Rachel E. Priestleya,
Alexander Mansfielda,
Joshua Byea,
Kevin Deplancheb,
Ana B. Jorgec,
Dan Brettc,
Lynne E. Macaskieb and
Surbhi Sharma*a
aCentre for Hydrogen and Fuel Cell Research, School of Chemical Engineering, University of Birmingham, Edgbaston, Birmingham, B15 2TT, UK. E-mail: s.sharma.1@bham.ac.uk
bUnit of Functional Bionanomaterials, School of Bioscience, University of Birmingham, Edgbaston, Birmingham, B15 2TT, UK
cUCL Chemical Engineering Department, Electrochemical Innovation Lab, Torrington Place, WC1E 7JE, London, UK
First published on 29th September 2015
A novel method for simultaneous reduction of graphene oxide (GO) and palladium salt, Pd(II), using Escherichia coli (E. coli) in the separate presence of two different mild reducing agents (hydrogen and formate) is investigated to successfully produce reduced GO (rGO)-biomass/Pd hybrid material for potential use as an electrocatalyst. Transmission electron microscopy, X-ray diffraction, thermo-gravimetric analysis, X-ray photoelectron spectroscopy and Raman microscopy demonstrate the successful reduction of Pd(II), GO and the biomass, resulting in the formation of Pd nanoparticles (PdNPs) on an rGO–biomass hybrid. The distribution of the NPs was found to be dependent on the type of reducing agent. PdNPs formed on rGO sheets showed relatively uniform distribution and size control (2–5 nm), whereas PdNPs on the bacterial scaffold were larger (up to 10 nm in size). Raman spectroscopy studies suggest that the presence of Pd leads to oxygen reduction and increased crystallinity in the bacterial biomass. Previous studies have suggested the potential for a bacterially-supported Pd electrocatalyst in fuel cells and, independently, the suitability of rGO as a support for PdNPs. This study confirms the simultaneous bacterial reduction of Pd(II) and GO and the association between the bacterial cells and rGO. We suggest that the simultaneous presence of E. coli and mild reducing agent together with GO and Pd(II) creates an interactive and synergistic environment in a hybrid material to allow (a) better control of PdNP size and distribution both on the inside of the bacterial membrane and on the rGO sheets and (b) increased crystallinity of the bacterial biomass compared to systems with bacteria alone.
Murray et al.8 used microbial reduction of soluble palladium(II) salt to recover Pd and Pt from spent automotive catalyst leachates in the form of nanoparticles on the surface of bacterial cells and these metals, biorecovered from a waste, were able to function as the anode catalyst in a PEMFC after processing.45 Bioreduction, first reported by Lloyd et al.9 using Desulfovibrio desulfuricans, and on the surface of various other bacteria, such as Shewanella oneidensis and Escherichia coli10–12 has generated substantial interest in this field. Yong et al.13 showed that by increasing the biomass
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Pd ratio, smaller nanoparticles could be produced, while a report by Sobjerg et al.14 demonstrated further size and shape control. Yong et al.14 found that Pd produced in this way (BioPd) gives an effective anode catalyst in PEMFCs after sintering. The low conductivity of the interstitial biomass12 needs to be addressed in order to improve the performance and efficiency of such catalyst-support systems. The properties of the catalyst support used also play an important role in determining the particle size uniformity, particle distribution, catalyst efficiency and lifetime.15 ‘Carbonised’ BioPd formed by sintering the biomass–Pd(0) composite was used in a fuel cell application,14 while electron paramagnetic resonance (EPR) measurements suggested that, when mixed with commercial activated carbon, there is evidence of electron transport between the BioPd and the activated carbon.16 Use of sintered BioPd in a PEMFC is reported to display a power density close to that measured using a commercial Pd/C catalyst. However, other residual elements remaining in the support material may be detrimental to the electrocatalytic activity; hence there is a need to explore other conductive supports where changes to the biomass component can be minimised. It is, therefore, essential to explore techniques to reduce Pd loading, control nanoparticle size, and also retain conductivity via proximity of PdNPs to the conductive material to facilitate electron transport between Pd and the electrode.
