Enikő
Farkas
ab,
Dávid
Srankó
c,
Zsolt
Kerner
c,
Bartosz
Setner
d,
Zbigniew
Szewczuk
d,
Wiesław
Malinka
e,
Robert
Horvath
*a,
Łukasz
Szyrwiel
*ef and
József S.
Pap
*c
aNanobiosensorics Group, MTA Centre for Energy Research – MFA, H-1121 Budapest, Hungary. E-mail: horvathr@mfa.kfki.hu
bDoctoral School of Molecular- and Nanotechnologies, Faculty of Information Technology, University of Pannonia, Egyetem u. 10, H-8200 Veszprém, Hungary
cSurface Chemistry and Catalysis Department, MTA Centre for Energy Research, Konkoly Thege str. 29-33, H-1121 Budapest, Hungary. E-mail: pap.jozsef@energia.mta.hu
dFaculty of Chemistry, Univ. of Wrocław, ul. F. Joliot-Curie 14, 50-383 Wrocław, Poland
eDept of Chemistry of Drugs, Wrocław Medical Univ., ul. Borowska 211, 50-552 Wrocław, Poland. E-mail: lukszyr@wp.pl
fCNRS/UPPA, LCABIE, UMR5254, Helioparc, 2, av. Pr. Angot, Pau, F-64053, France
First published on 21st April 2016
This work demonstrates the heterogenization of homogeneous water oxidation electrocatalysts in surface coatings produced by combining the substances with a suitable polyelectrolyte. The electrocatalysts i.e. Cu(II)-branched peptide complexes involving a 2,3-L-diaminopropionic acid junction unit are heterogenized by building composite layers on indium-tin-oxide (ITO) electrode surface. Alternating deposition of the peptide complexes and poly(L-lysine) or poly(allylamine hydrochloride) were carried out in the presence of phosphate in a pH range of 7.5–10.5. Discussion of the results is divided to (1) characteristics of composite layer buildup and (2) electrocatalytic water oxidation and accompanying changes of these layers. For (1), optical waveguide lightmode spectroscopy (OWLS) has been applied to reveal the layer-by-layer formation of a Cu-ligand/polyelectrolyte/phosphate coating. The fabricated structures had a nanoporous topography (atomic force microscopy). As for (2), electrochemistry employing coated ITO substrates indicated improved water oxidation electrocatalysis vs. neat ITO and dependence of this improvement on the presence or absence of a histidine ligand in the deposited Cu(II)-complexes equally, as observed in homogeneous systems. Electrochemical OWLS revealed changes in the coatings in operando, upon alternating positive–zero–positive etc. polarization: after some initial loss of the coating mass steady-state electrolysis was sustained by a compact and stable layer. According to X-ray photoelectron spectroscopy Cu remains in an N-donor ligand environment after electrolysis.
A novel family of branched peptides has recently been reported to form neutral 1:1 complexes with Cu(II) in the basic pH region, which could be thoroughly characterized in solution.26 The complexes undergo Cu(II) → Cu(III) oxidation and proved to be effective water oxidation electrocatalysts in phosphate electrolyte.27 The applied branched ligands are shown in Scheme 1 as bound in the catalytically competent complex forms. As far as light harvesting or heterogenization is concerned, the branching of peptides (although synthetically challenging) offers unique options, for example, to combine within the same molecule one or more peptide fragments designed for specific metal binding with free arms reserved for another purpose e.g. to support self-assembling. This requires the appropriate extension of each arm.
