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			<titleStmt><title level='a'>Aqueous Photoelectrochemical CO &lt;sub&gt;2&lt;/sub&gt; Reduction to CO and Methanol over a Silicon Photocathode Functionalized with a Cobalt Phthalocyanine Molecular Catalyst</title></titleStmt>
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				<publisher></publisher>
				<date>01/23/2023</date>
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				<bibl> 
					<idno type="par_id">10463191</idno>
					<idno type="doi">10.1002/anie.202215213</idno>
					<title level='j'>Angewandte Chemie International Edition</title>
<idno>1433-7851</idno>
<biblScope unit="volume">62</biblScope>
<biblScope unit="issue">4</biblScope>					

					<author>Bo Shang</author><author>Conor L. Rooney</author><author>David J. Gallagher</author><author>Bernie T. Wang</author><author>Andrey Krayev</author><author>Hadar Shema</author><author>Oliver Leitner</author><author>Nia J. Harmon</author><author>Langqiu Xiao</author><author>Colton Sheehan</author><author>Samuel R. Bottum</author><author>Elad Gross</author><author>James F. Cahoon</author><author>Thomas E. Mallouk</author><author>Hailiang Wang</author>
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			<abstract><ab><![CDATA[Abstract                          We report a precious‐metal‐free molecular catalyst‐based photocathode that is active for aqueous CO              2              reduction to CO and methanol. The photoelectrode is composed of cobalt phthalocyanine molecules anchored on graphene oxide which is integrated via a (3‐aminopropyl)triethoxysilane linker to p‐type silicon protected by a thin film of titanium dioxide. The photocathode reduces CO              2              to CO with high selectivity at potentials as mild as 0V versus the reversible hydrogen electrode (vs RHE). Methanol production is observed at an onset potential of −0.36V vs RHE, and reaches a peak turnover frequency of 0.18s              −1              . To date, this is the only molecular catalyst‐based photoelectrode that is active for the six‐electron reduction of CO              2              to methanol. This work puts forth a strategy for interfacing molecular catalysts to p‐type semiconductors and demonstrates state‐of‐the‐art performance for photoelectrochemical CO              2              reduction to CO and methanol.]]></ab></abstract>
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<div xmlns="http://www.tei-c.org/ns/1.0"><p>Anthropogenic CO 2 emissions and their contribution to climate change have made the development and implementation of carbon-neutral energy generation and storage a global priority. The United Nations Paris Agreement targets a 45 % reduction in global emissions by 2030 and carbonneutrality by 2050. <ref type="bibr">[1]</ref> As a potential carbon-neutral or carbon-negative technology, electrochemical CO 2 reduction reactions convert the greenhouse gas into value-added chemical building blocks or liquid fuels by using only water and electricity as additional inputs. <ref type="bibr">[2]</ref> Photoelectrocatalytic (PEC) CO 2 reduction further lowers the energy input by harvesting solar energy in tandem with an applied voltage. <ref type="bibr">[3]</ref> Major challenges of the CO 2 reduction reaction are its slow kinetics, low selectivity owing to the plurality of possible products, and competition for electrons by the hydrogen evolution reaction (HER). As the key to lowering the overpotential and achieving high activity and selectivity towards a single CO 2 reduction product, a variety of catalysts have been explored for modification of the photocathode in the PEC CO 2 reduction reaction. <ref type="bibr">[4,</ref><ref type="bibr">5]</ref> Among them, molecular catalysts are advantageous due to their well-defined structures, which are readily modified to tailor the reaction kinetics. Their detailed reaction mechanisms can also be probed by the well-developed tools of molecular chemistry. A number of molecular catalysts have been deposited on semiconductor surfaces for PEC CO 2 reduction and have shown promising activity. <ref type="bibr">[6]</ref><ref type="bibr">[7]</ref><ref type="bibr">[8]</ref><ref type="bibr">[9]</ref><ref type="bibr">[10]</ref> However, many of these systems require noble metal catalysts or expensive compound semiconductors, which makes the cost of the PEC electrode high.