediates in catalytic CO2 hydrosilylation11 and FADH processes.16 A challenge when using Ir-NSi complexes as FADH catalysts is that under the reaction conditions the active species can be reduced to inactive iridium nanoparticles.16 Therefore, with the purpose of preparing iridium(III)-NSi complexes stable under FADH conditions, we decided to use the monoanionic bidentate ligand (4-methylpyridine-2-yloxy)ditertbutylsilyl (NSitBu2), where the Ir–Si bond is sterically protected by the bulk of the two tert-butyl substituents on the silicon atom.
An additional difficulty when using homogeneous transition metal catalysts with silyl-based ligands in protic solvents is the breaking of the Ir–Si bond, which is favored in the presence of a base.17 Indeed, the hydrolysis of the Ir–Si bond in Ir-NSi species is favoured in basic-media, moreover the coordination of water to unsaturated Ir-NSi species has been recently reported.12b Thus, we decided to explore the potential of electronically and sterically saturated Ir–Si species as FADH catalyst in the absence and in presence of water. In this regard, it should be mentioned that examples of catalytic systems effective for catalytic FADH under neat conditions are scarce.16,18,19
The Ir-(κ2-NSitBu2) species 2 and 3 have been characterized by means of multinuclear NMR spectroscopy. The 1H NMR of 2 and 3 in CD2Cl2 show a singlet resonance corresponding to the Ir–H at δ −18.03 and −17.53 ppm, respectively. These values are low field shifted with respect to that observed for 1 (−20.68 ppm), 4 (−27.46 ppm) and 5 (−29.21 ppm). The 1H–29Si HMBC NMR spectra show the resonance due to the silicon atom at δ 46.8 (2) and 41.0 (3), which compare well with the value found for the unsaturated species 1 (δ 41.0),12a4 (δ 45.8),12a and 5 (δ 44.5).12b19F{1H} NMR spectra of 3 (at 298 K) in CD2Cl2 show a sharp resonance at δ −78.82. Considering that 19F{1H} NMR spectra of free TfO− in CD2Cl2 (298 K) show a singlet resonance at δ −79.0,20 the value found for 3 suggests a weak Ir–OTf bond.12b,20
In order to attain a deeper understanding about the metal coordination sphere, the solid-state structure of compound 3 has been determined by single crystal X-ray diffraction, using synchrotron radiation. Selected geometrical parameters are reported in Table 1. The metal atom exhibits a distorted octahedral geometry, with a κ2-Si,N and a κ2-N′,N′′ coordination of (NSitBu2) and bipyMe2, respectively, the hydride and an oxygen atom of the triflate fragment. The Ir–Si and Ir–N(1) bond lengths have been found to be slightly shorter than those reported in compound 1 (2.2853(6) and 2.0947(18) Å, respectively).12a Indeed, our previous studies have already revealed that the substitution of the chloride by a triflate ligand (which is a more electron-withdrawing group), reinforce the Ir–Si bond.12b On the contrary, the Ir–O(2) bond length in 3 (2.381(4) Å), with the oxygen trans to the silicon, is in the upper limit of Ir–O bond lengths reported in Ir–OTf fragments (in the 2.04–2.40 Å range),21 indicating a weak bonding, in good agreement with the aforementioned 19F{1H} NMR spectra of 3.