Scheme 1 Structural representation27 of the Cu(II) complexes Cu-3G and Cu-2GH of the present study. Open rectangles represent sites of water coordination. Ligands are H-Gly-Dap(H-Gly)-Gly-NH2 (3G) and H-Gly-Dap(H-Gly)-His-NH2 (2GH). Potential H-bonding sites are marked with red and blue. |
The schematic structures of the copper branched peptide complexes studied in water oxidation are presented in Scheme 1 to exemplify the complexity of the effects occurring upon the exchange of only one amino acid. The histidine at the C-terminus modifies the coordination sphere from {NH2, N−, N−, NH2} to {NH2, N−, N−, Nim} leaving a different arm (C-terminus instead of N-terminus) to supply second-sphere functions. The localization of His at the N-terminus favours Cu binding at lower pH ((ligand H-His-Dap(H-His)-Gly-NH2) = 2HG), at the C-terminus at higher pH (ligand 2GH), while use of both the N- and the C-termini allows Cu binding over the entire pH range (ligand H-His-Dap(H-His)-His-NH2) = 3H)28). The presence of a Dap junction unit suppresses dimeric or oligomeric complex forms allowing the stabilization of metal binding exclusively near the branching group. Competition studies between fragment-by-fragment modified branched ligands and their linear components for metal ion binding demonstrated that branching can increase stability.26 Above all, the C-terminal substitution of Gly with His affects homogeneous water oxidation catalysis positively through the equatorial ligand set, but H-bonding interactions can also contribute to the overall performance. Peptides are exceptionally rich in such groups, which has a profound effect in enzyme catalysis either by means of contributing to the active site structure or to protein dynamics.29 With respect to the complexes Cu-3G and Cu-2GH, the high number of potential donor/acceptor sites for H-bonding (Scheme 1) could be exploited to anchor these molecules as catalytic centres in a composite system on a working electrode surface. This kind of attachment could preserve the coordination sphere along with the associated catalytic activity, yet entrap catalyst molecules at the surface. Note that biological studies have shown that this unique group of peptides can carry out targeted transport of selected metal ions possibly involving specific interactions between the surface of biomolecules and the freely available arms of the peptide ligands.30
These considerations led to the idea that positively charged polymers such as poly(L-lysine) (PLL) could be candidates as a support medium for catalyst heterogenization. PLL itself has been used for functionalization of solid substrates, for example that of indium-tin-oxide (ITO) with biomolecules for a number of purposes.31 The layer-by-layer (LbL) deposition of composite systems consisting of polyelectrolytes of alternating charges is a well-established cost-effective methodology.32 The notion that certain complexes with pincer ligands can be attached to polypeptides by coordinative bonds33 and metal receptors can be imprinted into multilayer polyelectrolytes34 made this strategy even more attractive, since the accessible axial sites in complexes Cu-3G and Cu-2GH and the amine or amide groups of the polyelectrolytes should allow this kind of attachment (Scheme 2b). However, catalytic applications of such systems would require analytical methods that can detect rather small changes in mass on the surface.
The transport and binding of adsorbing molecules in the close vicinity of the coated surface can be investigated by means of optical waveguide lightmode spectroscopy (OWLS)35,36 and its combination with electrochemistry (EC-OWLS).
OWLS and EC-OWLS have excellent sensitivities to monitor molecular adsorptions in real-time, and have already evolved into reliable analytical methods (Scheme 2a). OWLS itself is ranked as a high performance surface-sensitive technique allowing real-time monitoring of processes accompanied by refractive index changes in the close proximity of the surface of a waveguide sensor chip (typically <200 nm depth into the solution above the sensor surface). The waveguide sensor consists of a high refractive index waveguide layer with a shallow diffraction grating embossed into its structure supported by a thicker optical glass slide. Incoupling of a linearly polarized monochromatic He–Ne laser beam via the grating results in sharp resonance peaks when plotting the intensity of the incoupled light against the incident angle of the illuminating beam. The sensing principle relies on the perturbation of the evanescent optical waves of the guided lightmodes. Refractive index variations in the close vicinity of the sensing surface alter the discrete incoupling angles, thus shift the positions of the resonance peaks.37,38 The waveguide film can be coated by a thin layer of any transparent material required by the application. For example, when a thin coating of the n-type semiconductor ITO (a good electric conductor) is employed the method can be extended to EC-OWLS. Electrochemical methods, such as controlled potential electrolysis (CPE), can be performed in parallel with the OWLS measurements.