</p><p>Si is a preferred photo-absorber for PEC CO 2 reduction because of its low cost and well-studied properties as the backbone of the semiconductor industry. Many molecular catalysts have been studied in the solution phase with Si photocathodes, <ref type="bibr">[11]</ref><ref type="bibr">[12]</ref><ref type="bibr">[13]</ref><ref type="bibr">[14]</ref> but in this configuration, the catalyst must diffuse to and from the photoelectrode and the achievable catalytic rates are therefore low. The development of a high-performance and low-cost Si photocathode with an anchored molecular catalyst for selective PEC CO 2 reduction in aqueous media remains a largely unmet challenge. A few recent reports have made progress towards this goal. Reisner et al. developed a photocathode consisting of p-type Si (p-Si) coated with a mesoporous TiO 2 layer and functionalized with cobalt bis(terpyridine) anchored via phosphonate groups. The resulting photoelectrode is active for PEC CO 2 reduction in a mixture of acetonitrile and water, producing a photocurrent of about &#192;0.18 mA cm &#192;2 with Faradaic efficiencies (FEs) for CO and formate of 48 % and 13 % respectively. <ref type="bibr">[15]</ref> In a subsequent study, the Reisner group used the same anchoring strategy for phosphonated cobalt phthalocyanine (CoPcP) and demonstrated improved performance in fully aqueous PEC CO 2 reduction. The p-Si j mesoTiO 2 j CoPcP photoelectrode achieves a photocurrent of &#192;0.15 mA cm &#192;2 and a FE CO of 66 % with the assistance of a bias of &#192;0.11 V vs the reversible hydrogen electrode (RHE), representing the state-of-the-art p-Si photocathode functionalized with a molecular catalyst for CO 2 reduction. <ref type="bibr">[7]</ref> Higher performance was realized by Li and co-workers with p-n junction Si. <ref type="bibr">[6]</ref> These findings open the door for further investigation to improve the rate and selectivity of PEC CO 2 reduction not only to CO but also to more deeply reduced products.</p><p>Recent work from our group has demonstrated that the immobilization of cobalt phthalocyanine (CoPc) molecules onto carbon nanotubes (CNTs) enhances their electrocatalytic performance. The planar aromatic ligand structure of CoPc enables non-covalent &#960;-&#960; stacking with the graphitic carbon surface. This strong electronic interaction promotes highly dispersed CoPc molecules on the CNT surface and fast electron transfer from the electrode to the active site. The CoPc/CNT catalyst produces CO with &gt; 95 % FE at low overpotential in electrochemical CO 2 reduction. <ref type="bibr">[16]</ref> Remarkably, at more negative applied potentials this hybrid catalyst is active for the six-electron reduction of CO 2 to methanol (MeOH) with FE higher than 40 %. <ref type="bibr">[17]</ref> CoPc/CNT is one of the very few molecular catalysts demonstrated to reduce CO 2 by greater than two electrons with appreciable activity and selectivity. Nevertheless, the six-electron reduction of CO 2 to MeOH over a molecular catalyst on Si-based photocathodes has not been reported to date.</p><p>In this work, we develop a p-Si photocathode interfaced with CoPc molecules immobilized on graphene oxide (GO/ CoPc) for PEC CO 2 reduction to CO and MeOH. Our photocathode architecture is composed of p-Si protected by a 2 nm thick film of TiO 2 , functionalized with (3aminopropyl)triethoxysilane (APTES), and coated with the GO/CoPc catalyst. Each component of this architecture makes an indispensable contribution to the PEC performance. The assembled photoelectrode shows CO production in a near neutral aqueous electrolyte at 0 V vs RHE (all potentials in this work are referenced to RHE unless otherwise stated) and reaches a maximum FE CO of 86 % and a current density of 0.5 mA cm &#192;2 at &#192;0.19 V under 1.5 sun illumination (300 W Xe lamp, 400 nm cut-off). MeOH is generated at an onset potential of &#192;0.36 V and reaches a maximum FE of 8 % at &#192;0.62 V. This work sets a new benchmark performance for p-Si photocathodes modified with a molecular catalyst in aqueous PEC CO 2 reduction to CO, as well as the photoelectrochemical production of MeOH for the first time at illuminated p-Si electrodes.</p><p>The GO/CoPc catalyst was assembled by non-covalent &#960;-&#960; stacking similar to our previously developed method for immobilization of CoPc on CNTs. First, GO was prepared by a modified Hummer's method (Supporting Information section 1.a). CoPc molecules were then assembled onto the GO flakes by ultrasonication in N,N-dimethylformamide (DMF) (Figure <ref type="figure">1a</ref>). GO serves as a conductive support to enable molecular-level dispersion of CoPc and facilitate electron conduction. <ref type="bibr">[18]</ref> Inductively coupled plasma mass spectrometry (ICP-MS) was used to determine the CoPc loading on the GO. The Co loading was found to be 0.24 wt.