The growing global energy demand, driven by population growth and industrial development, remains largely dependent on non-renewable sources for fuel and electricity. Molecular hydrogen (H₂) production technologies are pointed as key vectors for net-zero CO₂ emissions. It can be used as fuel due to its high energy density, producing only water as a by-product. Moreover, it also plays a vital role in the chemical industry, especially in fertilizer production and oil refining, with annual global demand reaching approximately 100 million tons in 2024^[1,2]. Photoreforming of alcohols, plastic residues and other organic compounds such as sugars and biomass-derived molecules has gained attention as a promising pathway for the so-called low-carbon hydrogen production^[3-6]. Moreover, photoreforming from agro-industrial waste streams couples solar energy conversion with the generation of fuels and chemicals, offering the dual benefit of hydrogen production and waste valorization^[7-9]. During the photocatalytic process, organic compounds, such as alcohols derived from biomass, industrial residues, or by-products like glycerol, are converted into hydrogen and valuable oxidation products^[7], including aldehydes, ketones, and carboxylic acids^[10-17].

In heterogeneous photoreforming, the process relies on a semiconductor material that absorbs light to yield electron-hole pairs. In general, a heterogeneous photocatalyst is an inorganic semiconductor whose electronic structure is defined by two main energy bands (valence and conduction bands), separated by an energy gap (bandgap). When the photocatalyst absorbs a photon with energy equal to or greater than the bandgap, an electron-hole pair is generated, which can either migrate to the surface and participate in redox reactions with adsorbed species, or recombine, dissipating the energy without producing chemical change^[18]. In the absence of molecular oxygen, the photogenerated electrons can drive proton reduction to produce hydrogen (H₂), while the holes promote the oxidation of the organic substrate, Figure 1A. In the absence of an organic substrate, the electron/hole pair can potentially promote water splitting, Figure 1B, which is kinetically and thermodynamically less favorable than photoreforming. If both O₂ and organic species are present, reactive oxygen species (ROS) are produced and can be used for environmental remediation purposes, Figure 1C.

Since most organic oxidation reactions are thermodynamically favorable, photoreforming uses light energy to drive charge generation and overcome the kinetic barriers associated with hydrogen production and substrate oxidation. Thus, the main challenge in the process is actually to control the oxidation step in order to increase selectivity for more valuable products, while simultaneously achieving efficient sunlight harvesting and suppressing charge recombination. Therefore, the photocatalyst is crucial in photoreforming, as its properties directly influence reaction efficiency, selectivity, and stability. Key characteristics include suitable band edge potential positions, a narrow bandgap for effective light absorption, high surface area, efficient charge separation, and chemical stability^[19,20]. Commonly reported photocatalysts for photoreforming include CdS^[21-24], graphitic carbon nitride (g-C₃N₄)^[25-28], TiO₂^[9,29-34], and perovskite-type metal oxides and halides^[35-37]. Among them, TiO₂ remains one of the most widely used due to its chemical stability, non-toxicity, low cost, and favorable band edge positions for both water and alcohol oxidation and H₂ evolution^[20,38]. Nevertheless, despite its potential, TiO₂-based photoreforming still faces important practical limitations, including the wide bandgap of TiO₂ (~3.2 eV), which restricts light absorption predominantly to the UV region, the fast recombination of photogenerated charge carriers, challenges associated with carbon efficiency and product separation, as well as scalability issues for large-scale hydrogen production^[4,5,10]. Moreover, most research in this field has focused on semiconductor materials development, while few studies are devoted to the systematic investigation of the influence of the organic species on the photoreforming process.

For instance, TiO₂ photocatalytic performance is also strongly influenced by its crystalline phase and structural design. Among its three crystalline forms (anatase, rutile, and brookite), anatase and rutile are the most widely employed in photocatalysis, while brookite is less explored due to its lower stability and more complex synthesis routes^[39]. Notably, mixed-phase TiO₂ systems, such as the commercial P25 photocatalyst, often exhibit superior performance because the anatase/rutile heterojunction promotes more efficient charge separation and interfacial electron transfer, while also improving light absorption^[39,40]. In addition, to overcome intrinsic drawbacks as UV-light dependence and rapid charge recombination, several modification strategies have been extensively investigated, such as doping^[41,42], modification with other semiconductors^[43-48], deposition of metallic co-catalysts (e.g., Pt, Ni, Ag, Cu, and Pd)^[49-53], incorporation of non-metallic co-catalysts^[54-56], and structural engineering approaches^[57,58]. These modifications also create additional catalytic active sites, thereby enhancing overall photoreforming efficiency^[7,9]. Other strategies include morphological engineering of TiO₂, such as the development of hierarchical 3D, mesoporous, macroporous, and supported architectures to improve substrate diffusion and light harvesting^[59-61]. In parallel, studies have highlighted the importance of metal-support interactions, particularly the influence of nanoparticle size and the metal/TiO₂ interface on reaction activity and selectivity^[62-65]. Furthermore, photothermal and tandem approaches integrating thermal energy^[66,67], plasmonic effects^[68,69], and heterojunction engineering^[70-72] have emerged as promising strategies to overcome kinetic limitations and improve the overall efficiency of photoreforming.

In this context, this review offers a comprehensive overview of research conducted on the photoreforming of alcohols and biomass derivatives using TiO₂-based photocatalysts. TiO₂, despite its low sunlight activity, was chosen as a benchmark due to the extensive mechanistic and photocatalytic data available in the literature, while also serving as an important model platform for understanding fundamental principles that can guide the design of more advanced photocatalysts^[20]. While previous reviews in the literature have mainly focused on TiO₂ photocatalytic properties or hydrogen evolution systems, the present work provides an updated perspective centred on photoreforming mechanisms and catalyst-engineering strategies. The fundamental aspects of the photoreforming mechanism are discussed in detail, with methanol used as a model to illustrate key reaction pathways and the main spectroscopic techniques used to evaluate them. The review also explores the influence of TiO₂ modification and the usage of co-catalysts on both hydrogen evolution and oxidative mechanisms. Furthermore, this review systematically compares the light-driven reforming pathways of C1-C6 alcohols, extending from methanol to more complex substrates such as glycerol and biomass-derived compounds, while discussing how molecular complexity influences oxidative pathways, intermediate formation, hydrogen evolution, and catalyst requirements. Therefore, Section "METHANOL PHOTOREFORMING AS A MODEL REACTION" initiates on methanol photoreforming as a model reaction to establish key mechanistic concepts and spectroscopic approaches. Subsequently, Section "PHOTOREFORMING OF C2+ ALCOHOLS" extends the analysis to C2+ alcohols, highlighting how increasing molecular complexity influences reaction pathways and intermediate formation. Finally, Section "GLYCEROL PHOTOREFORMING" addresses glycerol as a representative biomass-derived polyol, while Section "PHOTOREFORMING OF OTHER BIOMASS DERIVATIVES" covers other biomass derivatives.

Methanol is often used as a model compound to study the photocatalytic activity over different semiconductor surfaces^[73-76]. It is a simple molecule with a lower oxidation potential than water (0.103 V vs. standard hydrogen electrode for the methanol to formate oxidation)^[77]. It readily donates electrons during photocatalysis, suppressing the recombination of charge carriers. The first study on photocatalytic oxidation of methanol on TiO₂ dates back to the late 1970s and early 1980s^[78-81]. The photoinduced process starts with light absorption by the semiconducting material through band gap excitation (3.2 eV, the case of Anatase TiO₂), yielding an electron-hole pair or exciton. Once generated, these mobile charge carriers face a critical competition between productive and non-productive pathways, i.e., the effective promotion of redox reactions or the charge carrier recombination.

The non-productive electron-hole recombination occurs in a wide timescale range, from picoseconds to milliseconds depending on the structural properties of the semiconductor and dissipates the absorbed photon energy by radiative and/or nonradiative pathways. In TiO₂, an n-type semiconductor, the photoexcited electrons on the conduction band can be trapped in shallow or deep trap states in the oxide surface. Such trap states are typically oxygen vacancies (O_v), which can be understood as unpaired electrons, located initially in an O_2p orbital and then transferred, by the removal of the corresponding oxygen atom, into the conduction band formed by Ti_3d orbitals^[82,83]. Similarly, hole trapping can also occur at a bridging O^2- or surface-bound OH^- anions, resulting in the formation of O^•- or/and OH^• centres, respectively. Charge trapping and recombination dynamics are critical to the efficiency of the photocatalytic process and have been investigated by a myriad of time-resolved techniques.

Among them, Transient absorption spectroscopy (TAS) stands out because it provides direct, temporally resolved access to the dynamics of electrons, holes, excitons, and short-lived intermediates over an exceptionally broad temporal window. By tracking these species from femtoseconds to seconds, TAS uncovers mechanistic events that dictate photocatalytic performance, including exciton formation, hot-carrier cooling, charge separation, recombination pathways, carrier trapping, and interfacial charge transfer^[84-89].

Fundamental photophysics studies on TiO₂ nanoparticles revealed that electrons and holes are trapped onto the oxide surface within 50-150 fs following excitation. Electrons in the conduction band can be deeply trapped at the bulk within 50 ps, while holes are trapped in deep states at the surface within 200 fs^[90-93]. The overall lifetime of trapped holes and electrons will depend on the crystal structure of the photocatalyst, its surface composition, defect concentration, and the presence of adsorbed species.

Tamaki et al.^[90,94] investigated the reaction dynamics of the trapped holes by means of TAS in the presence of methanol and found that the transient absorption of the trapped holes decayed more rapidly, clearly indicating that trapped holes can react with the adsorbed alcohol on the surface. The lifetime of the trapped holes was around 300 ps in the presence of methanol. This ultrafast charge-transfer rate can be related to the adsorption behavior of methanol on the TiO₂ surface, which is predominantly dissociative, resulting in the formation of surface alkoxide and hydroxyl groups^[95-97]. Under UV irradiation, these surface alkoxide groups serve as effective hole trapping centers.

Generally, it is assumed that the hole or ^•OH-induced alcohol oxidation proceeds via two reaction steps (Eqs. 1 and 2), i.e., a dehydrogenation step resulting in the formation of the respective α-hydroxyalkyl radical, followed by the formation of the respective aldehyde under injection of an electron into the conduction band of TiO₂, which is known as “current doubling” effect^[93,98]. The presence of adsorbed water molecules has no influence on the hole transfer to methanol as shown by Shen and Henderson^[99], which confirms that the direct hole transfer to the adsorbed organic molecule is the dominant oxidation pathway, rather than an indirect mechanism involving the generation of freely diffusing hydroxyl radicals. The proposed mechanism resembles that proposed by Henglein in the early 70’s, which carried out a series of pulse-radiolytic experiments to investigate the reactivity of hydroxyl radicals with aliphatic alcohols in aqueous solutions^[100,101]. The authors observed that methanol reaction with OH leads to the formation of the reducing CH₂OH -hydroxiradical with 93% yield, with the oxidizing methoxy radical (CH₃O) as a minor product.

(1) $$ \begin{equation} \begin{aligned} \mathrm{CH}_{3} \mathrm{OH} \mathrm{----} \mathrm{O}\left(\mathrm{TiO}_{2}\right) \rightleftharpoons \mathrm{CH}_{3} \mathrm{O}^{-} \mathrm{----}^{+}\mathrm{HO}\left(\mathrm{TiO}_{2}\right) \xrightarrow{h\nu}{ }^{\bullet} \mathrm{CH}_{2} \mathrm{O}+\mathrm{H}^{+} \end{aligned} \end{equation} $$

(2) $$ \begin{equation} \begin{aligned} \dot{\mathrm{C}} \mathrm{H}_{2} \mathrm{OH} \rightarrow \mathrm{HCHO}+\mathrm{e}^{-}\left(\mathrm{TiO}_{2}\right) \end{aligned} \end{equation} $$

Continuous irradiation of oxygen-free methanol aqueous solutions in the presence of TiO₂ nanoparticles will ultimately lead to the formation of CO₂ as an oxidation product. However, if an excess of methanol is maintained in the course of the reaction, valuable oxidative products such as formaldehyde, formic acid, and even methyl formate can be obtained^[73]. The following steps after the initial photoinduced hole transfer from TiO₂ to adsorbed methanol molecules have been investigated by different groups.