Recent studies have shown that some of the bacteria that exhibit metal-reducing capabilities can also reduce graphene oxide (GO), producing reduced graphene oxide (rGO) with physical and electrochemical properties comparable to chemically reduced GO.17–21 Several studies have investigated the reduction of GO through various chemical routes to produce reduced graphene for application as catalyst support for metal nanoparticles in various catalytic applications (due to the outstanding electronic and surface properties of graphene), including polymer electrolyte fuel cells.22–31 However, these methods generally use high concentrations of Pt/metal precursors. The use of bacteria for GO reduction has attracted attention only recently. Yuan et al.32 have shown that, in a microbial fuel cell, GO is reduced in situ to form a biomass–graphene network that improves conductivity and hence power output of the cell. Compared to the various chemical/non-biological methods, biological reduction methods could allow better conservation of metal by the nanoscale scaffolding contributed by the bacterial surface, as well as stability against agglomeration.33 While many previous studies have suggested the potential for a bacterially-supported Pd electrocatalyst in fuel cells and, independently, the suitability of rGO as a support for PdNPs, no studies so far have investigated the simultaneous bacterial reduction of Pd(II) salt and GO and the resultant structure and potential interactions between these reactive species.
In this study, we report the production of a Pd/rGO composite using H2 or sodium formate by the simultaneous bacterial reduction of GO and Pd(II) salt supported by E. coli. The processing of the Pd, GO and E. coli together with a reducing agent means that the product exhibits enhanced reduction and altered structure. This work reveals that the presence of Pd nanoparticles and/or the nucleation process may have a catalytic effect in structuring the carbon present in the biomass, which could significantly enhance the Pd–biomass interaction and enable a more conductive response of the electrocatalyst overall.
| Control/test samples | Acronym |
|---|---|
| E. coli, GO, H2 | B-rGO(H) |
| E. coli, GO, formate | B-rGO(F) |
| E. coli, Pd, H2 | B-Pd(H) |
| E. coli, Pd, formate | B-Pd(F) |
| E. coli, GO, Pd, H2 | B-rGO/Pd(H) |
| E. coli, GO, Pd, formate | B-rGO/Pd(F) |
The as prepared Pd, E. coli, rGO hybrid samples, were not washed in acetone which is known to improve the accessibility of intracellular Pd NPs. This is a standard way of breaking down the permeability barrier by disrupting the cell membranes.46,47 This was not used in the present study as we wished to visualise the interactions of the GO/rGO with the bacterial surfaces.
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50 N2 and O2 at a combined flow rate of 50 mL min−1 was used in an environment of N2 and O2. XPS analysis was conducted on an Al K-Alpha (Thermo Scientific) instrument. Data was collected from the surface of thin film samples and analysis was performed using Casa XPS. Calibration was carried out by alignment of the spectra with reference to the C 1s line at 284.5 eV associated with graphitic carbon, and a Shirley background correction was applied. Raman spectroscopy was conducted on a Renishaw InVia Reflex Confocal Raman microscope using a 514 nm laser. Details of the preparation of samples for various characterisations are included in the ESI.†
Fig. 1a–c show images of B-rGO/Pd(F) samples while images Fig. 1d–f show images of B-rGO/Pd(H) samples. Comparison of images (b) and (c) with (d) and (e) in Fig. 1 clearly revealed that when formate was used as the e− donor/reducing agent, the PdNPs are more uniformly sized and distributed (Fig. 1b), whereas when H2 was used (Fig. 1d and e) more PdNPs were formed on the cell surface (i.e. close to the outer membrane) and as a result the particles are more likely to agglomerate (Fig. 1e), leading to larger particle size. XRD analysis (discussed further below) also confirmed larger particle sizes for both test and control samples prepared using H2 as the e− donor. In sectioned images, some larger PdNPs are visible on edges of long micron sized sheet like structures (circled in red in Fig. 1d). These sheet-like structures are possibly ruptured cell membranes as they are too long to be rGO sheets. It has been observed elsewhere that cells that have been disabled either by genetic removal of key enzymes11 or stressed by toxic chemicals45 can respond by making large nanoparticles outside the cell, presumably via leakage of contents from damaged cells and uncontrolled, ‘runaway’ NP formation on released additional nucleation sites. Flow cytometry studies are planned to look at the ‘robustness’ of the bacteria under the dual stress of palladisation and potential graphene penetration in the next phase of the work.
