Introduction

Mimicking the sophistication of naturally occurring enzymes has been a long-term goal of the scientific community. An artificial analogue that can perform equally well as its natural predecessor will not only provide deeper understanding of the native enzymes, but also enable the development of efficient artificial catalysts. For several decades now chemists have embarked on this daunting pursuit of emulating the efficiency and selectivity of naturally occurring enzymes and several important milestones have been achieved. Efforts from synthetic inorganic chemists have resulted in synthetic models of myoglobin (Mb), galactose oxidase, tyrosinase, cytochrome P450 and cytochrome c oxidase (CcO)1,2,3,4,5. Alternatively, there has been fervent pursuit of biochemical constructs inspired by natural metalloenzymes. A series of binuclear non-haem iron, cytochrome c, haem oxidases and iron–sulfur enzyme models have resulted from such efforts4,6,7,8,9,10,11,12. While none of the synthetic or biochemical models reported so far could match the reactivity exhibited by their natural counterparts, fundamental insights regarding the structure–function correlations of several metalloenzymes have been gained in the process7,13,14,15. In addition, key information about the secondary coordination sphere interactions present in the protein-active site, which play a dominating role in determining the electronic structure and reactivity of these metalloenzymes, have been identified16,17.

In a biosynthetic approach, stable naturally occurring proteins have been used as scaffolds for creating mimics of several metalloenzymes, such as hydrogenases which are involved in the reversible generation of H2 from water, haem proteins participating in electron transfer and O2-binding, non-haem iron and copper enzymes active in small molecule activation, and even novel enzymes containing non-native cofactors18,19,20,21,22,23,24. For example, using this approach, biosynthetic models that structurally and functionally mimic CcO and nitric oxide reductase have been reported7,25. Despite decades of focused effort, however, biosynthetic models with catalytic efficiencies approaching those of the naturally occurring metalloenzymes have remained elusive26,27,28. In this report, we communicate a biosynthetic model of CcO bearing the distal CuB and a tyrosine residue that is kinetically more competent in reducing O2 electrochemically than any known synthetic analogue, as well as native CcO itself.

X-ray crystallography of Mb and its mutant have revealed that its two propionate side chains project out of the protein surface into the solvent (Fig. 1)7. Taking advantage of this structural feature, we have previously developed an electrocatalytic O2 reduction system where the native haem cofactor in Mb is replaced by a modified hemin cofactor bearing an alkyne group (Hemin-yne, Fig. 2) so that electrons can be injected directly into the haem from a gold electrode to facilitate O2 reduction29. This method resulted in a Mb-functionalized electrode bearing 2.15 × 10−12 mol per cm2 of protein, which was characterized using several microscopic and spectroscopic techniques29. Over the last few years, a biosynthetic model of CcO has been reported in which two distal residues of Mb (L29 and F43) have been mutated to His, which along with the native His64, form a Cu-binding site, mimicking the distal CuB-binding site present in CcO (CuBMb)30. Furthermore, in an attempt to mimic the conserved Tyr 244 residue in the CcO-active site, a G65Y mutant of CuBMb (G65YCuBMb) containing redox-active tyrosine residue in the distal site and a variant where a tyrosine residue was crosslinked to the active site histidines were also created (Fig. 1)31.

Figure 1: Crystal structure.
figure 1

Crystal structure of a Mb-based biosynthetic model of CcO, F33Y-CuBMb; pdb id: 4FWY. (a) The haem cofactor is in a cleft on the molecule protein surface, (colour coded according to the charge of the residues), with the propionate groups exposed to the solvent. (b) The computer model of G65YCuBMb showing its catalytic centre containing the distal CuB bound to histidines and a tyrosine 65.

Figure 2: Construction of the electrode bearing the biosynthetic model.
figure 2

Reconstitution of apoprotein in situ with Hemin-yne groups that are covalently attached to mixed self-assembled monolayers of thiols on an Au electrode. The modified hemin is indicated as Hemin-yne.

Herein we report the electrocatalytic properties of the G65YCuBMb (higher synthetic yields than the tyrosine crosslinked variant) immobilized on an Au electrode using the method developed for WT Mb29.