%, corresponding to a CoPc loading of 2.3 wt.%. Atomic force microscopy (AFM) identifies GO/CoPc flakes with an average lateral size of &#65533; 1 &#956;m (Figure <ref type="figure">1b-d</ref>). Tipenhanced Raman spectroscopy (TERS) was employed to further characterize the distribution of the CoPc molecules on GO (Figure <ref type="figure">1e-f</ref>). TERS mapping, using the strongest Raman feature of CoPc at 1530 cm &#192;1 (Figure <ref type="figure">S1</ref>), confirmed the relatively uniform distribution of CoPc molecules on GO (Figure <ref type="figure">1e</ref>). <ref type="bibr">[19]</ref> The corresponding Raman spectrum of the hybrid catalyst shows clear combined features of CoPc and GO (Figure <ref type="figure">1f</ref>). <ref type="bibr">[20]</ref> These results confirm the successful assembly of CoPc on GO.</p><p>The preparation of Si-based GO/CoPc photoelectrodes was achieved in a stepwise assembly. First, a lightly doped ptype Si wafer (B doped, 1-10 &#937; cm), pre-cleaned with a buffered HF solution to remove the surface oxide layer, was coated with 2 nm TiO 2 as a surface protection layer by atomic layer deposition (ALD) (Supporting Information section 1.c). The Si-TiO 2 wafers were cut into squares with 1 cm 2 area and treated with an APTES solution, during which the APTES molecules react with TiO 2 surface oxygen groups via silanization, leaving the free amine groups of the molecules exposed. <ref type="bibr">[21]</ref> Finally, the Si-TiO 2 -APTES (STA) substrate was soaked in a GO/CoPc aqueous dispersion to form a monolayer-like coating on the surface with the aid of electrostatic and hydrogen bonding interactions between the APTES amine groups and the GO carboxylic acid groups (Figure <ref type="figure">2a</ref>). <ref type="bibr">[22]</ref> After each coating step, the contact angle of water on the substrate decreases, indicating successful functionalization of APTES and GO/CoPc on the substrate (Figure <ref type="figure">S2</ref>). Scanning electron microscopy (SEM) and AFM images in Figure <ref type="figure">2b</ref>-c confirm the uniform distribution on the micrometer scale of GO/CoPc flakes on STA. To provide more catalytic sites for CO 2 reduction, 0.05 mg of GO/CoPc was further drop-cast onto the 1 cm 2 photoelectrode, resulting in an approximately 600 nm thick catalyst layer (Figure <ref type="figure">2d-e</ref>). The prepared photoelectrode is denoted as STA-GO/CoPc.</p><p>The electrocatalytic activity of GO/CoPc deposited on carbon fiber paper (CFP-GO/CoPc) and the PEC activity of STA-GO/CoPc for CO 2 reduction were evaluated in 0.1 M KHCO 3 aqueous electrolyte. Prior to all catalytic tests, electrodes were subjected to a mild reductive potential under inert atmosphere, which was done to partially reduce the GO layer (Figure <ref type="figure">S3</ref>). Electrocatalytic tests were performed in a custom-made H-cell with gas products analyzed by in-line gas chromatography and liquid products detected by <ref type="bibr">1</ref> H NMR after the 30-min reaction (Figures <ref type="figure">3a,</ref><ref type="figure">S4,</ref><ref type="figure">S5</ref>). In dark electrochemistry, CFP was chosen to be the substrate because it is electrically conducting as opposed to the semiconducting p-Si. The CFP-GO/CoPc electrode produces CO at an onset of &#192;0.5 V and reaches a peak FE CO of 82 % at &#192;0.7 V (Figure <ref type="figure">3b</ref>). The electrochemical CO 2 reduction performance of the GO/CoPc catalyst is similar to that in our previous work on CoPc immobilized on CNTs, despite a lower current which may be attributed to the lower conductivity of GO compared to CNTs. <ref type="bibr">[16]</ref> To investigate the PEC performance of GO/CoPc, the STA-GO/CoPc assembly was first back-contacted with a metal wire using In-Ga eutectic and silver paste. Then the backside (including the metal contact) of the PEC electrode was sealed with vacuum wax to allow only the front surface of the assembly to be exposed to the electrolyte (Figure <ref type="figure">S6</ref>). The same setup of the electrochemical cell was used for PEC CO 2 reduction except for a quartz window in the cathode compartment