Imaging of samples produced by drop-drying the solution onto a copper grid (Fig. 1c and f and S1b†) showed the surface of rGO sheets decorated with very small (2–5 nm) Pd nanoparticles in both H2 and formate conditions. Formate has been used as a mild reducing agent for reduction of Pd(II) to PdNPs35 and in the presence of GO, PdNPs are likely to nucleate on the oxygen defects in a reducing environment (similar to Pt nanoparticles28). Fig. 1c shows a high resolution image of the rGO sheets clustering around the cell surface (circled in 1c). The inset in Fig. 1c shows a large (20–30 nm) individual nanoparticle extruded within a cell membrane vesicle, and the lattice fringes revealed a spacing of 0.223 nm, in agreement with the spacing of Pd(111) lattice planes, 0.2246 nm (JCPDS 46-1043). Interestingly, all PdNPs on rGO sheets showed smaller size and more uniform size distributions compared to the PdNPs formed inside the bacterial cells. This is speculated to be due to two reasons: (a) the bacterial cells have a quicker and/or greater uptake of the Pd(II) salt, leading to more PdNPs formation and resulting in agglomeration and larger particle sizes; (b) the rate of nucleation and growth of PdNPs inside the bacterial cells is faster compared to that on rGO sheets. Fig. S1c† also shows small (<5–10 nm) PdNPs on the rGO sheets as seen in the B-rGO/Pd(H) samples and those circled gave lattice spacing of (1): 0.243 nm, 0.239 nm, (2): 0.210 nm, (3): 0.204 nm, which is within 1.5% of the reference value. Such deviations are expected due to the varying orientations of the NPs with respect to the electron beam.36 The Pd nanoparticle size was found to vary from 20–30 nm to 2–5 nm depending upon the location of the nanoparticles. Particles inside the E. coli and in the absence of GO were found to be bigger while those formed on the rGO sheets showed a size distribution of 2–5 nm. Most traditional methods used for preparation of catalyst nanoparticles are reported to form nanoparticles in the range of 2–5 nm or at least below 10 nm. The nanoparticles we prepared in this current method show relatively larger size variation. However, it is evident from the TEM images that there is more agglomeration of Pd nanoparticles inside the bacterial cell when H2 is used and also when no GO is present. Thus, agglomeration and particle size is dependent on, (a) the Pd(II) uptake of the cell and also on, (b) the type of e− donor available. Further studies will be undertaken to optimise the nanoparticles size using these parameters for electrochemical studies during the next phase.
Fig. 1f (circled) shows the edges of a stack of 8 rGO sheets with PdNPs attached to both basal and edge planes. The sheet separation was found to be 0.338 nm, which is in agreement with the separation of graphene sheets (0.34 nm). EDX analysis (Fig. S2†) carried out at different positions on the samples confirmed the presence of carbon, palladium and oxygen in the cell and rGO areas. The presence of small amounts of P, Na and S was also found in the bacterial cells, as expected for biological material.