Scheme 2 (a) Parts and operation principles of the OWLS flow-through cell, (b) components for the self-assembled catalyst deposition on ITO surface. |
The aim to anchor Cu complexes and this way activate ITO electrodes toward the OER has urged us to explore the LbL build-up method as an option for the heterogenization with suitable polyelectrolytes and follow the process by means of (EC-)OWLS. Note that in principle this means only one extra component to the Cu complex–electrolyte–ITO triformity of the homogeneous system (Scheme 2b). To our knowledge the application of branched peptide complexes in self-assembled electrode materials is unprecedented. Reported below are the results of the alternating depositions of Cu-3G or Cu-2GH and PLL or poly(allylamine hydrochloride) (PAH), resulting in LbL-ITO electrodes sensitized toward electrocatalytic water oxidation. The fabricated composite layers were investigated by detailed electrochemical experiments.
(A) 14 × 14 mm pieces of ITO electrodes (∼20 ohm sq−1, Präzisions Glas & Optic) were first immersed into the polyelectrolyte solution (PLL, 0.01 mg mL−1 or PAH, 0.5 mg mL−1) then rinsed in phosphate buffer. The ITO was then dipped into the solution of the Cu complex (Cu-3G or Cu-2GH, 0.05–1 mM) and washed with buffer again. These steps were repeated 0–20 times. Each step took 5 min and this period was set to mimic the OWLS experiments. The pH of the concomitant solutions was identical, set by titration of 0.1 M phosphate electrolyte by NaOH. The solutions of the components were distributed in a multiwell sterile plate, the volumes were adjusted to cover half of the ITO, this way 0.98 (±10%) cm2 of the electrode surface could be exposed to LbL deposition. The ITO pieces modified by method (A) were then used as working electrodes in a standard electrochemistry cell.
(B) LbL was performed in the flow cell of the OWLS instrument to follow the build-up process in real-time. An ITO coated optical chip (MicroVacuum Ltd, Budapest) was used for either electrochemical i.e. EC-OWLS or OWLS experiments. The first polyelectrolyte solution (PLL or PAH) was injected into the cell. After no further changes were detected by OWLS, buffer was let through the cell by using a peristaltic pump with 1 μL s−1 flow rate to eliminate the remaining polyelectrolytes until, again, no further change was observed in the OWLS signal. Next, buffered Cu complex solution (Cu-3G or Cu-2GH) was injected trough a septum injection port, that was followed by buffer rinsing again. These steps were repeated in the case of multiple deposition cycles and each step took ∼10 min. The concentration and pH of the applied solutions were identical to those used in method (A). The complex solutions were made before the experiments by using slight excess of ligands (0.9:1.0 Cu:ligand ratio); these solutions were then titrated with 1 M NaOH to the desired pH and mixed with appropriate amounts of phosphate solution. Lower concentrations were set by dilution. All experiments were performed at 25 °C and the formation of the complexes was confirmed by measuring the electronic absorption spectra26 with an Agilent Cary 60 spectrophotometer coupled to the immersion probe.