Zhou and Guo have compared the oxidation of methanol and water on pristine Rutile TiO₂(110) surfaces by means of advanced surface characterization techniques such as atom-resolved scanning tunning microscopy, temperature-programmed desorption (TPD)/time-of-flight spectroscopy, and photoelectron spectroscopy in combination with theoretical calculations^[102,103]. Methanol adsorption on Ti⁴⁺ sites through its hydroxyl group lead to the formation of 5-fold coordinated Ti sites (Ti_5cs) onTiO₂ surface or, alternatively on bridging O_v. Both molecular and dissociative (proton transfer to the neighbouring oxygen on the surface) adsorption mechanism have been proposed. The energy difference between the two adsorption states is relatively small, so it is generally accepted that at higher temperatures they can easily interconvert between themselves. Under bandgap excitation, the adsorbed methanol molecules are photooxidized into formaldehyde by transferring both the hydroxyl and methyl hydrogen atoms to oxygen sites, reducing Ti⁴⁺ into Ti³⁺ ions. In fact, continuous irradiation of TiO₂ nanoparticles under oxygen-free methanol vapor leads to the build-up of bluish color ascribed to the Ti³⁺ d-d transition. Density functional theory (DFT) calculations reveal that the effective interfacial hole transfer is thermodynamically favored by the previous dissociation of the hydroxyl hydrogen to yield methoxy anions adsorbed on the surface (H₃CO^-). Very similar conclusions were drawn by Diebold and Seleni for Anatase (101) TiO₂^[104]. In this case, the proposed overall mechanism for formaldehyde formation is summarized in Figure 2.

The presence of metallic cocatalysts, such as Pt, not only allows the formation of molecular H₂ but also changes the energetics of the of hole transfer as the enhanced electron-hole separation intensifies the band bending and accelerate the photocatalyzed oxidation step^[105]. In fact, TAS measurements employing TiO₂ nanoparticles of different particle sizes, morphologies and crystalline phases reveal that Pt clusters on the oxide surface can efficiently scavenger the photoexcited electrons in the TiO₂ conduction band, improving considerably the lifetime of the charge carriers^[105,106]. Moreover, Kandiel et al. have provided evidence through isotopic studies that the molecular H₂ is mainly produced from protons originating from water^[107].

Al-Madanat and coauthors studied the influence of the platinum loading method on nanosized anatase TiO₂ on both reductive and oxidative half-reactions^[62]. Pt was added to TiO₂ either by physical mixing with laser-ablated Pt nanoparticles (PtLA-TiO₂) or via photodeposition (PtPD-TiO₂). Using sealed reactors under argon at 25 °C and under simulated solar irradiation (1000 W Xenon lamp), methanol and naphthalene were tested as substrates. For methanol, both platinized TiO₂ samples produced significantly higher amounts of acetaldehyde and formic acid compared to pristine TiO₂, with PtPD-TiO₂ showing about three times faster oxidation kinetics than PtLA-TiO₂. CO₂ formation was minimal but still higher for platinized samples, with PtPD-TiO₂ outperforming PtLA-TiO₂^[62]. Hydrogen production was negligible for pristine TiO₂ but substantially higher for the platinized catalysts, with PtPD-TiO₂ achieving a photonic efficiency of 15.6% vs. 6.1% for PtLA-TiO₂ after 1h of irradiation.

The superior performance of PtPD-TiO₂ is attributed to better Pt dispersion and smaller Pt islands, enhancing catalytic activity and charge separation. Increasing Pt loading in PtLA-TiO₂ only slightly improved activity but remained below that of PtPD-TiO₂^[62]. Overall, photodeposition of Pt provided a more effective and stable modification, especially enhancing hydrogen production and oxidation rates compared to physical mixing. Electron paramagnetic resonance (EPR) and TAS analyses has confirmed improved charge separation in PtPD, which was attributed to the preferential Pt deposition on the reductive {101} facets, enhancing electron transport. Interestingly, the enhancement achieved by Pt photodeposition strongly depends on the organic substrate. While the activity difference between PtPD-TiO₂ and PtLA-TiO₂ was not substantial for naphthalene in terms of photonic efficiency, methanol showed greater improvements. This was attributed to the current-doubling effect of methanol^[98,108,109], which increases the average number of photogenerated electrons per particle, thereby benefiting more from the superior electron-capturing ability of the photodeposited Pt clusters.

The role of Pt clusters in methanol photoreforming was also investigated by Zhou’s research group and compared to the pristine TiO₂ employing ultrahigh vacuum techniques and well-ordered single crystals^[110]. The authors conclude that Pt loading can favor the dissociation of methanol into methoxy and lower the desorption barrier of molecular hydrogen, which may work cooperatively for separating photoexcited charges to enhance the photocatalytic efficiency.

As expected, the main oxidative reaction pathway in the Pt/TiO₂ and pristine TiO₂ systems is similar, although with different kinetics. However, the presence of Pt clusters also leads to thermal dehydrogenation of methanol to CO species on the metal surface. Similar results were found by Walenta et al. using techniques such as Auger electron spectroscopy, TPD/reaction, isotopic labeling, and isothermal photoreactions^[111]. The photo-oxidation of methoxy species is identified as the rate-determining step in this process. Key findings include an initial "conditioning" of the photocatalyst. Platinum (Pt) serves as a cocatalyst, primarily facilitating the evolution of molecular hydrogen by promoting the dimerization of surface hydrogen atoms. The selectivity for formaldehyde formation is basically due to easier thermal desorption of the molecule in comparison to methanol^[111,112]. At temperatures below 250 K, the consecutive photooxidation of de aldehyde can be observed, leading to the formation of methyl formate, Equation 3.

(3) $$ \begin{equation} \begin{aligned} \mathrm{CH}_{3} \mathrm{O}_{\text {ads }}+\mathrm{CH}_{2} \mathrm{O}+h\nu \xrightarrow[\mathrm{Pt}/\mathrm{TiO}_{2}]{ } \mathrm{HCOOCH}_{3} \uparrow+\mathrm{H}_{2} \uparrow \end{aligned} \end{equation} $$

At room temperature and in aqueous solution, the consecutive oxidation of formaldehyde leads to formic acid (Eqs. 4 and 5) and ultimately CO₂. The methanol concentration, irradiance, pH, and photocatalyst load can be used to tune the selectivity as reported by Karimi Estahbanati and coauthors using TiO₂ P25 modified with 1% Pt^[10]. Hydrogen production from methanol significantly increased up to 10% concentration, remaining almost constant until 99%, which is consistent with the previous conclusion that the photooxidation of the adsorbed methoxy species is the rate-limiting step.

(4) $$ \begin{equation} \begin{aligned} \mathrm{CH}_{2} \mathrm{O}+ h\nu \underset{\mathrm{TiO}_{2}}{\longrightarrow} \mathrm{HCO}^{\bullet} \end{aligned} \end{equation} $$

(5) $$ \begin{equation} \begin{aligned} \mathrm{HCO}^{\bullet}+\mathrm{HO}^{\bullet} \rightarrow \mathrm{HCOOH} \end{aligned} \end{equation} $$

Kandiel et al. focused on the influence of physical and chemical parameters on the H₂ evolution rates and oxidation products distribution on methanol photoreforming^[113]. Different light intensities, pHs, and initial methanol concentrations were evaluated. The rate of photocatalytic H₂ evolution is found to strongly depend on the methanol concentration initially present in the suspension. It increases with alcohol concentration and levels off, reaching a plateau. Furthermore, higher photonic efficiencies are observed for H₂ evolution at low photon fluxes. Stochiometric amounts of formaldehyde are observed at short irradiation times independent of pH and methanol concentration. At longer irradiation times, formic acid and CO₂ appear as minor products, being slightly favored at basic pHs.

Eder et al. expanded the understanding of heterogeneous photocatalytic alcohol oxidation by emphasizing the critical role of surface chemistry and thermal reactions in determining catalytic activity^[114]. They found that the interaction of alcohols with TiO₂(110) surfaces can guide the development of new photocatalysts and challenge the conventional electrochemical model. Their approach was based on surface investigations under ultra-high vacuum (UHV) conditions, employing post-illumination TPD technique to distinguish thermal from photochemical reactions. Their study also observed the photochemical oxidation of tertiary alcohols, leading to the formation of ketones and alkanes even in the absence of cocatalysts. They argued that the electrochemical model, where only a set of redox reactions accounts for the overall outcome, does not adequately explain alcohol photoreforming in the gas phase, as exemplified in Figure 3. They proposed a hole-mediated disproportionation mechanism, involving the homolytic cleavage of C-H bonds and the formation of H₂ as a single-photon process. The authors highlighted the need for a holistic approach that integrates thermal surface chemistry and charge carrier dynamics for the rational design of photocatalysts. Although the study exhibits limitations such as the difficulty of replicating practical environments, it expands the scope of possible reactions and provides new guidelines aimed at innovative reactor concepts and selective oxidation under reductive conditions.

Interestingly, Courtois and collaborators investigated the origin of catalyst deactivation (“poisoning”) during the photoreforming of primary alcohols, such as methanol, on reduced rutile TiO₂(110) under ultrahigh vacuum^[115]. Contrary to the common attribution to increased trap states for charge carriers^[116], the loss of activity was linked to thermal back-reactions, particularly between surface hydroxyls and aldehyde intermediates formed during methanol photo-oxidation^[115]. These reactions regenerate methoxy species, reversing the desired oxidation step and progressively deactivating the surface. The absence of hydrogen evolution and the buildup of hydroxyl groups confirmed surface hydroxylation as the main cause of poisoning at room temperature. In contrast, tertiary alcohols like 2-methyl-2-pentanol, which undergo C-C bond cleavage instead of C-H oxidation, did not exhibit this deactivation, indicating that the effect arises from alcohol-specific back reactions rather than electronic or site-blocking factors^[115]. Overall, the study identifies thermal back-reactions as the key mechanism limiting primary alcohol photoreforming on TiO₂ surfaces.

Building upon the understanding of methanol photoreforming reaction steps, research efforts have increasingly focused on optimizing the activity and selectivity of photocatalysts. Material engineering has been a strategy to enhance the efficiency and selectivity of methanol photoreforming. By precisely tailoring the exposed crystal facets and introducing defects, the catalyst structure favored specific reaction pathways while improving charge separation. Yamakazi et al. explored rutile TiO₂ nanorods modified with Pt, aiming to maximize photocatalytic activity for H₂ production under visible light irradiation^[117]. Additionally, defect introduction was performed via hydrogen spillover during Pt deposition, enabling controlled formation of Ti³⁺ and O_v. Pt-loaded TiO₂ nanorods (TNR) reduced at 200 °C exhibited superior photocatalytic performance, producing hydrogen at rates approximately four times higher than conventional TiO₂ powders reduced at 600 °C under visible light irradiation (λ > 420 nm, 500 W Xe lamp) in methanol solution (50 vol%). This enhancement was attributed to the controlled introduction of Ti³⁺ species without excessive O_v and effective spatial charge separation facilitated by the exposure of both {110} and {111} facets^[117]. The aspect ratio of the nanorods, along with the balance between reductive {110} and oxidative {111} facets, played a critical role in catalytic efficiency. DFT calculations further revealed that oxygen vacancy formation is thermodynamically more favorable on the {111} facets, supporting the observed facet-dependent behavior.