The XRD pattern for GO (Fig. 2a) consists of the typical graphitic carbon (002) peak around 2θ = 30.6° corresponding to a d-spacing of 0.34 nm, as well as another broad C (002) peak shifted down to around 2θ = 13.5–15.3°, indicating that a major proportion of the carbon sheets have been separated by a larger distance (0.67–0.76 nm) by the oxygen functional groups added by the oxidation process.22 As GO is reduced, the peak at 2θ = 30.6° should increase in intensity, and the lower 2θ peak is reduced. In comparison, the scan for B-rGO(H) (Fig. 2a) revealed two relatively sharp peaks for carbon. The first is shifted to a lower 2θ angle (∼10°) and is less intense than in GO, while the 30.6° peak displayed an increase in intensity, indicating only a partial reduction of GO. However, the scan for B-rGO(F) showed almost a complete loss of the peak at low 2θ values, while the 30.6° peak showed a clear increase in the intensity, suggesting that the reduction with formate was more effective compared to that with hydrogen. Interestingly, in the presence of Pd (Fig. 2b) both B-rGO/Pd(H) and B-rGO/Pd(F), did not reveal any peak at lower 2θ values, suggesting that most or all of the oxygen functional groups on the GO sheets were removed. This is most likely due to the fact that the reduction of GO and nucleation of NPs on the GO surface are simultaneous processes. As metal NP nucleation takes place at the oxygen defect sites, more oxygen groups are reduced.28 The XRD analysis (Fig. 2b) for B-rGO/Pd(H) and B-rGO/Pd(F) samples further revealed the characteristic peaks for Pd(111) and Pd(002) (peak positions reveal plane spacing of 0.2246 nm and 0.1945 nm respectively confirmed by JCPDS, card no. 05-0681) for both B-rGO/Pd(H) and B-rGO/Pd(F). The powder patterns also confirmed the TEM observations of particle sizes. Calculations using the Scherrer equation indicated that PdNPs which nucleated and grew in the presence of GO using E. coli and H2 (i.e. B-rGO/Pd(H)) were on average 10–15 nm, while the PdNPs which nucleated in the presence of GO using E. coli and formate (i.e. B-rGO/Pd(F)) were 5–10 nm. These Pd peaks were found to be broad, compared to sharp peaks (Fig. S3†) for control samples Pd(H) and Pd(F) (particle size of 20–25 nm) where Pd was reduced in the absence of E. coli, demonstrating that the use of E. coli promotes formation of smaller nanoparticles. No Pd peaks were found in the XRD patterns for control samples B-Pd and B-rGO/Pd (Fig. S3†) i.e. in the absence of any electron donor, suggesting that Pd(II) salt is not reduced in the absence of a reducing agent. However, the formation of amorphous small Pd-NPs or single atoms of Pd(0) cannot be precluded.
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| Fig. 2 (a) X-ray powder diffraction patterns for GO, B-rGO(F) and B-rGO(H); (b) B-rGO(H) and B-rGO(F); (c and d): thermogravimetric analysis for samples (c) without Pd and (d) with Pd. | ||
Similarly, no shift or change was observed in the 2θ ∼ 10° peak for control sample B-rGO (Fig. S3a†) confirming that bacteria alone cannot promote GO reduction. On the other hand, control samples rGO(H) and rGO(F) showed the lower 2θ peak shifted slightly (2θ ∼ 14°) and was significantly sharper and more intense compared to that of starting GO; in addition, a small, very broad graphitic carbon peak near 2θ ∼ 30° indicated some reduction of GO in the presence of mild electron donors (Fig. S3a†).
No Pd peaks were found in the XRD patterns for control samples B-Pd and B-rGO/Pd in Fig. S3† (i.e. in the absence of any electron donor), confirming that Pd(II) salt is not reduced in the absence of a reducing agent. This, however, does not exclude the possibility of very small Pd-NPs (e.g. 2 nm or smaller which are invisible to XRD and appear as amorphous). Nevertheless, using XPS in this study no evidence was seen for ‘endogenous’ reduction of Pd(II), i.e. in the absence of added electron donor. Given time, Pd(II) reduces chemically under H2 (and with formate) and, indeed, killed cells or formate alone show very slow Pd(II) reduction.11 The presence of live bacteria (being enzymatic and hence catalytic) not only accelerates what would happen anyway, but also ‘steers’ to some extent the location(s) of the nucleation and nanoparticle growth.48 Hence, the E. coli provides a suitable ‘environment’ for the Pd salt and the e− donor to be adsorbed so that the reduction reaction can take place, as well as acceleration of this reduction.