to allow illumination onto the photoelectrode (Figure <ref type="figure">3c</ref>). A 300 W Xe lamp was used as the light source and a UV filter was applied to remove wavelengths shorter than 400 nm in all experiments. Light intensity was calibrated to 1.5 suns for all PEC measurements unless otherwise specified. Interest-  ingly, even at a 0 V applied bias, the STA-GO/CoPc shows a high FE CO of 76 %. At an applied potential of &#192;0.28 V, the STA-GO/CoPc achieves a maximum FE CO of 86 % with a photocurrent density of 0.7 mA cm &#192;2 (Figure <ref type="figure">3d</ref>), which compares favorably to previous reports based on molecular catalysts on p-Si, and is comparable to studies using largeband gap semiconductors under such low overpotentials (Table <ref type="table">S1</ref>). <ref type="bibr">[6-15, 23, 24]</ref> To attain the same FE CO , the overpotential on STA-GO/ CoPc was more than 0.5 V lower compared to CFP-GO/ CoPc (Figure <ref type="figure">3e</ref>), which can be attributed to the photovoltage contribution from p-Si. Although STA-GO/CoPc gives a lower current density than CFP-GO/CoPc, it is worth noting that the catalyst loading on the STA-GO/CoPc samples was eight times lower, which is necessary to prevent the catalyst layer from peeling off during the PEC tests (Figure <ref type="figure">S7</ref>). Assuming that every CoPc molecule on the photocathode is active, the CO turnover frequency (TOF) of STA-GO/CoPc is calculated to be 1.5 s &#192;1 at &#192;0.28 V, which is higher than the 0.5 s &#192;1 determined for CFP-GO/ CoPc at &#192;0.7 V (Supporting Information section 2.f). The higher TOF on the photoelectrode can be attributed to the lower loading of CoPc. <ref type="bibr">[25]</ref> These results demonstrate that the STA-GO/CoPc photoelectrode architecture provides highly efficient catalytic active sites for PEC CO 2 reduction.</p><p>At higher overpotentials, GO/CoPc, like CoPc/CNT in our previous work, <ref type="bibr">[17]</ref> is active for the six-electron reduction of CO 2 to MeOH. In dark electrochemistry, CFP-GO/CoPc yields MeOH at an onset potential of &#192;0.8 V and reaches an optimal FE MeOH of 23 % at &#192;1.0 V (Figure <ref type="figure">4a</ref>). In the PEC case, we find that the STA-GO/CoPc photoelectrode generates MeOH at a much lower onset potential of &#192;0.36 V and reaches a peak FE MeOH of 8 % at &#192;0.62 V (Figure <ref type="figure">4b</ref>). The 13 C isotopic labeling experiment confirms that CO 2 is the MeOH source (Figure <ref type="figure">S8</ref>). At &#192;0.62 V, STA-GO/CoPc produces MeOH with a TOF of 0.18 s &#192;1 , which is similar to the TOF for MeOH of CFP-GO/CoPc at &#192;1.0 V measured to be 0.21 s &#192;1 . We propose that the mechanism of MeOH formation in the PEC reaction is likely to be the same as in electrocatalytic CO 2 reduction, and that CO is the key intermediate to the formation of MeOH. <ref type="bibr">[17,</ref><ref type="bibr">[26]</ref><ref type="bibr">[27]</ref><ref type="bibr">[28]</ref> The optimal potential for FE MeOH of STA-GO/CoPc is about 0.4 V lower than that of CFP-GO/CoPc (Figure <ref type="figure">4c</ref>), demonstrating the photovoltage contribution from the Si to the catalyst. The lower optimal FE MeOH on STA-GO/CoPc compared with CFP-GO/CoPc may be due in part to the planar structure of the Si substrate; that is, the planar electrode is not able to trap the electrogenerated CO intermediate near its surface for further reduction as effectively as the porous CFP electrode. The lower catalyst loading, which leads to a slower rate of CO generation, may be another contributor. We hypothesize that improved MeOH selectivity may be accomplished by Si surface morphology engineering, which can be done using established techniques such as chemical treatment or photolithography, <ref type="bibr">[29]</ref> to increase surface roughness and manufacture porous Si for higher catalyst loadings and improved CO retention. Alternatively, gas diffusion layers can be employed as a top layer on the photoelectrode surface to increase mass transport of gas reactants to the active site. We will explore these strategies in future work. In summary, for dark electrocatalytic CO 2 reduction, CFP-GO/CoPc shows peak CO selectivity of 82 % at &#192;0.7 V and peak MeOH selectivity of 23 % at &#192;1.0 V. For PEC CO 2 reduction, STA-GO/CoPc shows peak CO selectivity of 86 % at &#192;0.28 V and peak MeOH selectivity of 8 % at &#192;0.62 V. This is the first example of successful integration of a molecular catalyst on Si for PEC CO 2 reduction to MeOH, and demonstrates the potential of molecular catalysis for greater than two-electron reduction of CO 2 on Si photocathodes.