Similarly, Hossein Hejazi and coauthors reported the influence of defect engineering in anisotropic brookite TiO₂ nanorods, considering also the substrate specificity^[118]. The nanorods were synthesized using hydrothermal methods, predominantly exposing the (210) facet. Defects were introduced through hydrogen reduction at 700 °C, enabling controlled formation of subsurface O_v and lattice distortions. Photocatalytic experiments using 1 wt% Pt as a cocatalyst showed that the methanol photoreforming rate was up to 11 times higher for the reduced anisotropic brookite in comparison to untreated brookite, achieving a specific methanol consumption of 99 mmol h^-1 m^-2 and hydrogen production of 88 mmol h^-1 m^-2. The catalyst showed clear substrate specificity, with methanol reforming being significantly more efficient than ethanol or isopropanol (50 vol%). The apparent quantum yield (AQY) for reduced brookite reached 33.5% at 334 nm but dropped to nearly zero in the visible range (≥ 380 nm). Experimental and DFT studies revealed that subsurface O_v, coupled with large electronic polarons, serve as active sites specifically for methanol oxidation. A direct correlation was established between the alcohol oxidation rate and hydrogen evolution, where methanol dissociation is favored by the combination of structural defects and exposed crystal facets in brookite^[118]. Comparisons with isotropic brookite and reduced anatase further confirmed that crystal morphology and orientation play a critical role in the formation of catalytic sites.

Another approach to increasing the efficiency of TiO₂-based photocatalytic methanol oxidation is surface-level modifications without altering the underlying crystal structure. Monocrystalline rutile TiO₂ with an exposed (110) surface offers an ideal model system for such investigations, particularly when coupled with the deposition of metal clusters as co-catalysts. The influence of their size and surface coverage remains insufficiently understood. By employing different cluster sources for size-selected deposition of Ni and Pt on TiO₂(110) under ultrahigh vacuum, Eder and coauthors evaluated distinct size- and coverage-dependent effects on the photocatalytic reforming of alcohols^[119]. Size-selected Pt and Ni clusters, ranging from single atoms to aggregates of over 47 atoms, were deposited on TiO₂(110) under UHV via laser ablation, achieving precise control over both cluster size and surface coverage from 0.1% to 2% of a monolayer. A detailed study of methanol photoreforming on TiO₂(110) under UHV (5 × 10^-7 mbar) at 300 K (UV laser of 242 nm) revealed strong co-catalyst effects linked to cluster size and coverage^[119]. The mechanism was based on the methanol partial oxidation, forming formaldehyde. Pt clusters consistently outperformed Ni, with Pt₁₀ achieving the highest turnover frequency of up to 4 H₂ molecules per site per second, while larger clusters showed diminished activity. In contrast, Ni activity improved with size and coverage but was limited by carbonaceous deposits. Hydrogen evolution followed second-order kinetics, confirming that surface H recombination is the rate-limiting step. The results highlight the critical role of sub-20 atom clusters and optimal coverage (< 1% monolayer) in maximizing H₂ production efficiency.

Furthermore, methanol reforming over Pd/P25 TiO₂ was investigated and compared with Au- and Cu-based catalysts, as well as with the photocatalytic water-gas shift (WGS) reaction (CO + H₂O → CO₂ + H₂)^[120]. First, methanol reforming was significantly faster than the photocatalytic WGS reaction. Since both CO and H₂O are produced during methanol reforming, the WGS reaction may contribute to overall H₂ generation, though it proceeds more slowly and is less frequently reported. Nanoparticles were deposited on TiO₂ via incipient wetness impregnation (IWI) (0.5 wt.%) and calcined at 400 °C, with Pd particles estimated at ~2.5 nm. Using a xenon arc lamp, photocatalytic methanol reforming and WGS reactions were tested in both liquid and gas phases. Pd/TiO₂ exhibited the highest H₂ production rate in the liquid phase (3.7 mL h^-1), and this rate approximately doubled in the gas phase, where small amounts of CO were also detected, suggesting partial desorption of CO intermediates, identified as a rate-limiting step. Notably, the observed H₂/CO₂ ratio exceeded the theoretical 3:1, due to significant CO₂ dissolution in water, as confirmed by pH monitoring, and CO₂ release upon heating. Au/TiO₂ was less effective than Pd for methanol reforming but showed superior performance in the photocatalytic WGS reaction, generating three times more H₂ than Pd/TiO₂^[120]. Cu/TiO₂, while not as efficient in the WGS reaction, demonstrated similar activity to Au in methanol reforming, making it a more cost-effective alternative. The study proposed a two-step mechanism: thermal decomposition of methanol on Pd into surface-bound CO and H₂, followed by photoinduced CO removal via reactive O^- species on TiO₂. These results also highlight the often-overlooked impact of CO₂ solubility in aqueous media on the apparent product distribution, underlining the importance of careful gas-liquid analysis in photocatalytic reforming studies.

An extensive study of redox dynamics of Pt and Cu nanoparticles on TiO₂ for methanol photoreforming was reported by Chiarello et al.^[121] The study employed in situ modulated excitation X-ray absorption spectroscopy (ME-XAS) during the gas-phase photocatalytic oxidation of methanol, under both aerobic and anaerobic conditions, as compared in Figure 4. The photocatalysts were synthesized in a single step using flame spray pyrolysis (FSP) and were tested for their ability to oxidize methanol to CO₂ in the presence (CH₃OH + 3/2 O₂ → CO₂ + 2H₂O) or absence (CH₃OH + H₂O → CO₂ + 3H₂) of oxygen under irradiation (300 W xenon lamp, 120 mW/cm²). Under anaerobic conditions, product formation included H₂, CO₂, formaldehyde, formic acid, and CO, with Pt/TiO₂ achieving the highest H₂ production rate (19.25 mmol·g^-1·h^-1), significantly outperforming both Cu/TiO₂ (~5.02 mmol·g^-1·h^-1) and pure TiO₂ (~4.94 mmol·g^-1·h^-1)^[121]. Interestingly, under aerobic conditions, pure TiO₂ outperformed the metal-modified catalysts, with CO₂ being the dominant product alongside formaldehyde, formic acid, methane, and CO. ME-XAS revealed that Pt acts as an active site for H₂ evolution under anaerobic conditions by reversibly switching between Pt⁰ and Pt⁴⁺, enabling hydrogen adsorption and proton reduction. In the presence of O₂, Pt facilitates methanol oxidation. Conversely, Cu undergoes light-enhanced redox cycling between Cu²⁺ and Cu⁺ under aerobic conditions, but under anaerobic conditions, Cu⁰ dominates. In addition, large Cu particles also hinder activity by blocking light and covering active TiO₂ sites. The study highlights Pt’s effectiveness in promoting H₂ evolution, emphasizing the limitations of Cu/TiO₂ systems under these conditions.

In contrast, other study shows that supported CuO could be reduced to 1-2 nm Cu⁰ nanoparticles, forming active species (≈1 wt.% Cu/TiO₂), which acted as efficient co-catalysts for hydrogen evolution^[63]. The study also evaluated the influence of alcohol concentration, and correlate H₂ production with alcohol physicochemical properties. Under UV irradiation (365 nm, 6.5mW cm^-2), Cu²⁺ reduction was driven by α-hydroxy radicals generated during alcohol oxidation. These radicals, strong electron donors, promote Cu^+/0 formation and enhance electron transfer to TiO₂, boosting charge separation and hydrogen evolution. The reduction rate and H₂ production followed the trend glycerol > ethylene glycol > methanol > ethanol, increasing with alcohol polarity, hydroxyl content, and lower oxidation potential. A similar trend was also observed for hydrogen generation by combining Cu₂O and TiO₂^[122].

In fact, copper modification has been extensively explored as an effective approach to enhance TiO₂ performance in methanol photoreforming without using precious metals^[123-125]. A particularly effective strategy reported by Cwieka et al. involves introducing Cu as atomically dispersed Cu⁺ and Cu⁰ species on the TiO₂ surface, without forming large Cu or Cu oxide nanoparticles, offering enhanced control over catalytic behavior and zero carbon emissions (CO or CO₂) during methanol photoreforming^[64]. Moreover, Cu-modified TiO₂ (1 wt%) enabled a zero-carbon methanol photoreforming process, as only H₂ was detected in the gas phase, with no trace of CO or CO₂. In this case, TiO₂ P90 was modified with highly dispersed copper via wet impregnation, followed by IR treatment (Vitalux 300 W) and calcination at 450 °C in a fritted glass reactor. In the liquid phase, carbon was fully retained as formaldehyde (~0.40 mmol) and formic acid (~0.41 mmol), confirming selective oxidation. The catalyst achieved an H₂ production rate of ~1.15 mmol·g^-1·h^-1, with excellent stability over 24 h of operation and even after 6 months of storage. Reproducibility was confirmed, and the system delivered 2.56 mmol·g^-1·h^-1·W^-1, with apparent quantum efficiency (AQE) of 10% (0.45 W LED source of 365 nm)^[64]. Mechanistically, the photocatalyst operates via a Cu⁺/Cu⁰ redox cycle, without Cu²⁺ formation, suppressing complete methanol oxidation and promoting charge separation via photoformed Cu⁰. DFT and XPS analyses supported the stable electronic state of Cu and its strong interaction with TiO₂, which were detailed in Figure 5.

The study from Plascencia-Hernández et al. employed P25-type TiO₂ modified with Cu₂O/CuO (Cu_xO)^[126]. Firstly, Cu_xO polyhedral particles were synthesized at room temperature via chemical reduction with PVP and L-ascorbic acid, and then, Cu_xO and P25 were mixed in an ethanolic solution. The introduction of Cu_xO enabled the formation of a p-n heterojunction with TiO₂, enhancing charge separation. Notably, under light irradiation, in situ self-reduction led to the generation of metallic Cu⁰, highlighting a dynamic and adaptive catalytic system. The Cu₂O/CuO-modified TiO₂ catalyst exhibited absorption in both UV and visible regions (up to ~650 nm), with enhanced activity under 470 nm excitation. Using a methanol-water mixture (1:10) at 1 g·L^-1 catalyst concentration, the study showed that Cu oxides undergo self-reduction to Cu⁰ during photoreforming, forming a Schottky barrier that improves charge separation. Color changes in the solution also reflected the cyclic redox of copper species. The best catalysts (0.05% and 0.1% Cu_xO) achieved H₂ production rates up to 2.86 mmol·g^-1·h^-1, about eight times higher than pure TiO₂, alongside CO₂ production, indicating complete methanol oxidation. The Cu₂O/CuO-TiO₂ p-n junction and in situ Cu⁰ formation both contribute to enhanced selectivity and stability, with performance maintained over multiple cycles.

A recent report showed an alternative approach to combine copper with TiO₂, using a copper-based metal-organic framework (MOF), which offered additional advantages due to their high specific surface area, tuneable porous structure, and structural stability^[127]. Composite materials based on P25 TiO₂ and copper-benzene-1,3,5 tricarboxylate (HKUST-1) were synthesized via a simple physical mixing method in methanol overnight. Right after, water was added to reach 25 vol% of methanol and photocatalytic experiments for hydrogen were conducted. Similarly to the previous report from Plascencia-Hernández et al.^[126] small Cu⁰/Cu⁺ nanoclusters (~1.6 nm) were formed in situ, without compromising the MOF structure^[127]. The composite extended light absorption into the visible region through Cu²⁺-induced ligand-to-metal charge transfer (LMCT) processes, enabling effective excitation under UV (λ = 380 nm) and visible light (λ = 550 nm). Under these conditions, the HKUST-1/TiO₂ (1:20) system reached H₂ evolution rates of 5.11 mmol·g^-1·h^-1 in the first run, increasing to 13.24 mmol·g^-1·h^-1 after six cycles, surpassing both pure TiO₂ and CuO-TiO₂, and eventually outperforming Pt-loaded TiO₂. The enhancement is attributed to progressive reduction of Cu²⁺ to Cu⁰/Cu⁺ nanoclusters, which act as stable co-catalysts by promoting electron transfer and suppressing charge recombination. Stability tests (XRD, XPS, FTIR, EPR) confirmed the structural integrity and reversible Cu redox cycling without significant copper leaching.