Control samples rGO/Pd(H) and rGO/Pd(F), i.e. without E. coli (Fig. S3c†), revealed sharp Pd peaks indicating reduction of Pd(II) but forming significantly larger crystals and little or no reduction of GO. Moreover, XRD data as shown in Fig. S3, S5(a) and (b)† confirmed that no reduction of GO occurs in the presence of e− donor (H2 or formate) alone. On the other hand significant GO reduction was observed when E. coli was present along with the reducing agent (Fig. 2a and 3), confirming that GO reduction occurs in the presence of E. coli due to possible synergistic interactions. This further suggests that there is electron exchange between bacterial hydrogenases and GO promoting GO reduction and possibly allowing size control of PdNPs on rGO sheets. Thus, the XRD patterns from various samples and control samples confirmed that the presence of the bacterial cells as well as a mild reducing agent (either H2 or formate), have a vital role to play not only in the reduction of both GO and Pd(II) but also in controlling the PdNP size and distribution. Moreover, the presence of Pd further enhances the reduction of GO.
Thermogravimetric analysis was used to provide information about the thermal stability and composition of the samples. The results for GO (Fig. 2c) show the typical three stages of the breakdown of GO in the presence of oxygen.37 However, all samples with rGO or no GO content revealed significantly less weight loss below 200 °C, indicating lower water content compared to GO. In the E. coli alone, and in all samples containing E. coli (with or without rGO), the removal of oxygen functional groups occurred at around 300 °C, suggesting that most of these are from the bacteria and that GO has been reduced during the reduction process. The removal of the carbon skeleton occurred around 500 °C for E. coli alone, while for the samples not containing Pd (Fig. 2c) it occurred between 500–600 °C. The breakdown of the carbon in B-rGO(H) and B-rGO(F) occurred over a wider temperature range and therefore appears to be a combination of the breakdown of the carbon content in bacteria and GO. Samples containing Pd (Fig. 2d) showed a lower final breakdown temperature, which was just below 400 °C. This could be due to Pd catalysing the breakdown of carbon. It is, therefore, suggested that the presence of the Pd is altering the structure of the carbon and thus its thermal behaviour. This argument is supported by evidence from XPS and Raman spectroscopy discussed in later sections. Studies using Pt have reported a higher temperature for carbon breakdown18 while Pd is reported to catalyse the formation of C–C bonds.31 However, samples with GO show a further 2–3 wt% loss between 600 and 800 °C which is similar to other TGA studies28 reported on metal nanoparticle/rGO samples, showing the structural stability of GO. There was some residue in all samples, which was due to residual elements from the production processes (chemicals used in production of GO, bacterial suspension medium, etc.) as well as substances found in the bacterial cells (phosphorus, sulphur and trace metallic residues from proteins etc.). The residue in samples containing Pd is largely the metal constituent, and 30–40 wt%, which is higher than the original loading of 25 wt%. This can be attributed to the mass loss in GO and bacteria during the reduction processes leading to higher metallic content in the product. Control samples without GO, (B-Pd(H) and B-Pd(F)) showed a higher Pd residue, suggesting higher intake of Pd(II) salt resulting in more Pd nucleation and growth (i.e. in the absence of GO ‘competing’ for available Pd(II)). Among these, the use of formate seems to enhance the Pd nucleation further than H2. The lower Pd wt% in B-rGO/Pd(F) and B-rGO/Pd(H) samples supports the theory that there is a possible competing process(es) between GO and E. coli for the uptake of Pd(II). As observed in TEM images, the nucleation and growth process on GO/rGO sheets appears to be slower compared to E. coli, leading to smaller and well distributed particles on rGO. Consequently, in the presence of GO, E. coli is not able to take up as much Pd(II) which it is otherwise capable of, resulting in a lower final Pd loading in the bacterial content of the overall sample.