Fig. 1 (A) Variation in surface density (PB, 0.1 M, pH = 7.5) with [Cu-3G] (for concentrations see legend) on ITO coated chip followed by OWLS (vertical grid lines stand for approx. time of injection of the different components as indicated); (B) mass development of Cu-3G (mCu-3G) with the number of LbL cycles (same as in A), inset: mCu-3G normalized with mPLL and plotted against the number of LbL cycles (used for calculating Γ0cat in Table S2†); (C) variation in surface density growth ([Cu-3G] = 0.5 mM) with pH (see legend); (D) variation in LbL development of Cu-2GH/PAH with [Cu-2GH] (PB, 0.1 M, pH = 7.5); (E) mass development of Cu-2GH (mCu-2GH) on ITO with the number of LbL cycles (same as in D), inset: mCu-2GH normalized with mPAH and plotted against the number of LbL cycles (used for calculating Γ0cat in Table S2†); (F) variation in surface density growth ([Cu-2GH] = 0.5 mM) with pH (as indicated by the legend). |
The pH optimum for LbL deposition was found at ∼9–10 (Fig. 1C), overlapped with the pH domain of the [CuH−23G] species.26 Note that pH strongly affects adhesion of PLL reaching a maximum at pH 10 (see the first 20 min in Fig. 1C, where the surface density of the 1st PLL layer was normalized to ∼300 ng cm−2 uniformly). For this reason pH 10 and [Cu-3G] = 0.5 mM represent optimum conditions for the LbL deposition of Cu-3G/PLL in PB. XPS analysis on bare ITO and after LbL deposition of Cu-3G and PLL by method (A) confirmed that the surface is composed of organic material with peptide bonds, contains Cu(II) in N donor environment and phosphate (for a detailed discussion see ESI, Fig. S1–S3†). The detected surface composition of the LbL-ITO is included in Table S1.†
Obviously, the number, nature and accessibility of the potential hosting sites can be expected to fundamentally determine the LbL build-up, but the sharp difference between Cu-3G and Cu-2GH is still surprising, since these complexes have very similar properties. However, this highlights the significance of the branched peptide structure that can be related to their interactions with biomolecules.30 Therefore the preference of Cu-3G to PLL is tentatively assigned to the available C-terminal glycyl amide unit that could form strong H-bonds with the peptide functions on PLL. Cu-2GH, on the other hand, has a C-terminal histidine coordinated to Cu(II). The non-coordinated arm here is the N-terminal glycine and this ligand arrangement is apparently more selective to allylamine functions with respect to H-bond formation. Electrostatic interactions are thought to have much less role (if any) in the adhesion of the Cu complexes, since PDDA or PSS did not support deposition. The role of electrostatic interactions involving phosphate anions is rather crucial in holding together the supporting polyelectrolytes, with ITO thus building the host surface arrangement for the catalytically active complexes. Note that in biological systems the affinity of the cationic side chain of lysine for the negatively charged phosphate backbone of DNA is well known42 and serves as a model for the interaction between PLL or PAH and phosphate.
The pH optimum for layering is ∼10 (Fig. 1F) resulting from parallel growing speciation% of the [CuH−22GH] species and the adsorption preference of PAH (i.e. although Cu-2GH is still adsorbed at pH 11, multiple deposition cycles with PAH is not possible). The pH also strongly affects adhesion of PAH to ITO (see the first 20 min section of Fig. 1F, the surface density of 1st PAH layer is normalized to ∼200 ng cm−2 for comparison). For the above experimental findings and for the sake of comparable conditions, during electrochemistry with LbL-ITO [Cu-3G] = [Cu-2GH] = 0.5 mM was set.
The above discussed OWLS experiments showed that the Cu complexes can be layered with polyelectrolytes in a highly selective manner, governed by the ligand structure. Optimum layering pH approximates that of catalysis in homogeneous solution, while multiple deposition cycles help attach increasing amounts of Cu complexes. These are important features from the viewpoint of electrocatalytic applications.
The combination of OWLS, XPS and AFM allowed gathering information about the surface density and chemical environment of the heterogenized Cu complexes and surface topography of the composite layers that was considered in the course of electrochemistry. This information served also as a starting point for the preparation of the LbL-ITO electrodes for water oxidation electrocatalysis.