Taking methanol as model alcohol, the mechanistic understanding of alcohol photoreforming can be extended to other alcohols with longer carbon chains. Moreover, photoreforming of diols and triols that could yield to value oxidation products and are derived from renewable sources, being therefore of great interest for sustainable low carbon hydrogen production. In the following sections, recent studies on photoreforming of C2+ alcohols are reviewed.

As previous discussed, the photoreforming proceeds through pre-adsorption of the target alcohol on the photocatalyst surface, either at metal-oxygen bonds or O_v, leading to the formation of alkoxy intermediates. These species are subsequently oxidized by photogenerated holes, generating alkoxy radicals that undergo α-H abstraction. The resulting aldehydes can either desorb as products or remain adsorbed, undergoing further oxidation to acids or even complete mineralization to CO₂^[73,128,129]. In parallel, the release of protons is coupled to their reduction by photogenerated electrons at the metal co-catalyst, driving hydrogen evolution. For ethanol, for example, Coronado et al. have shown that the alcohol is adsorbed on the TiO₂ surface by monodentate or bridged modes (Eqs. 6 and 7) to yield ethoxide groups^[130].

(6) $$ \begin{equation} \begin{aligned} \mathrm{CH}_{3} \mathrm{CH}_{2} \mathrm{OH}+\mathrm{Ti}-\mathrm{OH} \rightarrow \mathrm{Ti}^{4+}-\mathrm{OCH}_{2} \mathrm{CH}_{3}+\mathrm{H}_{2} \mathrm{O} \text { (monodentate) } \end{aligned} \end{equation} $$

(7) $$ \begin{equation} \begin{aligned} \mathrm{CH}_{3} \mathrm{CH}_{2} \mathrm{OH}+(\mathrm{Ti})_{2}-\mathrm{OH} \rightarrow(\mathrm{Ti})_{2}-\mathrm{OCH}_{2} \mathrm{CH}_{3}+\mathrm{H}_{2} \mathrm{O} \text { (bridged)} \end{aligned} \end{equation} $$

While this mechanism is broadly similar for different alcohols, the nature of the substrate strongly influences the reaction pathway and product distribution. For instance, the replacement of methanol by ethanol introduces C-C bond cleavage and additional α-hydrogens, leading to products such as acetaldehyde, acetic acid, and CO₂^[74]. Secondary alcohols, such as isopropanol, tend to undergo dehydrogenation more readily, with acetone as the main product, accompanied by small amounts of CO₂, formic acid, or acetic acid from over-oxidation. In some cases, dehydration by-products like propylene can also appear^[73,74]. Thus, compared to methanol, higher alcohols not only expand the spectrum of possible oxidation products but also reveal the complexity of competing pathways that influence the overall efficiency of hydrogen generation. Moreover, the balance between these transformations can be significantly affected by photocatalyst modifications, such as metal loading, defect engineering, or heterojunction design, which alter charge separation dynamics and surface reactivity.

Zhang and coauthors reported that induced defects in TiO₂ can control product selectivity of ethanol photoreforming^[131]. The defects were chemically formed into bare P25 TiO₂ using NaBH₄. Enhanced photoactivity was observed as the “defected” TiO₂ exhibited improved light absorption, charge separation, and better product selectivity, resulting in both higher hydrogen purity and a better liquid-to-gaseous carbon ratio. O_v were created in the TiO₂ lattice, forming Ti³⁺ sites, which were detected by EPR spectroscopy, with the signal increasing with increasing NaBH₄ amounts. The dominant reaction pathway was determined through active species trapping experiments, which showed that the preferred ethanol oxidation pathway was related to direct hole transfer, indicating that selectivity relies on surface chemisorption. In this case, surface defects decreased the acetaldehyde adsorption energy, promoting its rapid desorption and suppressing overoxidation into CO₂, thereby improving selectivity towards liquid hydrocarbon products. As represented in Figure 6, the oxidation mechanism involves C-H activation as the initial step of ethanol photoreforming on defected TiO₂, with the abstraction of an α-H from the ethanol molecule and the formation of a 1-hydroxyethyl radical. Then, acetaldehyde was formed as the 1-hydroxyethyl radical underwent further oxidation by photogenerated holes. In this case, the so-called current doubling effect described for methanol reforming was not investigated. Liquid product production reached 0.08 mmol/h of liquid acetaldehyde (from 10 v/v % ethanol), and the total organic production (acetaldehyde and acetic acid) was 0.47 mmol in 6 h compared to 0.14 mmol for the pristine P25^[131]. In relation to the H₂ production, an optimal rate of 0.08 mmol/h, with purity greater than 99%, much higher than the 93.4% purity from bare P25 TiO₂, was achieved.

Ethanol photoreforming was also evaluated using hierarchical Au/TiO₂ nanoflower (TNF) photocatalysts under UV irradiation^[132]. The effect of different calcination treatments on the physicochemical properties of the material were also evaluated, to benchmark their performance against selected reference photocatalysts. The Au/TNF-600-1 (600 °C, 1 h) sample exhibited the highest hydrogen production rate with 10 vol.% ethanol (23.8 mmol g^-1h^-1). This performance was superior to Au/P25 TiO₂ and other Au/anatase reference photocatalysts. The hydrogen production rates increased with calcination temperature up to 600 °C but then decreased sharply at higher temperatures, reflecting the interplay among surface area, crystallite size, and polymorphic composition. The Au/TNF-600-1 photocatalyst also demonstrated excellent stability, with no loss in activity over five successive 3-h test cycles. Additionally, Piedra-Lopez and coauthors have shown that smaller and more uniformly distributed Au nanoparticles can yield higher performance on H₂ production^[65]. Their study compared the effects of two reduction methods, thermal reduction (TR) and photocatalytic reduction (PR), on Au/TiO₂ (P25) photocatalysts prepared via deposition-precipitation (DP) with urea. The reduction route was found to critically influence nanoparticle size and distribution. The photocatalytically reduced sample achieved superior properties, with 94% of Au nanoparticles smaller than 4 nm, compared to 77% for the thermally reduced sample. The smaller particle size resulted in higher photocurrent and significantly enhanced hydrogen production (in 50% v/v ethanol). Moreover, Luo et al. reported how site-specific deposition of Au nanoparticles on TiO₂-Cu₂O photocatalysts influences ethanol photoreforming^[133]. Au nanoparticles (~2.5 nm, 0.85 wt%) were selectively anchored on either TiO₂ nanorods or Cu₂O nanocubes, or both, revealing distinct mechanistic behaviors. The catalyst with Au deposited on TiO₂ (Au@TiO₂/Cu₂O) achieved the highest H₂ production rate (8.5 mmol g^-1 h^-1) under simulated solar light, significantly outperforming other configurations. This enhanced activity was attributed to the synergistic effect between the Au-TiO₂ interface, where Au adjacent to Ti³⁺ defects and O_v promote proton reduction, while the p-n junction between TiO₂ and Cu₂O improves charge separation and hole transfer for ethanol dehydrogenation. As a result, acetaldehyde was produced at a nearly stoichiometric rate in relation to molecular H₂, indicating a highly selective process that suppresses C-C bond cleavage and byproduct formation (CH₄, CO₂).

Esteves et al. conducted a comprehensive investigation of TiO₂-reduced graphene oxide (rGO)-Pt nanocomposites for photocatalytic hydrogen production from ethanol in both liquid and gas phases^[134]. The catalysts were synthesized via a two-step procedure where TiO₂-rGO nanocomposites were first prepared using a hydrothermal method at 125 °C. Subsequently, Pt decoration was achieved through photodeposition using a 450 W mercury-vapor lamp under N₂ purging. The resulting nanocomposites had Pt loadings of 1.5%, 2.5%, and 3.8%, with rGO content optimized at 3 wt%. The TiO₂-rGO3%-Pt3.8% composite achieved the highest initial hydrogen production rate of 560 mmol h^-1g^-1 with > 95% H₂ selectivity. Gas-phase measurements confirmed a consistent H₂/CO_x molar ratio of approximately 3, indicating near-complete selectivity with minimal byproducts, including CH₄, CO, CO₂, C₂H₆, and C₂H₄^[134]. Platinum loading strongly influenced activity, with initial hydrogen production rates (slope 1) of 361, 356, and 567 mmol h^-1 g^-1 for Pt loadings of 1.5%, 2.5%, and 3.8%, respectively, followed by significantly lower rates (second slope) of 24, 34, and 66 mmol h^-1 g^-1, indicating a change in reaction regime over time. Stability tests in the liquid phase revealed a pronounced loss of activity upon cycling, attributed to platinum poisoning by adsorbed intermediates, notably acetaldehyde, and to nanoparticle agglomeration. In contrast, gas-phase experiments showed a much lower activity loss (ca. 8%), particularly for the TiO₂-rGO-Pt system, highlighting the role of rGO in mitigating deactivation^[134]. A rapid decrease in pH (from 7 to 3.5) was observed during liquid-phase reactions prior to stabilization, and this decline correlated with a decrease in the hydrogen production rate. Mechanistic analyses indicated a strong synergistic effect between rGO and Pt:rGO acts as an electron acceptor, suppressing charge recombination, while Pt significantly enhances hydrogen evolution activity. Voltametric studies further evidenced progressive catalyst poisoning, with oxidation peaks at 0.68 and 1.06 V vs. Ag/AgCl that gradually diminished over repeated cycles, supporting the role of reaction intermediates, particularly acetaldehyde, in activity loss. The dual-phase operation demonstrates that these nanocomposites are active in both liquid and gas phases, offering flexibility for hydrogen production processes. Although high hydrogen selectivity and the possibility of catalyst regeneration after treatment were observed, significant activity loss upon reuse and the requirement for relatively high Pt loadings (3.8%) may limit large-scale application^[134]. Additional challenges include the need for UV irradiation, accumulation of intermediates, pH variations, and stability issues under continuous operation. Therefore, the development of flow reactor systems enabling the continuous removal of oxidation products may improve process stability and scalability.

TiO₂ can also be modified with non-noble and earth-abundant materials to enhance its photocatalytic performance for ethanol photoreforming. In this context, the p-type semiconductor NiO was employed as a co-catalyst to form NiO-TiO₂ heterojunctions synthesized via the sol-gel process^[71]. The incorporation of NiO significantly improved hydrogen generation efficiency, doubling the H₂ production rate compared to pure TiO₂ and maintaining long-term stability. This enhancement arises from the formation of a p-n junction between NiO and TiO₂, which facilitates charge separation by directing photogenerated electrons to the conduction band of TiO₂ and holes to the valence band of NiO, thereby minimizing recombination. In situ DRIFTS analyses provided valuable mechanistic insights into ethanol adsorption and reaction pathways^[71]. On both catalysts, ethanol adsorbed in molecular and dissociative forms, but the proportion of surface ethoxy species (CH₃CH₂OTi) was higher on NiO-TiO₂. Upon illumination, pure TiO₂ underwent a multistep oxidation via acetaldehyde and acetic acid intermediates, resulting in greater aldehyde accumulation and partial deactivation. In contrast, NiO-TiO₂ favored direct dehydrogenation of ethanol through CH₂CHO-type intermediates, accompanied by higher H₂ evolution (20 mmol g^-1 h^-1) and increased oxidation reaction rates without surface poisoning by primary oxidation products.