Ir–Si | 2.2731(12) | O(2)–Ir–N(1) | 91.53(16) |
Ir–O(2) | 2.381(4) | O(2)–Ir–N(2) | 86.98(16) |
Ir–N(1) | 2.063(4) | O(2)–Ir–N(3) | 75.89(15) |
Ir–N(2) | 2.044(4) | O(2)–Ir–H | 94(2) |
Ir–N(3) | 2.148(4) | N(1)–Ir–N(2) | 175.12(15) |
Ir–H | 1.53(7) | N(1)–Ir–N(3) | 96.75(16) |
Si–Ir–O(2) | 171.94(13) | N(1)–Ir–H | 83(3) |
Si–Ir–N(1) | 81.92(12) | N(2)–Ir–N(3) | 78.38(16) |
Si–Ir–N(2) | 99.92(12) | N(2)–Ir–H | 102(3) |
Si–Ir–N(3) | 109.42(11) | N(3)–Ir–H | 170(3) |
Si–Ir–H | 81(2) |
The results of these experiments show that complex 3 (TOF5 min = 1210 h−1) is a more effective catalyst precursor than 2 (TOF5 min = 900 h−1) (Fig. 2), and both precursors are more active than [Ir(H)(OTf)(κ2-NSitBu2)(coe)] (4) (TOF5 min = 600 h−1) and/or [Ir(H)(OTf)(κ2-NSitBu2)(PCy3)] (5) (TOF5 min = 60 h−1) (Fig. 2). The systems based on 4 and 5 show the decomposition of the catalyst to give iridium nanoparticles, in a similar fashion to that previously observed for the related Ir-(κ2-NSiMe2)2 species.16 Conversely, the formation of iridium nanoparticles was not observed when using 2 or 3. These results show that the use of coordinatively saturated catalyst precursors prevents the reduction of iridium(III) and encouraged us to study the performance of 3 as catalyst for FADH.
![]() | ||
Fig. 2 TON versus time (min) from the 2, 3, 4 or 5 catalyzed (0.1 mol%) solventless dehydrogenation of FA-Et3N adduct (Et3N 40 mol%) at 353 K. The gas evolution was measured using a man on the moon™ reactor22 (H2: CO2 = 1![]() ![]() |
Subsequently, we have studied the influence of the catalyst loading on the catalytic performance of 3. The activity of the 3-catalyzed FADH in presence of Et3N (40 mol%) depends on the catalyst loading, thus using a 0.05 mol%, instead of 0.1 mol%, a reduction of the activity was observed (TOF5 min = 820 h−1; Fig. S14†). Therefore, we decided to use a 0.1 mol% loading in the following studies.
Once the best catalyst precursor, 3, was chosen and the catalyst loading (0.1 mol%) optimized, we decided to study the effect of temperature on the performance. Thus, we have studied the catalytic FADH using 3 (0.1 mol%) as catalyst precursor in the presence of an initial concentration of Et3N of 40 mol% at different temperatures (Fig. 3). These studies revealed that, as expected, the temperature produces a positive effect on the activity of the reaction (Fig. 3) and allowed us to determinate the initial reaction rates (TOF5 min) at 323, 333, 343, 353, 363 and 373 K (Table S16†). The Arrhenius plot for these data23 yields an apparent activation energy of 16.76 ± 1.72 kcal mol−1, which is lower than that found for the related [Ir(CF3CO2)(κ2-NSiMe2)2] species (27.5 kcal mol−1)16 and agrees with the greater activity of 3 in comparison to that found for [Ir(CF3CO2)(κ2-NSiMe2)2], under the same reaction conditions (Table 2).