Results

Electrode characterization by SERRS

Surface-enhanced resonance Raman spectroscopy (SERRS) data (Fig. 3a) of the electrodes bearing the G65YCuBMb protein with and without CuB show the oxidation and spin state marker ν4, ν3, ν2 and ν10 bands at 1,375 cm−1, 1,493 cm−1,1,585 cm−1 and 1,641 cm−1, respectively. The ν4, ν3 and ν2 values are consistent with the presence of a five-coordinated high spin haem in the active site on these electrodes bearing the biochemical constructs of CcO32. Also the bands at 1,504 cm−1 and ν4 at 1,641 cm−1 suggest the presence of a mixture of six-coordinate low spin species, which likely has H2O as the axial ligand. The positions of these bands in the G65YCuBMb and their relative intensities are different from Hemin-yne (Supplementary Fig. 1)29.

Figure 3: SERRS and CV data for the electrode fabricated with G65YCuBMb mutant.
figure 3

(a) SERRS spectra of G65YCuBMb with (green) and without (red) the distal Cu2+ in air-saturated 100 mM phosphate buffer (pH 7) solution. (b) Anaerobic CV of G65YCuBMb without CuB (red) and after CuB binding (green). 2 V s−1 scan rate, in degassed, pH 7, 100 mM phosphate buffer using a Pt counter electrode.

Electrode characterization by X-ray photoelectron spectroscopy

X-ray photoelectron spectroscopic (XPS) data of a G65YCuBMb-bound Au electrode clearly indicate the presence of Fe, Cu, C, N and O elements (Supplementary Fig. 2, Supplementary Table 1). The 3p3/2, 2p3/2 and 2p1/2 binding energy peak for the FeIII of haem group appear at 56.5 eV, 709.4 eV and 722.4 eV, respectively33,34. The 2p3/2 and 2p1/2 binding energy peak for CuII in the distal site appear at 931.7 eV and 951.8 eV, respectively35. The N1s peak is broad (Supplementary Fig. 2), as it contains several components due to the presence of amide, haem pyrroles and the triazole groups (resulting from the covalent attachment of Hemin-yne) on the surface33. Similarly, the C1s peak (Supplementary Fig. 2) contains contributions from different types of C atoms (aromatic, aliphatic, haem and so on) on these protein-modified surfaces36.

Electrode characterization by CV

Cyclic voltammetry (CV) of G65YCuBMb with and without the distal CuB immobilized onto the electrodes in degassed buffer show the haem Fe3+/2+ midpoint reduction potential (E1/2) at −97 mV and −57.5 mV, respectively (Fig. 3b). The peak separation between the cathodic and the anodic peak for both the cases is 70 mV (ref. 37). Hemin-yne displays the Fe3+/2+ reduction potential at −70.0 mV in the absence of a protein and −135.0 mV when bound to wild-type apo Mb29. In the case of the G65YCuBMb protein-bound electrodes, the Cu2+/+ process overlaps with the Hemin-yne Fe3+/2+ process, resulting in approximately twice the area under these CV peaks relative to the G65YCuBMb-bearing electrodes prior to CuB loading. The integrated area under these CV features in the absence of Cu2+ indicates that there are 2.55±0.05 × 10−12 mol of protein per cm2 of the surface. The ratios of the integrated area under the CV features of G65YCuBMb functionalized before and after loading the CuB is 1:2 (Table 1, fourth column) which is consistent with the expected 1:1 stoichiometry (that is, every G65YCuBMb binds one Hemin-yne and one Cu2+ ion). Note that the E1/2 values of the hemin and CuB measured for these electrodes are slightly different from those estimated from potentiometric titration in solution7,19. This is likely due to the interfacial microenvironment of the –COOH-terminated Self Assembled Monolayer (SAM) which is known to shift the apparent formal potentials of redox-active species in its vicinity38. Thus the in situ reconstitution of the protein with Hemin-yne on the electrode is evident from the SERRS, XPS (Supplementary Fig. 2) and CV data (Supplementary Fig. 3, Supplementary Fig. 4). The presence of the Cu2+ at CuB site on the electrode is indicated by XPS and CV data. Taken together, these data indicate the assembly of the G65YCuBMb, biosynthetic model of CcO covalently attached to the electrode via the linkage between the Hemin-yne and the azide terminated thiols created using click reaction (Fig. 2).

Table 1 E1/2 and coverage.