Shahpal et al. evaluated the H₂ evolution during aqueous-phase photo-oxidation of isopropanol (IPA) on Pt-decorated g-C₃N₄/TiO₂ hybrid photocatalysts^[135]. According to the hybrid band structure, the photo-generated electrons migrate from g-C₃N₄ to TiO₂, while the photogenerated holes migrate from TiO₂ to g-C₃N₄, reducing the likelihood of recombination. Furthermore, photodeposition of Pt nanoparticles localized the photogenerated electrons at the metal nanoparticles. In the proposed mechanism, IPA adsorbs on the surface of g-C₃N₄ or TiO₂, where it is oxidized to acetone upon reacting with photo-generated holes, simultaneously forming H⁺ ions. In a parallel reaction, the adsorbed water molecules react with the photo-generated holes, producing additional H⁺ ions along with OH^-. The hydronium ions then combine with the electrons accumulated on the Pt nanoparticles to form adsorbed H^•, leading to evolved H₂ gas.

Interestingly, Šalipur et al. illustrated the deactivation mechanisms of Pt-decorated g-C₃N₄/TiO₂ photocatalysts for hydrogen production using IPA^[136]. Under solar irradiation, the photocatalyst exhibited high initial activity (2.3 mmol g^-1·h^-1) but gradually deactivated to ~1.4 mmol g^-1·h^-1 due to the formation of inhibitory intermediates, such as propionic acid and pinacol, while Ti³⁺ surface defects were partially preserved^[136]. Under visible light, activity was lower (1.1 mmol g^-1·h^-1) but stable, with complete oxidation to Ti⁴⁺ and absence of critical intermediates, highlighting a trade-off between initial activity and durability. Cross-deactivation tests confirmed that solar-light-generated intermediates caused H₂ inhibition. The study revealed the dual role of O_v, the importance of TiO₂-carbon-Pt charge transport, and the kinetics of intermediate formation vs. decomposition. These findings provide guidelines for spectral optimization, defect control, and prevention of inhibitory products, supporting the design of more efficient and durable photocatalysts.

Local structural features on the photocatalytic oxidation of IPA to acetone were examined using a systematic series of titania materials anchored on mesoporous silica (SBA-15)^[60]. Titanium surface loading with monomeric and oligomeric Ti⁴⁺ species was prepared by grafting Ti⁴⁺ species onto SBA-15, with surface densities ranging from isolated low-loaded sites (0.02-0.35 Ti nm^-2) to higher loadings (up to 2 Ti nm^-2). The results showed that supported Ti⁴⁺ species exhibit superior selectivity compared to P25, particularly at low surface loadings where isolated tetrahedral TiO₄ sites are present. These single-site catalysts limit the availability of charge carriers, preventing overoxidation to acetate, whereas P25 suffers from active site blocking due to acetate formation. Photocatalytic performance normalized to Ti content indicated that supported catalysts achieved comparable or superior activity per Ti atom. Additionally, band gap measurements indicated that quantum confinement effects in low-loaded catalysts influence charge carrier dynamics and reactivity. Structural analysis also revealed that increasing Ti loading promotes oligomeric Ti⁴⁺ species formation, which correlates with slightly reduced selectivity. Moreover, the presence of isolated Ti⁴⁺ sites restricted sequential oxidation steps, while the silica support provided additional adsorption sites that prevented active-site deactivation. In-situ DRIFTS confirmed that low-loaded catalysts maintain surface integrity and allow efficient acetone desorption. In summary, the study established clear structure-activity relationships: isolated tetrahedral Ti⁴⁺ sites provide the highest selectivity, whereas increasing Ti content favors oligomer formation, which triggers acetate formation and losses in photocatalytic activity.

Ethylene glycol photoreforming was recently reported by Roebuck et al., with particular emphasis on how the crystalline phase of titanium dioxide affects the photo-oxidation mechanism^[137]. This substrate was selected because of its prevalence in bioderived compounds and its potential relevance as a waste or pollutant material. Its adsorption behavior and hole transfer mechanisms were analyzed across different TiO₂ crystalline phases, including anatase, rutile, and P25. Among the studied samples, Pt/anatase and Pt/P25 photocatalysts exhibited similar hydrogen production activities, quantum efficiencies of 15.9% and 11.7%, respectively. In contrast, Pt/rutile showed the lowest performance with a quantum efficiency of only 4.3%. Over time, the hydrogen production rate for all catalysts slightly decreased, while CO₂ evolution increased. The molar ratio of H₂ to CO₂ for Pt/P25 was approximately 2.5 after 4 h of irradiation, agreeing with the stoichiometric expectation for ethylene glycol photooxidation. Pt/anatase and Pt/rutile, however, displayed higher H₂ to CO₂ molar ratios of 3.7 and 3.1, respectively, suggesting additional H₂ production from partial water oxidation for Pt/anatase and limited CO₂ generation for Pt/rutile. With respect to oxidation pathways, Pt/anatase and Pt/P25 primarily oxidized ethylene glycol to glycolaldehyde, following an indirect oxidation pathway via hydroxyl radicals, leading to full mineralization, whereas Pt/rutile favored direct C-C bond cleavage to formaldehyde, which failed to undergo further conversion to formic acid and thereby limited hydrogen evolution. The inability of Pt/rutile to effectively oxidize formaldehyde was identified as a key factor for its lower hydrogen output. Overall, an indirect hydroxyl radical-driven mechanism predominated on anatase-containing catalysts, while the direct hole transfer mechanism governed on rutile. Therefore, the choice of TiO₂ polymorph is a critical strategy for enhancing hydrogen production, as it governs the oxidation mechanism. Although P25 exhibited lower overall H₂ production than pure anatase, it showed a more efficient conversion of ethylene glycol per unit surface area, indicating that the mixed-phase advantage may lie in its additive ability to convert both ethylene glycol and its intermediate species. This dual functionality of mixed-phase TiO₂ helps to avoid the accumulation of specific intermediates and consequent surface poisoning.

Some recent works have considered the photoreforming of alcohols with longer and more complex chains. The influence of butanol isomer on photothermal hydrogen production using Ti@TiO₂ core-shell photocatalysts was studied by El Hakim et al.^[138] Structural differences among 1-butanol (1-BuOH), 2-butanol (2-BuOH), and tert-butanol (t-BuOH) were evaluated with respect to hydrogen evolution kinetics, surface adsorption, and reaction mechanisms. A clear performance hierarchy for hydrogen production was observed: 1-BuOH significantly outperformed 2-BuOH, which in turn exceeded t-BuOH across all tested temperatures (up to 69 °C). This trend was attributed to stronger adsorption of primary alcohols on the TiO₂ surface, facilitating more effective interaction with photogenerated holes. Photothermal effects were pronounced, with reaction rates increasing with temperature under illumination; however, no hydrogen formation occurred in dark conditions, confirming the photonic origin of the reaction.

Product analysis showed that 1-BuOH and 2-BuOH produced H2 exclusively as a reduction product, whereas t-BuOH generated a mixture of H₂, CH₄, and C₄H₆, indicating a C-C bond scission in tertiary alcohols^[138]. Activation energies for 1-BuOH and 2-BuOH were similar (20-21 kJ·mol^-1), comparable to glycerol (25 ± 5 kJ·mol^-1), while t-BuOH exhibited a lower activation energy of 13 kJ·mol^-1, reflecting a different rate-limiting mechanism. Mechanistically, primary and secondary alcohols followed a photothermal pathway involving photogeneration of electron-hole pairs in TiO₂, thermal activation of shallowly trapped holes, transfer to highly reactive free holes at the surface, and subsequent hole-mediated O-H bond cleavage leading to hydrogen formation. In contrast, t-BuOH displayed a distinct mechanism characterized by lower activation energy, weaker surface adsorption, and C-C bond scission, producing multiple gaseous products. Therefore, for hydrogen production, primary alcohols were preferred due to their higher yields and exclusive H₂ formation.

Courtois and coauthors investigated the photochemical transformations of isobutanol on rutile TiO₂(110), as a model system to understand temperature-dependent photocatalytic processes of biomass-derived chemicals^[66]. A strong temperature dependence in the reaction selectivity was observed and would arise from the competition between thermal desorption of initial photoproducts from the surface and secondary photochemical reactions of surface-bound intermediates. They revealed that isobutanol desorbs from r-TiO₂(110) with coverage-dependent peaks between 300-350 K, with only about 2% of the adsorbed molecules undergoing thermal reactions to form isobutoxy species (surface-bound) and bridge-bonded hydroxyl groups, while at higher temperatures (~600 K) isobutoxy undergoes disproportionation to yield isobutanol and isobutanal, or dehydration to produce isobutene and water. Photochemical selectivity was found to be strongly temperature-dependent: at 300 K, the dominant pathway was selective aldehyde formation, where isobutoxy converted to isobutanal that rapidly desorbed into the gas phase, preventing further reactions and resulting in clean and selective aldehyde production. In contrast, at 240 K, the extended residence time of isobutanal (~420 s) enabled secondary photo-oxidation, leading to C-C bond cleavage with formation of propane and formyl species, which subsequently reacted with lattice oxygen to produce formate that decomposed to CO upon heating to 550 K.

Mechanistic analysis evidence that isobutoxy species are the key photoactive intermediates, supported by the complete suppression of disproportionation after UV exposure, and that oxidized TiO₂(110) surfaces enhanced alkoxy formation and photo-oxidation efficiency compared to reduced surfaces, with hydroxylated surfaces exhibiting intermediate behavior^[66]. The primary photochemical pathway involved isobutanol conversion to isobutoxy with release of protons and electrons, followed by photo-oxidation of isobutoxy to isobutanal, while at low temperatures secondary photo-oxidation occurred, in which isobutanal photochemically split into propyl and formyl radicals, the former recombining with surface hydrogen to yield propane and the latter reacting with lattice oxygen to form formate that decomposed into CO. Quantitative analysis showed that higher surface coverages of isobutanol increase photochemical efficiency. A significant fraction of surface isobutoxy was converted under UV illumination, and the thermal desorption processes exhibited Arrhenius-type temperature dependence.

The same group also investigated the photocatalytic conversion of tertiary alcohols on rutile TiO₂(110) surfaces under highly defined vacuum conditions^[139]. The study shows that tertiary alcohols, typically regarded as inert toward oxidation, undergo diverse reaction pathways under photocatalytic conditions, particularly because of the absence of an α-hydrogen, which normally facilitates C-H bond cleavage in primary and secondary alcohols. Moreover, the addition of co-catalysts, specifically platinum, influences the reaction rates and the emergence of new reaction channels, including the formation of molecular hydrogen and long-chain alkanes. The experiments were conducted under UHV conditions to ensure a highly controlled environment and to minimize interference from oxygen and water.

The tested photocatalyst was a rutile TiO₂(110) single crystal, and the studied tertiary alcohols were 3-methyl-3-hexanol, 2-methyl-2-pentanol, and 2-methyl-2-butanol^[139]. Platinum clusters were deposited on the TiO₂(110) crystal at well-defined coverages, ranging from 0.1% of a monolayer up to Pt₂₅ clusters, in order to assess their co-catalytic effects. Under UV illumination, contrary to typical oxidation pathways observed for primary and secondary alcohols, tertiary alcohols underwent a photocatalytic disproportionation reaction, yielding an alkane and the corresponding ketone. For instance, as represented in Figure 7, 3-methyl-3-hexanol produced 2-pentanone and ethane, as well as 2-butanone and propane, as well as 2-butanone and propane. Instead of the common C-H bond cleavage, the reaction proceeded via C-C bond cleavage; however, bonds to methyl groups were not cleaved. Instead, the longer alkyl chains in the α-position to the hydroxyl group were abstracted. This process exhibited 100% selectivity for the abstraction of the longer carbon chain in tertiary alcohols with two methyl groups at the α-C position, such as 2-methyl-2-butanol and 2-methyl-2-pentanol, which yielded acetone and the respective alkane exclusively. The introduction of platinum loadings significantly increased the overall reaction rate and also opened a new reaction channel, involving the formation of H₂ and a long-chain alkane, resulting from the recombination of two alkyl moieties. In the case of 2-methyl-2-pentanol on Pt-loaded TiO₂, hexane was detected (from propyl radical recombination), along with H₂, which were not observed on bare TiO₂.