XPS analysis was carried out in order to further and more accurately probe the proportions of different elements and types of bonds in the rGO sheets and bacterial surface layers. High resolution spectra of carbon, oxygen and palladium regions were deconvoluted using binding energies found in the literature. Components of spectra were allowed a full width at half maximum (FWHM) of approximately 1 eV and given a Gaussian–Lorentzian line shape (GL(30)). Table 2 gives the elemental composition of the samples as calculated from the survey scans. Since XPS is a surface analysis technique (probing up to ∼10 nm), and the PdNPs are largely situated within the bacterial cells, the overall proportion of Pd found by XPS (Table 2) was much lower than the Pd loading values obtained from TGA. The detection of Pd would be affected by the thickness of the thin film used for XPS analysis, the possible presence of very tiny scattered Pd nanoparticles and the uneven distribution of Pd at the spot under analysis. The reason why GO was introduced in the study was that the original biomass-supported Pd was not effective due to the Pd being inaccessible for electrocatalysis and non-conductive. This was reported for bio-Pt by Attard et al.49 This could be overcome by extensive chemical ‘cleaning’ (required several weeks in a series of solutions) to remove the biomass component which gave excellent electrochemical performance, albeit it also resulted in nanoparticle aggregation in completely cleaned samples. The incorporation of graphene is a simple way to potentially achieve the same outcome in a single step synthesis avoiding prolonged use of aggressive chemicals. The overall proportions of carbon and oxygen, however, confirm that oxygen has been removed in varying degrees from every sample during this reduction process. The assigned components for C 1s, O 1s, and Pd 3d for all the samples with bacteria are shown in Table S2.† The deconvoluted high resolution C 1s spectra of the various samples are shown in Fig. 3.
| Element | Sample | |||||||
|---|---|---|---|---|---|---|---|---|
| Average percentage area of elemental regions | ||||||||
| GO | E. coli | B-rGO(H) | B-rGO(F) | B-Pd(H) | B-Pd(F) | B-rGO/Pd(H) | B-rGO/Pd(F) | |
| C 1s | 76.3 | 67.2 | 72.4 | 71.4 | 75.4 | 75.2 | 75.1 | 73.4 |
| N 1s | — | 9.1 | 6.9 | 9.0 | 5.7 | 5.8 | 8.4 | 7.5 |
| O 1s | 23.7 | 22.2 | 19.3 | 18.6 | 18.2 | 18.0 | 15.9 | 18.2 |
| P 2p | — | 1.4 | 1.5 | 1.1 | — | — | — | — |
| Pd 3d | — | — | — | — | 0.7 | 1.0 | 0.5 | 0.9 |
Fig. 3a and b show the deconvoluted C 1s spectra for B-rGO(H) and B-rGO(F) which show only partial reduction of oxygen when compared with the spectra from GO alone and E. coli alone (Fig. S3†). This applies also to the samples B-Pd(H) and B-Pd(F) which did not have any GO, confirming that the carbon in the biomass is also altered by this process, as suggested earlier by the TGA studies. However, an inspection of the C 1s spectra for GO and E. coli (Fig. S4a and d†) revealed the similarities between them. These suggested that a large proportion of the components and features visible in samples containing both GO and E. coli are contributed by the carbon bonds present in the biomass. Thus, the assignment of the carbon peak components in such samples i.e. B-rGO(F), B-rGO(H), B-rGO/Pd(F) and B-rGO/Pd(H), is not straightforward. While the carbon–oxygen bonds in the biomass are also affected by this reduction process; the presence of nitrogen-containing groups in the biomass such as amine (C–N(CH2–NH2), occurring around 285.8 eV) and amide (N(O)–C
O occurring around 287.9 eV) overlap with the epoxide (C–OH) and carbonyl (C