![]() | ||
Fig. 3 TON versus time (min) from the 3-catalyzed (0.1 mol%) solventless dehydrogenation of FA-Et3N adduct (Et3N 40 mol%) at different temperatures. The gas evolution was measured using a man on the moon™ reactor22 (H2![]() ![]() ![]() ![]() |
Catalyst | T (K) | TOF (h−1)/(time) | Ref. |
---|---|---|---|
a sodium formate instead FA-Et3N (5![]() ![]() |
|||
4 | 353 | 600/(5 min) | This work |
5 | 353 | 60/(5 min) | This work |
2 | 353 | 900/(5 min) | This work |
3 | 353 | 1210/(5 min) | This work |
3 | 373 | 3260/(5 min) | This work |
[Ir(CF3CO2)(κ2-NSiMe2)2] | 373 | 2900/(5 min) | 16 |
[Ir(CF3CO2)(κ2-NSiMe2)2] | 353 | 600/(5 min) | 16 |
[Mn(CO)2(tBuPNNOP)] | 353 | 8500/(3 min) | 24 |
[RuCl2(PPh3)3] | 313 | 400/(2 h) | 3 |
[Ir(COD)(NPtBu)][TfO]![]() |
363 | 3000![]() |
18 |
The activity of the catalytic system 3/Et3N (40 mol%) as FADH catalyst (373 K; TOF5 min = 3260 h−1) is higher than that reported for the iridium(III) complexes [Ir(CF3CO2)(κ2-NSiMe2)2] (373 K; TOF5 min = 2900 h−1)16 and [Ir(COD)(NPtBu)][TfO] (363 K; TOF5 min = 3000 h−1)18 but lower than that reported for the manganese compound [Mn(CO)2(tBuPNNOP)] (353 K; TOF5 min = 8500 h−1)24 (Table 2) and for the iridium(III) species reported by Fischmeister et al. (TOF ≈ 13300 h−1),19a Iglesias et al. (TOF ≈ 11
600 h−1)19b and Gelman et al. (TOF ≈ 11
800 h−1).19c
FTIR studies of the gases resulting from these 3-catalyzed reactions evidenced that the selectivity of the catalytic process depends on the temperature. Thus, while at 353 K, the formation of CO was below the detection limit of the FTIR (3 ppm) and, therefore, the selective formation of H2 and CO2 and residual Et3N was observed (Fig. 4), the FTIR spectra of the gases obtained from the reactions at 373 K shows the presence of traces of CO (Fig. S17†). It is known that the dehydration of neat FA to form H2O and CO is favored at high temperatures.25 Therefore, it is reasonable to assume that the traces of CO observed at 373 K may be formed by thermal, uncatalyzed decomposition pathways.26
![]() | ||
Fig. 4 FTIR of the gas resulting from the solventless 3-catalyzed (0.1 mol%) FADH in presence of Et3N at 353 K. |
Kinetic isotope experiments on the 3-catalyzed FADH were performed at 353 K using 40 mol% of Et3N (Table 3 and Fig. 5). The results from these studies show that the initial TOF values (calculated after 5 min) dropped from 1210 to 770, 270 and 290 h−1 when HCOOH was replaced by HCOOD, DCOOH and DCOOD, respectively (Table 3). These TOF5 min values show a high kinetic isotopic effect (KIE) for DCOOH and DCOOD of 4.5 and 4.2, respectively (Table 3, entries 3 and 4), which evidenced that the hydride transfer from the CH of FA to the metal leading to CO2 is the rate-determining step of the process.26 Moreover, the KIE value (1.6) obtained when using HCOOD show a secondary KIE effect, analogous to that found for the related Ir-(κ2-NSiMe2)2 species (Table 3, entry 2).16
![]() | ||
Fig. 5 TON versus time (min) from the 3-catalyzed (0.1 mol%) solventless dehydrogenation of HCOOH, HCOOD, DCOOH and DCOOD in presence of Et3N 40 mol% at 353 K. The gas evolution was measured using a man on the moon™ reactor.22 |
In all the studied 3-catalyzed (0.1 mol%) dehydrogenation of FA-Et3N (Et3N 40 mol%) reactions, once the gas evolution ends a blue residue remains in the reactor. 1H NMR spectra (DMSO-d6) of these blue residues show the presence of triethylammonium salts, a major component of the mixture, together with several unidentified Ir–H species. 1H–29Si HMBC spectra shows three different silicon resonances (Fig. S19†). Two of them correspond to compounds with tBu2Si groups not bonded to Ir (29Si{1H} NMR; δ −14.11 and −22.85 ppm), but the remaining resonance is due to a complex with an Ir–Si bond (29Si{1H} NMR; δ 45.11) and two inequivalent tBu substituents (Fig. 6).