The study confirmed that the reaction is truly catalytic under illumination, with no evidence of catalyst poisoning by unwanted surface species^[139]. Selectivity patterns, such as the pentanone-to-butanone ratio of about 2:1 for 3-methyl-3-hexanol, remained largely unaffected by variations in Pt coverage or temperature in the range of 230-360 K. The observed preference for ethyl over propyl cleavage, along with the consistent absence of methyl cleavage, is in agreement with thermochemical principles, as methyl radical formation requires significantly higher energy. The proposed reaction mechanism involves photoactive alkoxy species generated upon surface adsorption undergoing a hole-mediated oxidation process, leading to homolytic C-C bond scission, with longer alkyl chains such as ethyl and propyl interacting more strongly with the TiO₂ surface and remaining adsorbed, subsequently recombining in a consecutive thermal reaction step with hydrogen atoms derived from dissociative alcohol adsorption. In summary, the study demonstrated novel and unexpected photocatalytic reactions of tertiary alcohols on rutile TiO₂(110), characterized by disproportionation into an alkane and a ketone via C-C bond cleavage [Figure 8].

Glycerol is widely used as a sacrificial agent in photocatalytic reforming due to its unique structural and chemical properties^[140-142]. As a triol, glycerol contains three hydroxyl groups, which makes it highly reactive and easily oxidizable under photocatalytic conditions. Its low redox potential facilitates electron transfer to the photocatalyst, enhancing charge separation and promoting hydrogen evolution. Moreover, as it shares chemical features with polyols and sugars present in lignocellulosic or agricultural residues, glycerol also serves as a model substrate for biomass photoreforming. Additionally, it is a byproduct of biodiesel production, making it abundant, inexpensive, and renewable, which increases its appeal for sustainable energy applications^[143-147]. Compared to other alcohols, glycerol often leads to higher hydrogen production rates and the formation of valuable intermediates such as dihydroxyacetone (DHA), formic acid, and glyceraldehyde (GA), providing opportunities for combined energy and chemical valorization^[148]. These characteristics make glycerol a model substrate for investigating photocatalytic hydrogen generation and designing efficient photocatalyst systems. Selected results on photoreforming of glycerol using different TiO₂-based photocatalysts are summarized in Table 1, while key aspects of the process and materials development are discussed in the following paragraphs.

In the context of photocatalytic applications using TiO₂, the kinetics and mechanistic pathways of glycerol transformation can be influenced by diverse factors, as reported by Panagiotopoulou and coauthors^[174]. Under photo-oxidation conditions, TiO₂ (P25) promotes the complete oxidation of glycerol to CO₂, with reaction rates increasing considerably upon the addition of Pt. Under photoreforming conditions (in the absence of O₂), TiO₂ alone exhibits very low activity. In contrast, when Pt (0.5 wt.%) is added as a cocatalyst, H₂ and CO₂ production rates increased by about 25 and 60 times, respectively. Analysis of liquid-phase products revealed a series of common intermediates formed during both oxidation and reforming reactions, including acetol, acetaldehyde, ethanol, methanol, GA, glycoaldehyde, acetone, and acrolein. Their formation, first increasing and then decreasing with irradiation time, indicates sequential oxidation and reforming steps leading ultimately to CO₂. In the presence of oxygen, adsorbed intermediates were more rapidly oxidised, resulting in a cleaner surface compared with the oxygen-free conditions of photo-reforming, in which persistent surface residues were observed. In general, the reaction mechanism involves two main initial routes: hydrogenolysis of glycerol into propylene glycol and dehydrogenation into GA, followed by decarbonylation and dehydration steps yielding oxygenated species such as acetaldehyde, ethanol, and acetone (see scheme in Figure 9). In both oxidation and reforming conditions, these intermediates are eventually transformed into CO₂, where in the latter, protons from water are reduced to generate H₂. Consequently, both processes share the same overall pathway, differing mainly in the terminal electron acceptor and the presence of oxygen.

Wahab and Idriss also investigated the photocatalytic reforming and oxidation pathways of glycerol using anatase TiO₂ modified with silver (0.1 at.%) and palladium (0.3 at.%)^[14]. Photocatalytic tests (100 W, 360 nm filter) were conducted varying oxygen partial pressure (0.002-0.96 atm), glycerol concentration (0.002-5 vol.%), and photocatalyst mass. It was observed that hydrogen production rates remained nearly constant up to approximately 0.2 atm of O₂; beyond this threshold, oxygen began to dissolve and interfere with the reaction, marking a transition between the regimes of photoreforming and photo-oxidation. Moreover, H₂ production exhibited insensitivity to glycerol concentrations above ~0.05 vol%, suggesting a zero-order kinetic regime associated with full surface coverage. In this case, the rate-determining step is likely a surface transformation (e.g., H_ads recombination or charge transfer) rather than reactant adsorption, in agreement with the Langmuir-Hinshelwood mechanism. Analysis of dissolved CO₂ revealed that it represented about 15%-20% of the CO₂ detected in the gas phase, a ratio that remained consistent across different glycerol concentrations, indicating that gas-phase measurements alone underestimate the true reaction extent. Regarding liquid-phase products, their distribution depended strongly on the initial glycerol concentration. At low concentrations (e.g., 0.005 vol.% ≈ 1.34 × 10^-5 M), formaldehyde was the main intermediate detected, whereas at higher concentrations (e.g., 5 vol% ≈ 1.34 × 10^-2 M), hydroxyacetone (glycerone) became predominant; ethylene glycol was detected only in trace amounts. The study demonstrated that combining Ag and Pd on anatase TiO₂ substantially enhanced proton-reduction activity, thus promoting hydrogen generation in aqueous media while selectively steering the oxidation pathways of glycerol. Overall, the authors concluded that the predominance between photoreforming and photooxidation shifts around 0.2 atm O₂, with hydrogen production being inhibited at higher oxygen pressures. Furthermore, H₂ generation remained unaffected by glycerol concentrations above 0.05 vol%, while liquid-phase analysis revealed that hydroxyacetone dominated at high concentrations and formaldehyde at low concentrations. Further oxidation of the latter to formate contributes to reaction inhibition.

Additionally, Hu and coworkers investigated how different crystalline phases of TiO₂ (anatase and rutile) affect the generation of ROS and the selective conversion of glycerol into formic acid^[175]. In this case, rutile favors ROS formation via the sequential pathway O₂ → O₂•^- → H₂O₂ → •OH, facilitated by its low oxygen vacancy formation energy (0.96 vs. 4.49 eV for anatase). Heterojunctions between anatase and rutile further lower this energy to -0.77 eV, thereby enhancing charge separation. The TiO₂ sample containing 74% anatase achieved the highest glycerol photoreforming performance with 66% conversion and 42% selectivity toward formic acid. Key intermediates such as GA and glycolaldehyde were identified. Moreover, excess ^•OH causes over-oxidation to CO₂, but adjusting the solution pH to 11 could suppresses this, increasing selectivity to 59%. The main pathway under neutral conditions was glycerol → GA → glycolaldehyde → formic acid, while excess ^•OH drives undesired CO₂ formation. Further report by Pecoraro et al.^[151] on glycerol photoreforming using the TiO₂ polymorphs (anatase, brookite, and rutile) combined with Pt reveals that H₂ generation arises from both glycerol dehydrogenation and, predominantly, from water dissociation. The observed superior performance of brookite was attributed to two distinctive surface properties. First, Fourier-transform infrared (FT-IR) spectroscopy revealed a higher hydrophilicity, leading to an enhanced ability to adsorb water molecules. Second, the distribution and nature of platinum sites were more favorable, with a predominance of Pt⁰ species located at edges and steps, which are known to be more catalytically active. Consequently, the following trend in hydrogen evolution efficiency was Pt-brookite > Pt-P25 ≈ Pt-anatase > Pt-rutile. Under UV irradiation, the Pt-brookite catalyst achieved an H₂ yield 3.1 times higher than that of the reference Pt-P25. These results, further supported by the higher H₂/CO₂ ratio observed for brookite, highlight that the combination of enhanced hydrophilicity and an optimized distribution of metallic platinum active sites is crucial to maximize photocatalytic efficiency in glycerol photoreforming.

In this regard, Maslova et al. demonstrated the importance of structural control over both the support and the metallic phase to maximize glycerol photoreforming using platinum-supported TiO₂ catalysts^[150]. TiO₂ support was prepared via a microemulsion route, enabling controlled synthesis of nanoparticles with high uniformity, stability, and specific surface area. This process yielded a material predominantly in the anatase phase, with a small fraction of rutile, and exhibiting a large surface area favorable for metal dispersion. To optimize the anchoring sites, the TiO₂ support underwent a dehydroxylation treatment under dynamic vacuum at various temperatures, with 500 °C selected as the optimal temperature. Platinum was then introduced using Pt(COD)Me₂ (COD: 1,5-cyclooctadiene, Me: -CH₃) as a precursor, via a surface organometallic chemistry (SOMC) approach for precise control over the formation and dispersion of metallic nanoparticles. Highly dispersed and ultrasmall platinum nanoparticles (≈1 nm) were obtained after reduction under H₂ atmosphere at 300 °C (Pt-OM@TiO₂-m-500). For comparison, photocatalysts were also prepared through conventional techniques, such as IWI and DP, using the same metal precursor. Different characterizations confirmed that the SOMC-prepared catalysts exhibited significantly higher platinum dispersion and smaller nanoparticles on the TiO₂ surface. Photocatalytic tests were performed in a reactor irradiated with simulated sunlight (100 mW·cm^-2) under a nitrogen atmosphere, using an aqueous 1 mol·L^-1 glycerol solution and 0.5 g·L^-1 of catalyst. The results showed that the SOMC-prepared catalyst exhibited substantially higher activity than that of catalysts prepared by conventional methods. Moreover, enhanced selectivity toward GA, compared to glycolaldehyde and other liquid products, was observed. This high selectivity was attributed to the well-defined uniformly distributed active sites resulting from the fine control of metal dispersion. Specifically, the Pt/TiO₂-mSOMC catalyst achieved a hydrogen production rate of 4.9 mmol·g^-1·h^-1, outperforming Pt/TiO₂-mDP (3.7 mmol·g^-1·h^-1) and Pt/TiO₂-mIWI (3.1 mmol·g^-1·h^-1).

Escamilla-Mejía et al. presented a study focused on the preferential incorporation of platinum in TiO₂-carbon composites^[154]. The work highlights how the selective localization of Pt within specific regions of the TiO₂/carbon matrix can positively influence glycerol photoreforming. For the studies, a commercial TiO₂ P25 and a carbonaceous support (MSH) derived from olive pit biochar were used, where the TiO₂-MCH composite was prepared via the sol-gel method, followed by photodeposition of platinum and a final calcination step. The carbonaceous supports enhanced intermediate adsorption, although excessive adsorption could potentially hinder light absorption and electron transfer if intermediates block TiO₂ active sites. The results demonstrated that the composite exhibited a higher H₂/CO₂ ratio during glycerol photoreforming, indicating improved overall system efficiency and greater selectivity toward hydrogen generation compared to other catalysts tested in the study. This improvement was attributed to the strategic placement of Pt in regions that facilitate proton reduction, thereby minimizing charge recombination and preventing excessive oxidation of the substrate. The authors emphasized that the synergistic interaction of TiO₂, the carbonaceous support, and Pt contributes to enhanced catalytic stability over multiple reaction cycles, maintaining consistent performance and preventing significant degradation of the active material. Overall, the study underscores the importance of targeted synthetic strategies that account for factors such as selective metal incorporation, functional support design, and light absorption dynamics to optimize photocatalytic efficiency.