O) peaks, respectively. Therefore, the presence of significantly strong components at these binding energies in samples containing GO and biomass, even after the reduction, is justified and is not suggesting incomplete reduction of carbon. The previous evidence from XRD shows that the GO is largely reduced to rGO, which supports this hypothesis. This is particularly true for samples B-rGO/Pd(H) and B-rGO/Pd(F) which, according to XRD and TGA studies, show almost complete reduction. However, the presence of closely positioned oxygen and nitrogen functional groups highlights the limitation of XPS in identifying the true level of oxygen reduction in these samples. The above also explains why, in all samples containing bacteria, the hydroxyl groups show a relative decrease while epoxide groups show a relative increase after the reduction process (Fig. 3, Table S1†). It was also observed that the carbon reduction was stronger in the samples containing GO which were reduced with hydrogen when compared to those reduced with formate. Moreover, in the hydrogen-reduced samples there was a higher proportion of C
O. The mechanism of reduction appears to be favouring formation of C
O groups which are more stable. Comparing the peaks in the spectra in Fig. 3 it can be seen that, in the presence of Pd, more hydroxyl and carbonyl groups are removed. This supports the evidence from XRD that the Pd improves the reduction of the GO, which is in agreement with the literature reports on Pt/rGO,28 suggesting that metal nanoparticle nucleation on oxygen defect sites accelerates oxygen reduction in GO.
C 1s spectra for various other control samples (Fig. S5†) further confirmed that without each element present in the system, reduction of carbon–oxygen bonds does not happen as extensively as it does in the combined presence of bacteria and a mild reducing agent. There are large peaks due to epoxide bonds remaining in all samples containing GO reduced in the presence of either E. coli or H2/formate alone. It is also evident that the reduction of Pd alone using E. coli results in a relatively higher quantity of epoxide/amine residues though there are fewer hydroxyl groups. The exception to this low rate of reduction is the reduction of GO and Pd using H2 (Fig. S5d†). However, exposure of GO and Pd to formate alone does not result in any significant reduction of GO. Taking this evidence together with the XRD data, suggests that both the GO and Pd(II) are reduced with hydrogen alone (in the absence of any E. coli), but the GO appears to form amorphous carbon rather than more crystalline graphene sheets.
Palladium XPS spectra (Fig. 4) were fitted using three symmetric Gaussian–Lorentzian peaks according to the method described by Chen et al.38 The doublet peak components in the 3d5/2 and 3d3/2 regions are constrained to have a separation of 5.26 eV and an area ratio of 3/2 (Thermo Fisher Scientific 2013). The components in the Pd 3d5/2 peak were assigned as listed in Table S2† and were in agreement with the literature.38 The spectra in Fig. 4a–d show the extent of the reduction of Pd(II) to Pd(0) in the samples. Based on the component percentage composition as obtained from the deconvolution data, on an average, between 80 and 85% of the Pd(II) in surface layers was reduced to Pd(0), supporting the findings of XRD and TEM. B-Pd(H) samples show relatively less Pd(0) compared to those with formate (Table S1†) which could also be due to the fact that most Pd(0) formed in H2 samples was inside the bacteria which would have relatively weaker intensity. The Pd spectra for control samples (Fig. S6†), revealed that using H2 alone (Fig. S6d and j†) resulted in good reduction, but reduction with formate alone resulted in large quantities of Pd(II) and bulk Pd (Fig. S6k†). Tests using E. coli alone did not lead to any reduction, resulting in strong, intense peaks due to Pd(II) (see Fig. S6d and e†).