Fig. 3A shows the effect of electrolyte pH on the cyclic voltammetry (CV) responses. A symmetric oxidation peak occurs and shifts from ∼0.71 to ∼0.59 V vs. Ag/AgCl upon changing the pH from 9.1 to 11.0. This behaviour is analogous to that of Cu-3G in solution and therefore the current peak can be assigned as the Cu(III/II) transition of adsorbed complex. Further polarization yields a current peak that is pH-sensitive and evolves into a catalytic current, again, very similarly to the homogeneous system with the complex in solution. Upon reverse polarization no reduction can be detected, which indicates that the oxidation peaks attributed to the [CuII–OH2] → [CuIII–OH] → [CuIII–O˙] PCET transitions (numbers in red circles in Fig. 3A), respectively, may originate from a portion of Cu-3G that is non-reversibly transformed upon oxidation. This portion could theoretically dissociate to the bulk or yield another complex form (or both processes could take place). After the 3rd cycle the CV current response becomes steady and corresponds at 1.1 V vs. Ag/AgCl to the CPE current value after 5 min (Fig. 3B, for description of CPE experiments at different pH values and the effect of the number of deposition cycles see Fig. S5 and S6,† respectively) e.g. these CV conditions represent diffusion controlled rates (see also Fig. S7† to compare two different scan rates on LbL-ITO previously used for CPE for 10 min). Apparently, the portion of Cu-3G that is responsible for the current peaks in the first cycle has no further role in sustained electrolysis (EC-OWLS and XPS experiments are supportive of this presumption).
In Fig. 3B the 3rd cycles of CVs taken with differently fabricated LbL-ITOs are compared. The neat (orange curve) or PLL coated ITO (green curve) cannot compete with the current growth on the electrode coated by Cu-3G/PLL (purple curve). When the final deposition cycle is that of PLL the current response is lower at the potential of the Cu(III/II) transition of Cu-3G in the first cycle (Fig. S8†), while the catalytic current corresponds to that of CPE at 1.1 V from the 3rd cycle (Fig. 3B, dark blue curve, PLL–Cu-3G/PLL). This can be explained by the existence of a complex fraction that behaves like Cu-3G in solution and corresponds by amount to roughly 38% of the total deposited amounts at most. This is supported by the quantitative analysis of the Cu(III/II) current peaks (see Fig. S8,† caption) and calculated from OWLS data on the Cu-3G/deposition cycle quantity (values are listed in Table S2†).
The optimum pH of the deposition from the electrochemistry perspective was investigated by comparison of the performance of LbL-ITO electrodes layered at different pH values and immersed into a phosphate electrolyte at pH = 10.6 (Fig. S9†). It can be concluded that LbL-ITOs layered at pH 9–10 show the highest catalytic currents by good reproducibility of CPE currents (Fig. S10†). However, further anodic polarization of the electrodes to above 1.2 V vs. Ag/AgCl results in gradual loss of catalytic capacity (Fig. S11†) therefore EC-OWLS experiments and FOWA (vide infra) were done on LbL-electrodes polarized to a maximum of 1.2 V.
ITO pieces modified with PAH and Cu-2GH and used as working electrodes in CV experiments behave similarly to the Cu-3G/PLL system. The results are in favour of pH ∼ 10 as the optimum for LbL build-up (Fig. S12† shows the effect of deposition pH). The peak associated with the Cu(III/II) transition in the first cycles shifts from ∼0.77 to ∼0.61 V vs. Ag/AgCl as the pH is set from 9 to 11 (Fig. S13a and b†). The peak cannot be observed upon consecutive cycles and the reduction peak is also missing from the reverse polarization curve (Fig. S13c†), which points to the same conclusions as for the Cu-3G/PLL system. Anodic polarization to 1.2 V yields a catalytic current response, which, after the 3rd cycle is similar to CPE current after 5 min at the corresponding potential (Fig. 3C, for CPE experiments see Fig. S14†). The exception is CPE at above pH ∼10.6, where the development in current with time is associated with unexplored side events.