Zhong et al. presented a multifunctional approach based on Au/TiO₂@n-octadecane microcapsules with an organic core and a photothermal shell^[156]. The study reports a multifunctional Au/TiO₂ (AT) encapsulated in n-octadecane (a phase-change material, PCM), designed for the photothermal reforming of glycerol. The microcapsules were prepared via a hydrothermal route, yielding rectangular particles (70 nm), where gold nanoparticles were deposited on TiO₂ nanosheets and embedded in a the PCM matrix. These microcapsules acted as integrated solar energy harvesting systems, absorbing across a broad spectral range including the infrared region, serving simultaneously as thermal storage media and photocatalytic supports. Under simulated solar irradiation (Xe lamp, 300 W; 200-2,500 nm), the photothermal effect was quantified by monitoring a temperature increase in the glycerol suspension. The Au/TiO₂@PCM system significantly outperformed conventional systems without PCM, where the internal thermal storage maintained elevated reaction temperatures even under fluctuating irradiance, sustaining a high hydrogen generation rate. Specifically, the microcapsules resulted in a H₂ production rate of 5.4 mmol g^-1·h^-1, compared to 3.8 mmol g^-1·h^-1 for Au/TiO₂ nanoparticles without PCM. The enhanced performance of the encapsulated photocatalyst was also attributed to its superior dispersion stability and the prevention of particle aggregation afforded by encapsulation. However, the study primarily focused on hydrogen production and photothermal conversion efficiency, without explicitly detailing or quantifying the oxidation products or selectivity toward other glycerol-derived intermediates.

Interestingly, Oliveira et al. reported the design of photocatalytic plates containing immobilized TiO₂/Pt, with a comparable performance to that of the powder photocatalyst^[142]. The preparation involved the photodeposition of Pt onto TiO₂ (P25), followed by homogenization with Nafion™ and ethanol and application onto acrylic substrates (5.0 × 1.0 cm) by solvent evaporation, with a final thickness of 150 µm. The optimal mass ratio per plate was fixed at 25 mg of TiO₂-Pt, sufficient to prevent charge recombination without increasing Pt-related costs. The authors evaluated the stability and recyclability of the plates for up to 10 reaction cycles (3 h each), observing that at 0.3 wt.% Pt, the system maintained ~361 mmol H₂·h^-1·m^-2 evolution from glycerol aqueous solutions up to the seventh cycle, while at 0.1 wt.% Pt, a noticeable performance decline occurred after the fourth cycle, likely due to catalyst loss from washing or leaching.

Several studies have explored replacing noble metals such as platinum and gold in TiO₂-based photocatalytic systems for glycerol photoreforming, with copper emerging as a particularly promising and widely studied alternative due to its effectiveness and lower cost^{[141,162-164,166,167]}. Pecoraro et al. presented a simple and cost-effective approach for synthesizing TiO₂ (P25) photocatalysts modified with copper oxides using mechanical milling as the preparation method^[72]. Among the tested samples, the catalyst containing 3 wt.% Cu₂O-TiO₂ exhibited a performance comparable to that of the benchmark TiO₂-Pt system, achieving a glycerol conversion of approximately 33% and a hydrogen production rate of 0.17 mmol·h^-1·g^-1. Notably, the Cu₂O-TiO₂ catalyst showed good selectivity for the formation of high-value compounds such as 1,3- DHA and GA, the latter of which was not detected with the platinum-based catalyst. The enhanced efficiency of the system was attributed to the formation of a p-n heterojunction between Cu₂O (p-type) and TiO₂ (n-type), which enables a direct Z-scheme charge transfer mechanism. Additionally, a detailed investigation into the mechanisms of glycerol photoreforming using physical mixtures of CuO and TiO₂ was reported by Martín-Gómez and coauthors^[165]. Through EPR and cyclic voltammetry (CV), the origin of the improved photocatalytic activity was analyzed, with particular emphasis on the role of copper species. CuO nanoparticles with varying particle sizes were physically combined with TiO₂ P25, and their performance was evaluated. While pure CuO and TiO₂ showed no or limited activity for hydrogen evolution, the CuO:TiO₂ mixtures demonstrated markedly superior performance, achieving up to 88 mmol·g^-1 of H₂ (10 wt.% CuO). The study established that the size of CuO nanoparticles strongly influences the photocatalytic efficiency, likely due to increased surface area and enhanced accessibility of active sites.

Accordingly, the proposed mechanism is based on a redox Cu(II)/Cu⁰ catalytic cycle, where photogenerated electrons migrate from TiO₂ to CuO. The resulting Cu⁰ species act as active sites that facilitate proton reduction^[165]. Subsequently, Cu⁰ is reoxidized back to Cu²⁺, completing the catalytic redox cycle. EPR analyses provided direct evidence for the presence and transformation of paramagnetic Cu²⁺ species during the photocatalytic process, confirming the dynamic operation of the Cu(II)/Cu⁰ cycle. Complementary CV measurements identified the characteristic redox potentials of copper species, consistent with the proposed mechanism.

In a similar study, Umair et al. investigated the pilot-scale photoreforming of glycerol for hydrogen production using Cu₂O-TiO₂ (P25) catalysts^[30]. Conducted in a large-scale solar reactor, the work exemplifies translating laboratory-scale photocatalytic processes into pre-industrial applications. The catalyst was synthesized through a mechanical milling method, where structural analyses confirmed the formation of a p-n heterojunction between Cu₂O and TiO₂. In this configuration, Cu₂O acts as a visible-light antenna due to its narrow band gap (1.8-2.2 eV), and both semiconductors are activated, promoting electron transfer from the Cu₂O conduction band to that of TiO₂, and holes from TiO₂ migrate to the valence band of Cu₂O. The pilot reactor, operated with suspended catalyst and fed with biomass-derived substrates (glycerol, glucose, and ethanol) under simulated solar exposure, demonstrated technical feasibility of scaling up such systems. EPR measurements confirmed the formation of hydroxyl radicals (^•OH), which play a key role in substrate oxidation pathways.

During glycerol photoreforming, formic acid (formate) was identified as the main oxidation product, formed through intermediates such as GA and DHA, which were rapidly converted before full mineralization to CO₂, as detected^[30]. The optimal glycerol concentration was 0.075 M (6.9 g L^-1), corresponding to a solar-to-hydrogen (STH) conversion efficiency of 1.71%. Lowering the concentration to 0.05 M led to a marked decrease in hydrogen generation (STH = 1.26%). Among the tested substrates, glycerol proved the most efficient, producing 57 mmol H₂, followed by glucose (20.96 mmol) and ethanol (17.63 mmol). This superior performance was attributed to glycerol’s three easily oxidizable hydroxyl groups and low redox potential. Overall, the study demonstrated that Cu₂O-TiO₂ catalysts prepared by mechanochemical methods can be effectively scaled up, maintaining high performance, operational stability, and reproducibility under semi-industrial conditions.

Clarizia et al. investigated the effect of surface properties on copper-modified TiO₂ photocatalysts using in situ photoinduced deposition of Cu onto three different TiO₂ samples (100% anatase, 100% rutile, and P25)^[161]. Characterization through XRD, UV-Vis, TEM, XPS, and XANES/EXAFS confirmed the oxidized nature of copper species and their interaction with the TiO₂ support. However, under UV irradiation, copper was present as metallic Cu⁰ nanoparticles, formed via in situ photodeposition of Cu²⁺ ions. Interestingly, a big difference in photocatalytic performance was observed between methanol and glycerol as sacrificial agents. Superior activity for glycerol was observed and attributed to its molecular structure, which contains three hydroxyl groups, along with higher polarity and a greater number of hydrogen atoms in α-positions, favoring stronger adsorption on the photocatalyst surface. Glycerol also undergoes oxidation more readily than methanol, reacting more efficiently with photogenerated holes. Photocatalysts containing 1-10 wt.% Cu exhibited significant activity under UV irradiation, demonstrating that both the thermal pre-treatment and the TiO₂ polymorphic form play crucial roles in determining photocatalytic performance. Among the tested supports, P25 consistently outperformed pure anatase and rutile. This was attributed to the intrinsic homojunction between the anatase and rutile phases in P25, and its surface displaying a higher density of hydroxyl groups, serving as preferential nucleation sites for copper deposition. This leads to the formation of smaller, more uniformly dispersed Cu⁰ nanoparticles, maximizing the interfacial area between metal and semiconductor. The incorporation of copper also modifies the electronic properties of the Cu-TiO₂ heterostructure, primarily through the formation of a Schottky barrier at the metal-semiconductor interface. Additionally, plasmonic and optical effects may further enhance performance.

Interestingly, the study by Wang et al. reported the photoreforming of biopolyols and sugars to produce methanol and syngas (CO + H₂) under UV irradiation at room temperature^[160]. The photocatalyst was synthesized from anatase TiO₂, which was first transformed into protonated titanate nanotubes (H-TNTs), subsequently exchanged with ammonium (NH₄-TNTs), and finally subjected to ion exchange with Cu(NO₃)₂ followed by calcination to form defect-rich titanium oxide nanorods (TNRs). For comparison, a wide range of other semiconductor photocatalysts, including TiO₂ P25 and other metal oxides, were also evaluated. Using Cu²⁺ species dispersed on defect-rich TiO₂ nanorods (Cu/TNR), characterized by abundant O_v, the study reported the selective C-C bond cleavage of substrates such as glycerol, glucose, and even lignocellulosic biomass residues, leading to the formation of methanol and a mixture of CO and H₂. The Cu loading was varied between 0.01 and 5 wt.%, with 1-2 wt.% found to be optimal for methanol generation and 0.01 wt.% for high CO selectivity. The authors proposed that glycerol photoreforming proceeds via an initial hydrolysis step, forming intermediates such as GA and 1,3-DHA, concurrently with the production of H₂ and CO₂. Water acts as the primary hydrogen source, while glycerol undergoes dehydrogenation, with the overall efficiency governed by selective C-C bond cleavage without overoxidation. Under optimized conditions, the 2 wt.% Cu/TNR catalyst using glycerol achieved a methanol yield of approximately 40% and H₂ production of 22 mmol·g^-1 after 12 h of irradiation, with an AQE of 3.4%. The same system also yielded 45% CO, an H₂/CO ratio ≈ of 0.8, and 96% glycerol conversion. The method was further applied to various polyols (e.g., ethylene glycol, sorbitol, erythritol, xylitol) and sugars (e.g., fructose, glucose, sucrose), achieving methanol yields of 6%-28%, CO selectivity of 43%-52%, CO₂ yields of 5%-6%, and H₂ production ranging from 5 to 40 mmol·g^-1, depending on the carbon chain length and water content of the substrate. Remarkably, the approach was successfully extended to biomass-derived materials such as cellulose and wood sawdust, after pre-treatment via hydrolysis or hydrogenolysis, enabling methanol production up to 14%, along with syngas mixtures rich in H₂ and CO (up to 45% CO and 9.5 mmol·g^-1 H₂) using Cu/TNR catalysts with low or high Cu loadings, respectively. The copper loading was also shown to tune the selectivity between CO and CO₂ through controlled degradation of formic acid intermediates; low Cu content favored CO formation, while higher Cu loadings promoted CO₂ evolution.