</p><p>The stability of the STA-GO/CoPc photocathode for PEC production of CO and MeOH from CO 2 was tested under 1 sun illumination to better simulate real-world conditions. At an applied potential of &#192;0.19 V, the photoelectrode shows a stable FE CO of around 86 % and only slight decay in current density over 6 hours of continuous operation (Figure <ref type="figure">5a</ref>). The FE CO and photocurrent are comparable to the result from 30 min controlled potential photoelectrolysis under 1.5 suns (Figure <ref type="figure">3d</ref>). At an applied potential of &#192;0.62 V, the photocathode generates MeOH with a FE of 6 % for the first hour (Figure <ref type="figure">5b</ref>), which is slightly lower than that from the 30 min measurement under 1.5 suns (Figure <ref type="figure">4b</ref>). FE MeOH continues to decrease over the next two hours along with a concurrent increase in HER. This decay is likely due to the partial detachment of the catalyst layer caused by bubble generation and/or degradation of the APTES layer, <ref type="bibr">[30]</ref> which might expose HER-active sites on the Si surface. The stability tests under 1.5 sun illumination show similar results but with a slightly quicker decay in catalytic activity (Figure <ref type="figure">S9</ref>). We hypothesize that this detachment problem can be solved by engineering the Si surface to increase the surface roughness and improve the adhesion between catalyst film and substrate.</p><p>Admittedly, interfacing the hydrophilic GO/CoPc film on the smooth hydrophobic Si surface was a significant obstacle in this work (Table <ref type="table">S2</ref>). If the TiO 2 layer is omitted (Si with the native oxide layer as the substrate), the current drops to one-tenth of the current under optimal conditions, suggesting that charge recombination at the native oxide layer may be the dominant kinetic pathway (Figure <ref type="figure">S10</ref>). If the APTES binding layer is omitted, the GO/CoPc quickly peels off the electrode and a low current and FE CO is obtained (Figures <ref type="figure">S11,</ref><ref type="figure">S12</ref>). Without the drop-cast thick catalyst layer, the current and FE CO are also low because of the limited number of catalytically active sites and the uncovered STA surface, which is active for HER (Figures S13, S14). Notably, replacing GO/CoPc with the CNT/ CoPc catalyst resulted in a significant decrease in the photocurrent and stability, which can be explained by the high optical density of CNT (thus less light can reach the Si surface to generate electron-hole pairs) and the absence of interaction between CNT and APTES (Figure <ref type="figure">S15</ref>). Together, each layer of the STA-GO/CoPc plays a critical role in achieving high-performance PEC CO 2 reduction. The quantum efficiency (QE) of STA-GO/CoPc was tested using a power-adjustable 730 nm LED (Supporting Information section 2.c). The maximum QE values under low illumination power at applied potentials of &#192;0.2 V and &#192;0.7 V were 6.5 % and 40.6 %, respectively (Figure <ref type="figure">S16</ref>). When the illumination power was increased, the QE was observed to drop rapidly. This may indicate that charge separation of p-Si or the catalyst turnover rate may be limiting the QE under high-power illumination, limitations that could be overcome by constructing p-n junction photocathodes or by developing more active catalyst materials. <ref type="bibr">[6,</ref><ref type="bibr">17,</ref><ref type="bibr">31]</ref> In summary, for the first time, we demonstrate aqueous PEC CO 2 reduction to MeOH at a molecular catalystmodified Si photocathode. Additionally, the as-constructed STA-GO/CoPc photoelectrodes produce CO with high selectivity at ultralow overpotential owing to a photovoltage estimated to be greater than 0.5 V. The onset potential of CO generation is 0 V and an optimal FE CO of 86 % is achieved. Under higher applied potentials of &#192;0.36 V to &#192;0.62 V, MeOH emerges as a liquid product with FE MeOH up to 8 %. This study thus serves as a starting point for multi-electron PEC CO 2 reduction to liquid fuels at low overpotentials on hybrid photoelectrodes based on molecular catalysts on Si.</p></div></body>
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