Highly eﬃcient hydrogen generation from formic acid using a reduced graphene oxide-supported AuPd nanoparticle catalyst †

Highly dispersed AuPd alloy nanoparticles have been successfully immobilized on reduced graphene oxide (rGO) using a facile non-noble metal sacrificial method, which exhibit the highest activity at 323 K (turnover frequency, 4840 h (cid:2) 1 ) for hydrogen generation without CO impurity from the formic acid/sodium formate system.

Hydrogen is of critical importance in clean energy applications although effective hydrogen storage technologies still need to be developed. 1 Formic acid (FA) is a promising hydrogen carrier, 2 which has several remarkable features such as (a) nontoxicity with high hydrogen content (4.4 wt%), (b) high stability as a liquid at room temperature, and (c) easy synthesis via a biomass process, CO 2 reduction or methyl formate hydrolysis. 3 Depending on the catalysts, however, FA can be decomposed in two ways: desirable dehydrogenation (HCOOH -H 2 + CO 2 ) and undesirable dehydration (HCOOH -H 2 O + CO), which produces CO impurities that are toxic to the fuel cell catalysts. 4 So far, homogeneous catalysts have been extensively studied for hydrogen production from FA and very high catalytic activities have been reported. 5 Along with the ongoing progress in FA dehydrogenation using homogeneous systems, heterogeneous catalysts have attracted tremendous attention due to their advantages of easy separation and recycling. A large number of metal nanoparticle (MNP) catalysts have been studied, most of which, however, suffer from severe aggregation and limited catalytic activities. 6 Herein, we report a highly active AuPd alloy nanoparticle catalyst prepared using a non-noble metal sacrificial approach (NNMSA), which exhibits the highest turnover frequency (TOF) of 4840 h À1 at 323 K for hydrogen generation from the FA/sodium formate (SF) system. 7 Cobalt was used as the sacrificial agent. Amorphous Co 3 (BO 3 ) 2 was formed from the reaction between Co(CH 3 COO) 2 and NaBH 4 , which can be easily dissolved in H 3 PO 4 ( Fig. S1 and S2, for details see the ESI †). 8 Graphite oxide (GO) was prepared from graphite using a modified Hummers' method. 9 The rGO-supported AuPd nanoparticle (NP) catalyst was synthesized using a wet-chemical process, as illustrated in Scheme 1. Firstly, according to the stoichiometry, the aqueous solution containing HAuCl 4 , Co(CH 3 COO) 2 and K 2 PdCl 4 was added into 50 mL of GO suspension (0.1 wt%). Then the above mixture was reduced by a fresh aqueous solution of NaBH 4 . After continuous stirring for 2 h, the mixture was washed and re-dispersed in H 3 PO 4 solution for etching (2 h). Finally, the catalyst, denoted as (Co x ) E Au y Pd 1Ày /rGO (ESI †), was obtained by centrifugation and washing with water.
Scheme 1 Schematic illustration of the synthesis of the (Co x ) E Au y Pd 1Ày /rGO catalyst via a non-noble metal (cobalt) sacrificial approach (NNMSA).  Fig. 1b. Generally, the restacking of rGO can be partially overcome by the direct deposition of NPs. 11 Hence, the Au 0.6 Pd 0.4 /rGO and Co 3 Au 0.6 Pd 0.4 /rGO possess a type-IV N 2 sorption curve with Brunauer-Emmett-Teller (BET) surface areas of 189 and 219 m 2 g À1 , respectively. Notably, the surface area of (Co 3 ) E Au 0.6 Pd 0.4 /rGO (321 m 2 g À1 ) increases drastically, illustrating that the removal of cobalt by the acid etching has resulted in high porosity, which will favour the diffusion of reactants to metal NPs in catalysis.
The morphologies of the Au 0.6 Pd 0.4 /rGO, Co 3 Au 0.6 Pd 0.4 /rGO and (Co 3 ) E Au 0.6 Pd 0.4 /rGO catalysts were analysed by transmission electron microscopy (TEM). As shown in Fig. S4 and S5 (ESI †), Au 0.6 Pd 0.4 /rGO and Co 3 Au 0.6 Pd 0.4 /rGO possess larger particles with severe aggregation (ESI †). In contrast, the AuPd NPs in the (Co 3 ) E Au 0.6 Pd 0.4 /rGO catalyst are well dispersed and immobilized on the rGO support (Fig. 2a). The high-angle annular dark-field scanning transmission electron microscopy (HAADF-STEM) images further reveal the uniform distribution of AuPd NPs in the (Co 3 ) E Au 0.6 Pd 0.4 /rGO catalyst with an average particle size of 3.9 AE 0.9 nm (Fig. 2b and c), indicating that the sacrifice of the cobalt compound can prevent the primary AuPd NPs from aggregation, which will benefit their catalytic performance. Energy dispersive X-ray (EDX) analyses ( Fig. S6-S8, ESI †) show that Co 3 Au 0.6 Pd 0.4 /rGO is rich in cobalt, whereas no signals for cobalt are detected in (Co 3 ) E Au 0.6 Pd 0.4 /rGO, clearly confirming that cobalt has been eliminated by the H 3 PO 4 etching. The inductively coupled plasma optical emission spectroscopic analysis reveals that the molar ratio of Co : Au : Pd in (Co 3 ) E Au 0.6 Pd 0.4 /rGO to be 0.04 : 0.6 : 0.4, indicating that almost all the co-precipitated Co 3 (BO 3 ) 2 can be removed by H 3 PO 4 . The X-ray photoelectron spectroscopic (XPS) measurements show no signals for Co in (Co 3 ) E Au 0.6 Pd 0.4 /rGO before and after Ar sputtering (Fig. 3a). The observed Au 4f and Pd 3d spectra reveals that (Co 3 ) E Au 0.6 Pd 0.4 /rGO is composed of metallic Au and Pd ( Fig. 3b and c), further confirming the successful formation of AuPd alloy NPs.
The catalytic activities of the (Co x ) E Au y Pd 1Ày /rGO catalysts in hydrogen generation from the FA/SF system were evaluated. Fig. 4a shows the gas generation from the FA/SF system in the presence of (Co 3 ) E Au 0.6 Pd 0.4 /rGO and Au 0.6 Pd 0.4 /rGO. Unquestionably, the sacrificial agent plays a dominant role, by decreasing the size of NPs, in the promotion of catalytic performance. Under our evaluation conditions, the (Co 3 ) E Au 0.6 Pd 0.4 /rGO catalyst shows an extremely high catalytic activity for the complete dehydrogenation