The first cycle of CV experiments revealed two consecutive oxidation steps upon anodic polarization of LbL-ITOs preceding electrocatalysis at above ∼1 V that were assigned to a fraction of Cu-3G and Cu-2GH that dissociates from the surface. The catalytic current became steady upon repeated cycles between 0 and 1.2 V and the oxidation step triggering catalysis shifted to the anodic direction. This and the absence of the initial oxidation steps indicated a substantial change in the mechanism of catalysis compared to the homogeneous systems.
Most importantly, after the initial change in mass the current during CPE became steady and caused no further loss of surface density. The question emerged whether the LbL-ITO exposed to CPE will accommodate additional Cu-3G. In an attempt to re-supply the LbL film with Cu-3G only minimal (<0.1 × 10−10 nmol cm−2) complex was adsorbed indicating the formation of a very compact LbL-ITO surface upon electrolysis. The follow-up CPE shows higher current, however, this may be caused by remaining Cu-3G in the bulk dead-space of the cell (in the case of Cu-2GH no change in the follow-up CPE current was experienced).
According to XPS analysis of Cu and N content on Cu-3G/PLL LbL-ITO pieces as prepared and after exposure to CPE at pH 10.64 (Fig. 5A) the Cu remains in the Cu(II) state in a peptide environment that is rich in N (Fig. 5B).34 This is evident from the Cu2p3/2 peaks that are present at nearly the same energy (with no shake-up peaks typical for Cu-oxide/hydroxide formations27). Modelling the N1s peak with amine (NH), quaternary ammonium (NH+) and amide (OCNH) component peaks yields a somewhat changed ratio and enrichment in NH+. In parallel, the N/Cu ratio is higher in the sample exposed to CPE, suggesting that the surface structure of the Cu-3G/PLL layers changes upon electrolysis and 31% less Cu remains in the deposited film. This is in accordance with CV results (absence of the [CuII–OH2] → [CuIII–OH] current peaks typical for the original complex Cu-3G after repeated cycles, indicating ∼38% initial loss of Cu-3G, Fig. S8†) and with the EC-OWLS findings (some change in surface density and no increase in mass with follow-up addition of Cu-3G).
The same general observations could be highlighted in the case of Cu-2GH/PAH (Fig. 4B) judged from a similar set of experiments. After three deposition cycles finished with PAH, 1.6 × 10−10 mol cm−2 complex could be anchored in total and the electrode could traffic 3 × 10−8 moles of electrons in the course of 3 × 10 min of CPE at 1.1 V (periods indexed with red asterisks). Remarkably, the loss in surface density ceased at ∼1160 ng cm−2, where the last PAH deposition after 160 min was finished (dashed orange line). No further changes upon addition of Cu-2GH and follow-up CPE could be detected, in support of a compact electrocatalyst film on ITO.
Taken together, these findings indicate that the fraction of the Cu-3G and Cu-2GH complexes responsible for catalysis changes coordination mode upon deposition and oxidative polarization of the LbL-ITO. The resulting Cu is still bound in N donor set according to XPS however. Leaching of the complexes from LbL-ITO can be estimated based on CV and XPS results, and supported by EC-OWLS. This means that an altered complex form of Cu should be responsible for the sustained CPE.
According to the FOWA results (Fig. S17 and S19†), the catalysis is less disturbed by side phenomena below the formal potential of the redox transition initiating catalysis for Cu-3G/PLL and Cu-2GH/PAH in good agreement with the CPE experiments that show steady currents on LbL-ITO electrodes at pH ≤ 10.6. The potential of the catalysis-initiating oxidation step was detected by square wave voltammetry (SWV) for both systems as illustrated in Fig. S16.†
Long-term CPE experiments for Cu-3G/PLL and Cu-2GH/PAH at pH = 10.6 (Fig. S18†) were performed to decide whether the catalytic current was associated with O2 production. The data suggest that O2 is produced and the stability of the Cu-3G/PLL systems lags behind that for Cu-2GH/PAH even at lower potential. This is associated with the strongly overlapping onset potential for PLL with that of catalysis (Fig. S18 inset†). The steady current (i.e. the linear increase of charge, Fig. S18†) of the long-term electrolysis experiments indicate no change in the catalyst for a ∼20 min (Cu-3G/PLL/phosphate) and ∼40 min (Cu-2GH/PAH/phosphate) period during which several turnovers of O2 production takes place with acceptably good faradaic efficiency. CV performed after CPE experiments confirmed that the LbL-ITO still exhibited catalytic current over several cycles and current peaks associated with the Cu content were present (Fig. S18A inset and B†). On the other hand, when pH or the potential (see Fig. S11†) are further increased the catalysis is affected by side events, which is traced in the shifting CPE currents with time (Fig. S5 and S14†).