O2 reduction reactivity of the electrode

In linear sweep voltammetry experiments performed in aerated buffers, large electrocatalytic O2 reduction currents are observed by the G65YCuBMb (with and without Cu2+) bearing bio-electrodes at pH 7 at room temperature, as the applied potential is lowered below +100 mV versus NHE (Fig. 4a, Supplementary Fig. 5). Thus as the potential of the electrode is lowered such that the iron in these proteins is reduced to FeII, an electrocatalytic O2 reduction current is observed. It is important to note that the potential of O2 reduction reaction (ORR) (EORR) is −263 mV, which is more negative than the E1/2(−97 mV), suggesting that the potential determining step of ORR is not the reduction of resting FeIII to FeII but the reduction of a different species with −166 mV more negative potential (Fig. 4a inset). A more negative EORR relative to E1/2 is mechanistically significant (vide infra).

Figure 4: RDE data for electrode modified with G65YCuBMb with Cu2+.
figure 4

(a) Linear sweep voltammogram of G65YCuBMb with Cu2+ in air-saturated pH 7, 100 mM phosphate buffer solution at 100 mV s−1 scan rate, potentials are scaled relative to NHE and a Pt counter electrode is used. Data are collected at different rotation speeds (200 r.p.m.—red, 400 r.p.m.—purple, 600 r.p.m.—green, 800 r.p.m.—blue). (b) Plot of icat−1 for G65YCuBMb-bearing bioelectrode at −300 mV potential and at multiple rotation rates, with the inverse square root of the angular rotation rate (ω−1/2) (c) Difference between the potential for O2 reduction (EORR) and the midpoint reduction potential of Fe3+/2+ redox couple (E1/2).

In these active sites, O2 may be reduced by 4e and 4H+ to H2O, or by fewer electrons to produce partially reduced oxygen species (PROS) like O2and H2O2. The extent of 4e reduction and the second order rate constant (kORR) of the ORR can be determined using rotating disc electrochemistry (RDE) where the catalytic O2 reduction current increases with increasing rotation rates (Fig. 4a,b) following the Kouteky–Levich (K–L) equation (equation (1))39.

where, iK(E) is the potential-dependent kinetic current and iL is the Levich current. iL is expressed as

where n is the number of electrons transferred to the substrate, A is the macroscopic area of the disc (0.096 cm2), [O2] is the concentration of O2 in an air-saturated buffer (0.26 mM) at 25 °C, DO2 is the diffusion coefficient of O2 (1.8 × 10−5 cm2 s−1) at 25 °C, ω is the angular velocity of the disc and ν is the kinematic viscosity of the solution (0.009 cm2 s−1) at 25 °C (ref. 40).

Plot of icat−1 at multiple rotation rates with the inverse square root of the angular rotation rate (icat−1) for G65YCuBMb (with Cu2+) (Fig. 4b) is linear. The slope of K–L plot is expressed as 1/[n{0.62FA(DO2)2/3ν−1/6}], which can be used to experimentally estimate the value of n where n is the number of electrons donated to the substrate, that is, O2. The slope obtained from the experimental data for G65YCuBMb (Fig. 4b) is close to the theoretical slope (Fig. 4b, dotted purple line) expected for a 4e process and very different from the slope for a 2e process (Fig. 4b, dotted green line). Thus the G65YCuBMb bioelectrode predominantly catalyses a 4e/4H+ reduction of O2 to H2O at pH 7.

The intercept of the K–L plot is the inverse of the kinetic current (iK(E)−1), where iK(E) is expressed as41

where, n is the number of electrons, A is the geometric surface area, [O2] is the bulk concentration of O2, Γcat is the surface coverage of the catalyst (obtained from the integration of the anaerobic CV data) and kORR is the second order rate constant for O2 reduction estimated at −300 mV. At this potential, in an oxygenated buffer, the G65YCuBMb catalyst is involved in substrate diffusion-limited ORR. Using this equation (equation (3)) and the experimentally obtained iK(E) at −300 mV, the second order rate constant for O2 reduction G65YCuBMb is evaluated to be 1.98 × 107 M−1 s−1 (Table 2). The pseudo first order rate can be determined (Table 2) from the second order rate by taking into account the substrate, O2 concentration under these experimental conditions to be 0.26 mM (Supplementary Fig. 6). The catalytic ORR rate by G65YCuBMb surpasses those reported for the best artificial synthetic analogues (Table 2).