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of FA with the release of 146 mL gas of H 2 + CO 2 in 0.62 min (n AuPd /n FA = 0.02 and n SF /n FA = 2.5) at 323 K, giving a TOF as high as 4840 h À1 (Fig. S9, ESI †), the highest value reported thus far (Table S1, ESI †). 7 After that, the generated gas with a slow speed is attributed to the decomposition of SF. The catalytic activities of the (Co 3 ) E Au 0.6 Pd 0.4 /rGO catalysts with lower metal loadings have not shown significant changes (Fig. S10, ESI †). Gas chromatography (GC) measurements demonstrate that the produced gas consists of H 2 and CO 2 without a trace of CO (below 5 ppm), implying that the as-synthesized (CO 3 ) E Au 0.6 Pd 0.4 /rGO catalyst has a high selectivity for the dehydrogenation of FA into H 2 and CO 2 (Fig. S11, ESI †). Such excellent catalytic performance for FA dehydrogenation can meet the requirements of practical applications. Herein, it should be noted that the molar ratio of SF/FA has an obvious influence on the gas release rate (Fig. S12, ESI †). The gas release rate increases rapidly until the molar ratio of SF/FA increases up to 2.5. The further increase, however, makes no actual impression on the FA decomposition. On the other hand, the catalytic performance of (Co 3 ) E Au y Pd 1Ày /rGO is affected by the molar ratio of Au/Pd (Fig. S13, ESI †). The mono-metallic (Co 3 ) E Au/rGO has no activity while (Co 3 ) E Pd/rGO has a low activity. However, the introduction of Au to Pd leads to a dramatically enhanced efficiency, which reaches its best value at n Au /n Pd = 6/4, indicative of the excellent synergistic effects between Au and Pd for FA decomposition. 12 Additionally, rGO is an excellent support for the catalysis, which is demonstrated by the quite low activities of their support-free counterparts (Fig. S14, ESI †).
Further, the increased hydrogen release rates from the FA/SF systems have been observed at elevated temperatures (Fig. S15, ESI †). The activation energy (E a ) in this process is calculated to be 39.77 kJ mol À1 , which is lower than most of the reported heterogeneous and homogeneous systems for FA dehydrogenation. 5,6d,7,13 After the catalytic reaction, the catalyst was recollected by centrifugation, washed with water and recycled for further use. As shown in Fig. 4b and Table S2 (ESI †), no significant loss in activity was observed over five cycles. The structure and  size distribution of metal NPs after the catalytic reactions have been found to be identical to those of the pristine catalyst ( Fig. S16 and S17, ESI †). In contrast, the CO poisoned (Co 3 ) E Au 0.6 Pd 0.4 /rGO, prepared by exposing the catalyst to a CO atmosphere showed no catalytic activity (Fig. S18, ESI †). It is clear that the (Co 3 ) E Au 0.6 Pd 0.4 / rGO catalyst possesses high selectivity, durability and stability during the FA dehydrogenation.
In conclusion, a (Co 3 ) E Au 0.6 Pd 0.4 /rGO catalyst has been synthesized using a simple non-noble metal sacrificial method. The obtained catalyst shows efficient catalytic activity for hydrogen generation from the FA/SF system with the highest TOF of 4840 h À1 at 323 K and possesses high selectivity, durability and stability over 5 cycles. It is believed that the way to the utilization of FA as a hydrogen carrier will be paved by the practical use of the presently provided catalyst.
The authors thank Dr Takeyuki Uchida for TEM measurements, and METI, AIST and Kobe University for financial support. X. C. Yang is grateful to the China Scholarship Council (CSC) and Ministry of Education, Culture, Sports, Science and Technology-Japan (MEXT) for a PhD scholarship.