The comparison of kcat values from FOWA should reflect dominantly the inner-sphere structural differences in the two different catalytic centres that are anchored at the LbL-ITO. The TOF values from the homogeneous catalysis study between Cu-3G (TOF = 24 s−1, pH = 11) and Cu-2GH (TOF = 53 s−1, pH = 11)27 and especially their ratio of 2.2 therefore represent a good reference for comparison (note that direct numerical comparison is not viable since TOF values were determined by a different method at a glassy carbon electrode e.g. GCE in the earlier study). Remarkably, the kcat(Cu-2GH)/kcat(Cu-3G) ratios in Table S2† (2.32 in average) are in good agreement with the value for the molecular catalysts, where the better catalytic performance of Cu-2GH was attributed to the coordinated C-terminal His. This (and the high preference of His over amines toward Cu) supports the hypothesis that His should be found within the first coordination sphere of Cu in the LbL built system. Finally, if one compares TOF values obtained by different numbers of deposition cycles (n, Table S2†) it becomes apparent that the TOF values drop when n > 8 in spite of increasing Γ0cat. In accordance, saturation in the steady-state current can be observed during CPE with increasing n (Fig. S6†). This suggests that only a certain fraction of the anchored complex molecules is activated toward catalysis that is limited by the LbL film thickness.
Scheme 3 Proposed mechanism for the water oxidation catalysis at LbL-ITO in accordance with experimental findings and in comparison with the homogeneous systems (3G and 2GH ligands are omitted). |
It has been shown by means of CV and CPE experiments that water oxidation can be performed and sustained for longer periods on LbL-ITO, if pH and potential are kept at values below those resulting in high initial rates, but conflicting with layer stability. In operando EC-OWLS analysis revealed mass transport events that ceased after initial loss in surface density. Failed efforts to supplement the LbL-ITO used in EC-OWLS experiments with Cu-peptide and the observed transformation of CV curves altogether imply that structural changes take place upon polarization of the electrode. Most likely the Cu complexes act as nodules, to form (in part) catalytic centres and get wrapped into microcapsules of the polymeric chains through coordinative bonds, similarly to literature examples with pincer ligand complexes.47 However, in the present case these events are completed by electrochemistry. The nanostructured surface assemblies can accommodate no additional catalyst and follow a different operating mechanism in comparison with the homogeneous system. The method represents a viable strategy to incorporate molecular catalysts by self-assembly into functional layers. Based on these initial results a PLL-type polylysine extension of the branched metal binding peptide site (head–tail structure) is currently being investigated in order to advance layering properties. Although it was neither exploited nor emphasized, PLL and both catalysts were enantiomerically pure isomers that could be utilized in future enantioselective electrocatalytic applications. It was also out of the scope of this study to pursue electrolytic transformations at high pH and E (with simple precursors, of course) that could serve as templates of nanostructured patterns for metal-oxide–hydroxide WOCs with enhanced catalytic activity.19,48
Footnote |
† Electronic supplementary information (ESI) available: Tables S1 and S2, X-ray photoelectron spectroscopy (XPS) on LbL-ITO with Cu-3G and PLL, Fig. S1–S20. See DOI: 10.1039/c6sc00595k |
This journal is © The Royal Society of Chemistry 2016 |