Table 2 kORR of different ORR catalysts.

The G65YCuBMb biosynthetic Mb scaffold-based bio-electrode for O2 reduction is remarkably stable. Monolayers bearing covalently attached O2-reducing electrocatalysts reported so far have never been stable enough to allow these dynamic electrochemical experiments to determine the kinetic parameters (kORR, number of electrons and so on). Enzymes like laccases, directly attached to chemically modified graphite electrodes, were found to be stable enough to be investigated with these hydrodynamic techniques27. The failure to perform these experiments has been attributed to degradation of the catalyst during RDE experiment, that is, very small turnover numbers presumably due to the production of PROS during ORR. Rotating ring disc electrochemistry (RRDE) shows formation of only 6% PROS by the G65YCuBMb (Supplementary Fig. 7) during ORR, indicating that it reduces 96% of O2 to H2O consistent with the RDE data. During the RDE experiments (Fig. 4a), the G65YCuBMb-functionalized electrodes bearing 10−12 mol of the catalyst reduced 1.8±0.3 × 10−8 mol of O2 (7±1 × 10−3 C total charge and 4e per O2 molecule) yielding a turnover number of at least 104. The role of PROS in degrading the catalyst is established by the fact that the electrolytic current (at −0.3 V) remains stable in the presence of 50 μM catalase in solution (Supplementary Fig. 8).

Discussion

To understand the facile and selective O2 reduction catalysed by the G65YCuBMb biochemical model, the recently developed SERRS-RDE technique is employed42. In this technique, the rR spectra of the catalyst (that is, G65YCuBMb) bearing electrode is collected while the system is involved in steady state O2 reduction and the species accumulated in the steady state can be identified. For any species to accumulate in steady state, its rate of formation has to be greater than its rate of decay. Thus, while the species preceding the rate-determining step (rds) will accumulate at steady state, the accumulation of a species in steady state does not immediately imply its decay as the rds. In the absence of O2, a high spin ferrous species is formed, characterized by a ν4 and ν3 vibrations at 1,357 cm−1 and 1,473 cm−1 (Fig. 5a, cyan), respectively, when a cathodic potential of −0.4 V is applied signifying reduction of the resting ferric state (Fig. 5a, red) to the active ferrous state at these potentials. However, when the same reducing potential is applied in an oxygenated buffer the SERRS-RDE data (Supplementary Fig. 9) clearly show the presence of different species during electrocatalytic ORR, which leads to broadening of the ν4, ν3 and ν2 regions (Fig. 5a, green) relative to the oxidized and reduced states (Fig. 5a, red and cyan). In particular, the ν3 and ν2 vibrations discernibly shift to higher energies as indicated by clear increase in intensities at 1,508 cm−1 and 1,591 cm−1 (Fig. 4b), suggesting the accumulation of FeIV=O species during steady state ORR43. Signals from high spin ferrous, resting high spin ferric, low spin ferric and ferryl species with ν3 at 1,473 cm−1 (Fig. 5a, cyan; and Fig. 5b, brown), 1,493 cm−1 (Fig. 5a, red and Fig. 5b, dashed green), 1,504 cm−1 (Fig. 5a, cyan and Fig. 5b, cyan) and 1,508 cm−1 (Fig. 5a, green and Fig. 5b, green), respectively, could be convoluted by fitting the ν3 region of the spectrum. The lack of significant signal from the high spin ferrous species (weak ν3 at 1,473 cm−1) suggests that O2 binding to these species is facile in the steady state. These mutants use the basic design of Mb which has a very fast O2-binding rate (107 M−1 s−1) (refs 44, 45). This rate is indeed 10 times faster than O2 binding to the haem a3 site of CcO (ref. 46). Similarly, the very weak intensity of the high spin (HS) FeIII species indicates that the ET to FeIII resting state is very facile at these potentials as may be expected due to direct attachment of the Hemin-yne to the electrode. The significant intensity of ferryl species (ν2 at 1,591 cm−1 and ν3 at 1,508 cm−1) entails the O–O bond cleavage leading to its formation to be faster than its decay via reduction under steady state. Thus the reduction of the resting FeIII state, O2 binding to FeII are facile in G65YCuBMb under the reaction conditions. The low spin ferric species accumulated during steady state ORR could be a dioxygen adduct or peroxide adduct similar to those observed in native CcO and its model systems46,47,48,49,50,51. The low frequency region shows 18O2-sensitive bands suggestive of the formation of a low spin ferric peroxide and Fe(IV)=O (Supplementary Fig. 10).