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| Fig. 4 (a–d): High resolution Pd 3d XPS spectra: deconvoluted peaks for samples containing Pd. (e and f): Raman spectra for the various test and control samples obtained using a 514 nm laser. | ||
To provide further insight, Raman spectroscopy was used to analyse the carbon structure in the materials. The two main peaks of interest are the D (disorder) and G (graphitic) carbon peaks at approximately 1345 cm−1 and 1582 cm−1, respectively.39 Other interesting features are the 2D and D + G peaks at around 2700 and 2950 cm−1, respectively. The ratio of these (I2D/ID+G) indicates the extent of the aromatic carbon structure versus lattice disorder. The shape and position of the 2D peak indicates the layering of the graphite planes.40 The Raman spectra in Fig. 4e show that in GO the G peak is found at a higher wavenumber position, and the amorphous nature of a sample shifts the D peak to lower wavenumbers, which is in agreement with the literature.39 The ID/IG ratio for the reduced sample containing GO showed an increase when compared with pristine GO, suggesting an increase in disorder for all samples after reduction. This supports the evidence for reduction of carbon and is in agreement with Ganguly et al.41 who hypothesised that the removal of oxygen groups from GO creates more defects in the carbon structure due to loss of oxygen in the form of CO2 etc. The B-rGO samples also revealed clearer 2D and D + G peaks (at around 2700 and 2950 cm−1, respectively) than the B-rGO/Pd samples, indicating more disorder but fewer layers in the B-rGO. Moreover, comparing the formate and hydrogen reduced samples, it was found that hydrogen provides a sample with better separated 2D and D + G peaks compared with formate, suggesting there are fewer layers of graphene sheets in the B-rGO(H) than in B-rGO(F). The positions of the D and G peaks also provide information about the level of reduction.42 The D peak in B-rGO and B-rGO/Pd samples, compared to the starting GO, showed a down-shift of up to 8 cm−1, indicating an increase in amorphous nature, perhaps due to the bacterial biomass and loss of oxygen functional groups in the form of CO2. The G peak with respect to the pristine GO displays an up-shift of 9–11 cm−1 for B-rGO suggesting an increase in disorder but shows almost no change (a negligible down-shift of 1–3 cm−1) for B-rGO/Pd, suggesting that there is more amorphous carbon in B-rGO than in the B-rGO/Pd samples. Overall, this evidence supports the reduction of GO, and hydrogen appears to be the more effective reducing agent. The evidence here obtained from XRD and XPS supports that reduction of GO in the presence of Pd is more effective than GO alone. However, confirmed reduction of carbon in B-rGO/Pd samples based on XRD and TGA data in conjunction with no change in the G peak position for these samples compared to pristine GO samples suggested that the reduction process did not increase or induce any further disorder in the samples despite the possible loss of CO2. The samples of Pd reduced without GO (i.e. B-Pd(F) and B-Pd(H), Fig. 4f) also revealed D and G components. E. coli alone has no peak in this region (Fig. 4e) which is consistent with previous reports.43,44 This provides clear evidence that the carbon in the biomass was altered by the reduction processing and/or the presence of Pd(II) and further strengthens our hypothesis based on XRD and XPS analysis. The comparison of the various Raman spectra further confirmed that the GO–Pd system is more effectively reduced in the presence of both (bacteria and electron donor) elements together, than by separate reduction.
The enhanced crystallinity in the carbon biomass following simultaneous GO and Pd(II) reduction, along with the better size and distribution control of PdNPs formed in rGO–biomass support, makes the final product potentially suitable for testing in catalyst-support studies in applications like fuel cells and electrolysis. This bacterially-driven process also has the potential to pave the way towards a more healthy precious metal economy, allowing easy and effective recycling of precious metals for ‘greener’ fuel cells.45 Hence, further studies will include relocating the surface-Pd to intracellular sites and vice versa in optimisation of the methodology, electrochemical studies of this catalyst-support system and in-depth studies investigating the effect of reaction time, proportions of Pd(II), GO and bacterial mass and pH in optimising the electrochemical behaviour of this system for potential applications.
Footnote |
| † Electronic supplementary information (ESI) available. See DOI: 10.1039/c5ra12552a |
| This journal is © The Royal Society of Chemistry 2015 |