![]() | ||
Fig. 6 1H–29Si HMBC spectrum DMSO-d6 (400 MHz, 298 K) of the blue residue from the solventless 3-catalyzed (0.1 mol%) FADH in presence of Et3N (40 mol%) at 353 K. |
The addition of a second load of FA (50 μL) to this blue residue at 353 K evidenced that it catalyzed FADH. However, a decrease of the activity (TOF5 min ≈ 940 h−1) was observed (Fig. 7). This demonstrates that, although the use of 4,4′-dimethylbipyridine as ancillary ligand somehow protects the Ir–Si bond, the partial deactivation of the active species still occurs. It should be mentioned that the blue-residue is still active after 24 h (TOF5 min ≈ 270 h−1) (Fig. S15†).
![]() | ||
Fig. 7 TON versus time (min) from the 3-catalyzed (0.1 mol%) of FA (250 μL) in presence of Et3N 40 mol% or the blue-residue catalyzed solventless dehydrogenation of HCOOH (50 μL) at 353 K. The gas evolution was measured using a man on the moon™ reactor.22 |
Therefore, the catalytic system based on 3, with bipyMe2 as auxiliary ligand, is more active (Table 2) and stable than [Ir(CF3CO2)(κ2-NSiMe2)2].16 This encouraged us to study its performance as FADH catalyst in an aqueous medium. These studies show that initially the system based on 3 (0.1 mol%), in presence of Et3N (40 mol%) at 353 K, is slightly more active in water solution (TOF5 min = 1500 h−1) than under solventless conditions. However, after 15 min of reaction catalyst deactivation is observed (Fig. 8).
![]() | ||
Fig. 8 TON versus time (min) from the solventless 3-catalyzed (0.1 mol%) of FA (250 μL) in presence of Et3N 40 mol% (blue) at 353 K or 3-catalyzed (0.1 mol%) of FA (250 μL)/H2O (250 μL) in presence of Et3N 40 mol% at 353 K. The gas evolution was measured using a man on the moon™ reactor.22 |
All reactions and manipulations were carried out under an argon atmosphere by using Schlenk-type techniques or in a Glovebox-MBraun UNIlab. Organic solvents were dried by standard procedures and distilled under argon prior to use or obtained oxygen- and water-free from a Solvent Purification System (Innovative Technologies). 1H, 13C, 29Si, 31P and 19F NMR spectra were obtained on a Bruker AV-300, AV-400 or AV-500 spectrometer using TMS as the internal reference in CD2Cl2, or DMSO-d6 as solvent. All chemical shifts (δ) are reported in ppm and coupling constants (J) are reported in Hz to apparent peak multiplets. 1H–1H-COSY, 13C-APT, 1H/13C HSQC, 1H/13C HMBC and 1H/29Si HMBC sequences were used for help in the assignments of the 1H, and 13C{1H} spectra. All catalytic experiments have been reproduced a minimum of three times.
Kinetic studies at variable temperature show that the activation energy of the 3-catalyzed FADH process is 16.76 kcal mol−1. KIE values of 1.6, 4.5, and 4.2 were obtained for the 3-catalyzed dehydrogenation of HCOOD, DCOOH, and DCOOD, respectively, at 353 K. The strong KIE found for DCOOH, and DCOOD (>4.0) evidenced that the activation of the C–H bond of FA is the rate-determining step of the process.
In conclusion, the use of the ligand κ2-NSitBu2 with two tert-butyl substituents on the silicon atom and 4,4′-dimethylbipyridine as ancillary ligand enhances the catalytic performance of Ir-NSi species as FADH catalyst precursors under solventless conditions. However, their use in an aqueous medium is hampered due to the short life of the catalyst under these conditions.
Footnote |
† Electronic supplementary information (ESI) available. CCDC 2247182 for compound 3. For ESI and crystallographic data in CIF or other electronic format see DOI: https://doi.org/10.1039/d3dt00744h |
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