Figure 5: SERRS-RDE data of G65YCuBMb-bearing electrode.
figure 5

(a) SERRS-RDE data of G65YCuBMb-bearing electrode at oxidized (applied potential was 0 V with respect to Ag/AgCl reference electrode), reduced (applied potential was −0.4 V with respect to Ag/AgCl reference electrode) state and in the presence of O2 (O16) saturated 100 mM pH 7 phosphate buffer and (b) Components of the rR spectrum determined by simulating the spectra of G65YCuBMb-bearing electrode in the presence of O2 (O16) saturated 100 mM pH 7 phosphate buffer indicated in green in a.

If one were to conceive of a Gedanken steady state turnover experiment with CcO where the electron transfer to the active site is very fast (that is, in the hypothetical situation where ET from Cyt c to CcO is not the rds) as the ET from the electrode to the active site is very fast due to direct attachment of the later to the former, the species that would accumulate during turnover, based on the Babkock–Wikström mechanism (Fig. 6, the parameters of native CcO are indicated in purple and G65YCuBMb are indicated in green52 and the arrows in black indicate general route for O2 reduction by CcO followed in both the native system, as well as in the G65YCuBMb-immobilized electrode) are the FeII,FeII-O2, FeIII-O22−, FeIII-OOH, FeIV=O and FeIII-OH species as the rates of formation of these species are greater than their rates of decay53,54. Out of these, the FeII-O2, FeIII-O22− and FeIII-OOH species will have Raman signatures of low spin haem (Fig. 6), FeIII-OH will have rR signature of high spin haem and the FeIV=O will have signatures unique to haem ferryl species46,54,55. The SERRS-RDE data show the presence of species having signatures of low spin FeIII and FeIV=O. While the later can originate from only a single species, the former can indicate the presence of any of the three species or a combination of them. The lack of significant high spin signal indicates that the biosynthetic model circumvents accumulation of FeIII-OH and resting FeIII species in the steady state by facile ET. The overall rate-limiting step of native CcO in solution is the dissociation of hydroxide of the FeIII-OH end product of O2 reduction from haem to generate the active ferric resting form and has a first order rate constant of 500 s−1 (refs 46, 54, 55, 56). This dissociation is required during turnover as the potential of this hydroxide-bound form is likely to be more negative that the five-coordinate resting oxidized site (which will be regenerated after hydroxide dissociation) and will not be reduced by haem a. While the E1/2 of a haem a3 FeIII-OH species cannot be determined with confidence due to strong interaction potential and co-operativity between the haem a and haem a3 sites, the potential of formate and azide-bound high spin haem a3 site (analogous to hydroxide) is 130 to 200 mV more negative than the resting ferric site57,58. The potential determining step of ORR (defined as the electron transfer (ET) step in catalysis having lowest potential) by the G65YCuBMb is 166 mV more negative than the E1/2 for the resting high spin ferric state and is likely to be the reduction of the FeIII-OH species. Thus the bioelectrode can circumvent the kinetic barrier associated with the dissociation of the hydroxide by directly reducing it to ferrous at 166 mV lower potential. This direct electron transfer to the ferric hydroxide species, which is an intermediate in the catalytic cycle of CcO, circumventing a slow step in catalysis, is an electron transfer shunt analogous to peroxide shunt in cytochrome P450, which overcomes the rate-determining O2 activation step of the native enzyme59. In the mass transfer controlled region of the catalytic current, all ET steps are facile and steps like O2 binding, protonation and O–O bond cleavage can be rds at these potential. The lack of HS FeII accumulation in the SERRS-RDE indicates that O2 binding to FeII is very fast and not the rds. The O–O bond cleavage in the Babkock–Wikström mechanism involves ET to the active site and not the rds as well. Thus rds of ORR by these biosynthetic models is likely to be the protonation of the FeIII-O2 species with a first order rate of 5,000 s−1 (Fig. 6).

Figure 6: Mechanisms.
figure 6

Comparison between the mechanism of native CcO (ref. 46) in solution and the biosynthetic G65YCuBMb model on electrode.

In an air-saturated buffer (0.26 mM O2), the pseudo first order rate constant of ORR by G65YCuBMb is determined to be 5–6 × 103 s−1 (kORR [O2]).The highest second order O2 reduction rate reported for any synthetic mimic of CcO is 1.2 × 105 M−1 s−1; that too on a multilayer having 1,000 times more catalyst than the G65YCuBMb electrodes60. The second order rate constant of G65YCuBMb is 107 M−1 s−1 which is, thus, 2 orders of magnitude higher than best synthetic haem/Cu-based O2 reduction electrocatalyst. Thus the selectivity and kinetic rate of the G65YCuBMb-bearing electrode surpasses those reported for smaller synthetic analogues and illustrates the advantages of using a biochemical scaffold over a synthetic scaffold. Although the pseudo first order rate constant of the G65YCuBMb is 10 times faster than the rate of native CcO in solution, such a comparison is vulnerable to differences in reaction conditions (for example, G65YCuBMb is water soluble but CcO exists in membranes). Alternatively, erstwhile efforts resulting in electrodes bearing native CcO in a manner similar to these bio-electrodes show extremely sluggish O2 reduction60,61,62. This is due to improper alignment of this membrane-bound protein on the electrode, which precludes efficient electron transfer to the active site63,64,65. However, the direct attachment of haem to the electrode utilizing its solvent-exposed propionate groups (that is, a short circuit) enables fast electron transfer to the active site29. This is further supported by the fact that when ethynylferrocene (Fc) is attached to the same surface 25 mV peak separation is observed even at 5 V s−1 (Supplementary Fig. 11)38, suggesting that the ET is indeed fast. As a result when a CcO-functionalized SAM-covered Au electrode produces <1 μA electrochemical O2 reduction current at −300 mV, this bio-electrode produce 100 μA current at similar potentials66.

Finally, the G65YCuBMb mutant has residues in the distal pocket that can help both electron and proton transfer during O2 reduction (Y65 in G65YCuBMb). In CcO, the involvement of Tyr 244 residues in proton/electron transfer during O2 reduction is now widely accepted67,68. Previous biochemical and structural studies on these mutants had indeed indicated the close proximity of this residue to the distal site7,19,30. An analogous biochemical model without the Y65 residue, CuBMb, is not as stable as the G65YCuBMb as the former degrades rapidly during the RDE experiments (Supplementary Fig. 12). In summary, a electron transfer shunt which circumvents the rate-determining dissociation of a ferric hydroxide species by directly reducing it at slightly negative potential, fast O2 binding, fast electron transfer to the active site and the presence of a protective Y65 residue in a biochemical model of CcO results in O2 reduction activity 100 times faster than the best synthetic models, order of magnitude faster than CcO immobilized on electrode and follows a mechanism comparable to that of native CcO in solution.

Methods

Materials

1-Azidoundecane-11-thiol and Hemin-yne were synthesized following the reported procedure29,69. 6-Mercaptohexanoic acid was purchased from Sigma Aldrich. Di-sodium hydrogenphosphate dihydrate (Na2HPO4. 2H2O) was purchased from Merck. 2, 6-lutidine was purchased from Avra Synthesis Pvt. Ltd. These chemicals were used without further purification. Au wafers were purchased from Platypus Technologies (1,000 Å of Au on 50 Å of Ti adhesion layer on top of a Si(III) surface). Transparent Au wafers (100 Å of Au on 10 Å of Ti) were purchased from Phasis, Switzerland. Au and Ag discs for the RRDE and SERRS experiments, respectively, were purchased from Pine Instruments, USA. The Mb mutants were prepared as reported in the literature7,30. Analysis of the components of the rR spectrum was done by using Lorenztian line shape of peak fit software.

Instrumentation

All electrochemical experiments were performed using a CH Instruments (model CHI710D Electrochemical Analyzer). Bipotentiostat, reference electrode and Teflon plate material evaluating cell (ALS, Japan; http://www.als-japan.com/1398.html) were purchased from CH Instruments. The RRDE set-up from Pine Research Instrumentation (E6 series ChangeDisk tips with AFE6M rotor) was used to obtain the RRDE data. The mutant Mb-functionalized or SAM-covered Au surface (disc of 0.1 cm2 area for RDE, RRDE and wafer of 0.45 cm2 area for CV) was always used as the working electrode. The XPS data were collected in a Omicron (model: 1712-62-11) spectrometer using a high-resolution monochromatic Al-Kα source at 1,486.7 eV under 15 kV voltage and 10 mA current maintaining a base pressure of 5 × 10−10 mbar. The binding energies were calibrated to the Ag 3d5/2 peak at 368.2 eV. The resonance Raman experiments were done in the Kr+ Laser (Sabre Innova, Model—SBRC-DBW-K) purchased from Coherent, and the data were collected using the Spectrograph (Model—Trivista 555) from Princeton Instruments.

Formation of mixed SAM and covalent attachment of Hemin-yne to it

Mixed self-assembled monolayer of 1-azidoundecan-11-thiol and 6-mercaptohexanoic acid was formed on immersing the properly cleaned Au wafers or disks into the deposition solution containing 1-azidoundecan-11-thiol and 6-mercaptohexanoic acid in 10 ml of ethanol in a desired ratio (typically 1:49). The total thiol concentration of these deposition solutions were always maintained at 1 mM. On this SAM Hemin-yne was covalently attached using ‘Click’ reaction29.

Reconstitution of Apo-G65YCuBMb mutants to G65YCuBMb

For all the experiments on heterogeneous SAM surfaces, the Hemin-yne modified –COOH SAM surfaces were incubated with a 20 μM apoprotein (Apo-G65YCuBMb) solution for 2 h. The supernatant solution was drained and the surface was cleaned with water. The presence of Cu2+ in the non-haem-binding site is confirmed by electron paramagnetic resonance (EPR) spectroscopy (Supplementary Fig. 13). The immobilization of the mutant is further confirmed by the absorption spectra and SERRS of the surface fabricated with those mutants (Supplementary Fig. 14, Supplementary Fig. 15).

Cyclic voltammetry

The CV was performed using Au wafers sandwiched between two Teflon blocks of the Plate material evaluating cell. All electrochemical experiments were done in pH 7 phosphate buffer containing potassium hexafluorophosphate. Anaerobic cyclic voltammetric experiments were done by using degassed buffer (three cycles of freeze–pump–thaw). Ag/AgCl reference electrode and Pt counter electrode were used throughout all the electrochemical experiments except the case of anaerobic experiments where only Ag wire was used as the reference electrode.

The peak areas were estimated by integrating the anodic/cathodic peak of the anaerobic CV of the mutant Mb-functionalized SAM-covered Au surface, using the data acquisition software itself. A line collinear with the background is used to subtract the background. The estimated area has been further confirmed by subtracting the background current of a SAM-functionalized electrode (Supplementary Fig. 11) bearing ferrocene. Both these approaches provide the same estimate.

To ensure that the SAM surface is stable during the electrocatalytic investigations, disc bearing just the SAM was subjected to several rotations (200–1,000 r.p.m.) and its capacitive current was found not to change, indicating that the SAM is retained on the electrode during these dynamic electrochemistry experiments (Supplementary Fig. 16). SAM can also be damaged when the protein atop the SAM degrades during ORR due to the reactive oxygen species produced. When an unstable electrocatalyst (Hemin-yne) decayed there was a steady loss of ORR current, indicating degradation of the active site but the capacitive currents of the SAM were unaltered (Supplementary Fig. 17).

SERRS and SERRS-RDE

The excitation wavelength used in the Resonance Raman experiments was 406.7 nm and the power applied to the sample was 10–15 mW. The spectrograph was calibrated against naphthalene. The Ag surfaces were roughened before SERRS experiments following literature protocols70. The SERRS-RDE set-up is described in ref. 42. The data for the oxidized state was obtained by holding the potential of the disc at 0 mV versus NHE, and the data during steady state ORR was obtained by holding the disc at −400 mV versus NHE and the disc was rotated at 300 r.p.m. Normally data were acquired over a period of 300 s.

Additional information

How to cite this article: Mukherjee, S. et al. A biosynthetic model of cytochrome c oxidase as an electrocatalyst for oxygen reduction. Nat. Commun. 6:8467 doi: 10.1038/ncomms9467 (2015).