Another possible modification involves using nickel-based co-catalysts. Eisapour et al. proposed the design of a p-n heterojunction between TiO₂ and NiO to enable the simultaneous generation of H₂ and selective production of DHA and GA from glycerol^[168]. The system employed two-dimensional anatase TiO₂ nanosheets combined with nickel oxide (NiO) nanoparticles. NiO (5 wt%) was deposited onto the TiO₂ nanosheet surface via an impregnation-calcination method, leading to well-dispersed NiO nanoparticles. As observed in microscopy images, dark contrast points on the nanosheet surface confirmed the nanometric nature and uniform distribution of NiO particles. Under Xe-lamp irradiation (300 W), the 7.5 wt% NiO/TiO₂ composite achieved an H₂ production rate of approximately 8.0 mmol g^-1·h. Recognizing that hydrogen production alone may be economically limited, the authors conducted a techno-economic analysis (TEA) to evaluate the integrated value of co-generated chemical products. From an initial 1.37 M glycerol solution, approximately 20% of glycerol was converted into high-value chemicals. GA accounted for ~89% of the projected annual revenue, followed by DHA (~11%) and H₂ (0.03%), highlighting the economic advantage of coupling energy generation with chemical valorization. Mechanistically, the formation of the p-n heterojunction between TiO₂ and NiO markedly enhanced charge carrier separation, steering the oxidation of glycerol toward selective formation of GA and DHA, rather than full mineralization to CO₂ as commonly observed for bare TiO₂.

The same group proposed the development of a “sandwich” NiO-Ni-TiO₂ heterojunction designed for the simultaneous coproduction of green hydrogen and value-added chemicals via glycerol photoreforming^[169]. The structure consists of consecutive layers in which TiO₂ and NiO are intercalated with an active metallic Ni layer, forming a p-n system with internal barriers that enhance electron-hole separation. The metallic nickel functions as a conductive layer, optimizing the internal electric field and consequently improving charge transport within the photocatalyst. For the synthesis, anatase TiO₂ was employed, and after comparative photocatalytic tests using different morphologies, the nanosheet type (sample S3) was identified as the most effective for hydrogen production. NiO-TiO₂ composite was obtained by mixing the TiO₂ nanosheets with a 15 wt.% nickel acetate solution in ethanol, followed by calcination at 450 °C. In the second step, the sandwich-type NiO-Ni-TiO₂ heterojunction (SPN) was synthesized by thermally treating the NiO-TiO₂ composite under a hydrogen flow at 500 °C, generating the metallic Ni interlayer. Finally, the Ni-TiO₂ sample was partially reoxidized in air at 350 °C. The optimized sample (10 wt.% Ni) achieved the highest activity (300 W Xenon lamp), producing 24.5 mmol g^-1 h^-1 of H₂ with AQE of 6.9 % at 365 nm. Glycerol conversion reached approximately 58 % after 24 h, generating primarily DHA and GA, with DHA being the most selective product (~21 % selectivity, ~12 % yield). The system demonstrated operational stability, maintaining high photocatalytic activity over repeated cycles.

Liu et al. also demonstrated a p-n heterojunction photocatalyst composed of TiO₂ and NiO, but featuring oxygen-bridged diatomic Ni-O-Ni sites instead of single-atom Ni sites, to optimize glycerol photoreforming through local electronic structure engineering^[170]. The strategy involved anchoring Ni-O-Ni diatomic sites onto a highly porous TiO₂ support derived from a MOF, employing oxalic acid chelation. The study demonstrated that atomic-level Ni deposition reduces the contact angle between TiO₂ and the glycerol-water mixture, thereby enhancing substrate adsorption. Multiple characterization techniques were employed to elucidate the reaction mechanism and the structure-activity relationship. Femtosecond TAS revealed that O-Ni₂/TiO₂ exhibits the longest average carrier relaxation lifetime (54.3 ± 2.6 ps), confirming effective suppression of charge recombination. XAFS (XANES and EXAFS) analyses verified that Ni atoms are coordinated to five oxygen atoms, forming Ni-O-Ni dimers. Contact angle measurements and DFT calculations demonstrated a stronger glycerol affinity (adsorption energy of -0.82 eV) and a reduced energy barrier for the rate-determining step (0.88 eV). Finally, in situ DRIFTS spectroscopy detected key intermediates (*CHO, *COOH, *CO), validating the proposed reaction pathway. Beyond syngas (H₂ and CO), the optimized catalyst also generated other valuable oxidized intermediates in both liquid and gas phases. ¹H NMR and HPLC analyses identified formaldehyde (HCHO), formic acid (HCOOH), and ethylene glycol as major liquid products, with production rates of 581.2, 866.7, and 658.4 µmol g^-1 h^-1, respectively. These compounds are key intermediates in the oxidation pathway leading to CO and CO₂, as confirmed by in situ DRIFTS analyses. Additionally, CO₂ was detected in the gas phase (113.5 µmol g^-1 h^-1) but was maintained at levels consistent with high syngas selectivity (96.1%). The catalyst achieved remarkably high H₂ and CO production rates of 2,542.6 and 361.7 µmol g^-1 h^-1, respectively. The study further demonstrated the versatility of O-Ni₂/TiO₂ by testing a variety of substrates, including C₁ molecules (methanol, formaldehyde, formic acid) and polyols C₄-C₆ (erythritol, xylitol, sorbitol), all of which yielded H₂ and CO. The proposed mechanism involves rapid migration of photogenerated electrons and holes to the catalyst surface, where Ni-O-Ni sites adsorb and oxidize glycerol into intermediates such as formaldehyde and formic acid, which subsequently form CO and CO₂. In parallel, protons are reduced by electrons to form H₂.

A pilot-scale hydrogen production via solar-driven photocatalysis using NiO-TiO₂ mixtures and glycerol as a sacrificial agent was reported by Villachica- Villachica-Llamosas et al.^[176] The aim was to evaluate the photocatalytic efficiency of this system under real solar irradiation and natural water conditions. Experiments were conducted in a 25 L pilot-scale compound parabolic collector (CPC) photoreactor with a 2.10 m² sun-exposed surface area, using both demineralized and natural water. The catalysts, commercial P25-TiO₂ and NiO, were mixed mechanically in different ratios (1:10, 2:1, and 5:10) and concentrations (25-200 mg L^-1). The best performance was achieved with NiO:TiO₂ = 1:10 at 50 mg L^-1, producing the highest hydrogen yield and a STH efficiency of 1.44 % in demineralized water, considering only the UV fraction of sunlight. The study also found that in natural water, hydrogen production was significantly lower (STH 0.4%) due to photocatalyst sedimentation promoted by ionic species. During the glycerol photoreforming process, H₂ and CO₂ evolution were monitored, and intermediate carboxylic acids were identified, confirming partial oxidation before complete mineralization. The H₂/CO₂ ratio initially exceeded the theoretical value (2.3) due to the formation of these intermediates but tended toward stoichiometry over time. Overall, the study demonstrates that commercial NiO and TiO₂ nanoparticles can achieve hydrogen production efficiencies comparable to those of more complex, synthesized photocatalysts. However, ionic strength, catalyst sedimentation, and water quality are key limiting factors under real solar conditions. The authors conclude that for large-scale solar hydrogen generation, flow photoreactors with higher catalyst loadings may be required, especially when using saline wastewater as feedstock. Similarly, Toledo-Camacho et al. also demonstrated hydrogen generation from water-glycerol mixtures using Pd/TiO₂ photocatalysts in a 25 L solar CPC pilot plant^[177]. The photocatalyst containing 0.25 wt% Pd exhibited a satisfactory activity, achieving a quantum yield of approximately 2.4%.

Li and Zhang reported the use of an anatase TiO₂ modified with Ba²⁺ ions to optimize the photocatalytic conversion of glycerol and nitrate into glycine^[178]. The incorporation of Ba²⁺ was found to be crucial, as it enhances charge separation, prolongs carrier lifetimes, and increases the surface density of hydroxyl groups on the catalyst. The reactions were conducted under UV irradiation (365 nm) at 50 °C, in a sealed argon atmosphere. The proposed mechanism involved a cascade of coupled reactions: glycerol undergoes photoreforming to produce glycol, while nitrate is reduced to ammonia (NH₃). The key step is the coupling of glycol with NH₃ to generate glycine. Simultaneously, nitrate acts as a nitrogen source and moderates overoxidation by scavenging hydroxyl radicals (^•OH) to form ^•NO₃, thereby enhancing reaction selectivity. Radical species such as ^•CHOHCH₂OH and intermediates like glycol and methanol were detected using EPR experiments. The glycine production rate reached 765 µmol·g^-1·h^-1, with a 5.3 % yield and nearly 100 % glycerol conversion. The Ba²⁺-TiO₂ catalyst outperformed other tested materials, including pure TiO₂ and modified with Ag, Cu, Mg, Ca, and Sr. The system also demonstrated substrate versatility, successfully converting various polyols (glycerol, glycol, erythritol, xylitol, sorbitol), sugars (glucose, fructose, xylose), and even raw biomass (wood sawdust) hydrolysis, showing potential for glycine production from renewable feedstocks. Comparisons highlighted the essential roles of nitrate and Ba²⁺-TiO₂, since glycerol alone with pure TiO₂ showed poor selectivity, and replacing nitrate with NH₄⁺ or NH₃ was ineffective.

Kobayashi developed a cascade photoredox system designed to integrate photocatalytic and redox mechanisms in a coordinated manner, combining homogeneous and heterogeneous catalysts to improve substrate contact and enhance charge separation efficiency^[173]. This approach primarily aims to overcome limitations related to the restricted interaction between solid catalysts and complex organic substrates in biomass, particularly those with low solubility, such as cellulose. The system, termed the Photoredox Cascade Catalyst (PRCC), consists of TiO₂ nanoparticles loaded with platinum and functionalized with two polypyridine-type ruthenium dyes, forming a dual-dye-sensitized photocatalyst (DDSP). The DDSP absorbs blue light (λ ≈ 460 nm), generating electrons that reduce protons to hydrogen, while simultaneously oxidizing the homogeneous catalyst 2,2,6,6-tetramethylpiperidine-1-oxyl (TEMPO). TEMPO acts as a redox mediator, being oxidized to TEMPO⁺ by DDSP and subsequently regenerated through oxidation of organic substrates such as glycerol or cellulose. Additionally, N-methylimidazole is incorporated to facilitate proton transfer, stabilizing the photocatalytic process and promoting efficient charge separation. The functional integration of DDSP, TEMPO, and the acid-base mediator creates a closed catalytic circuit that partially mimics the electron transport chain of natural photosynthesis. Experimental results showed high hydrogen production rates, reaching 2.7 mmol g^-1·h^-1 for glycerol photoreforming and 1.6 mmol g^-1·h^-1 for cellulose, the latter particularly notable given the substrate’s low solubility. The system also exhibited stability and reproducibility over multiple reaction cycles. Other substrates were evaluated, including 2-propanol and glucose. For 2-propanol, H₂ production was significantly lower, about 0.7 mmol g^-1·h^-1, consistent with TEMPO’s selectivity for primary alcohols. In contrast, glucose outperformed glycerol, producing 1.3 times more H₂ (3,430 μmol g^-1·h^-1), attributed to its greater reducing capability and the formation of carboxylate groups via primary alcohol oxidation. This study highlights the potential of hybrid photocatalytic systems for highly efficient and selective solar-driven hydrogen production, with promising applications in biomass-based fuel generation and sustainable chemical platforms.

As it becomes clear from some of the above-cited examples, the photoreforming studies on glycerol can be readily extended to other polyols typically found on biomass residues. They contain predominantly lignocellulosic materials, whose main structural constituents are carbohydrates, cellulose and hemicellulose, and the aromatic polymer lignin^[179]. Moreover, such residues are carbon-neutral sources of electrons for photocatalytic reactions, acting simultaneously as a scavenger for photogenerated holes to support hydrogen evolution, while converting renewable feedstocks into value-added chemicals^[180,181]. Nevertheless, despite these advantages, the efficiency of current systems remains far from practical application. Major challenges stem from the structural complexity, poor solubility, and the recalcitrant nature of lignocellulosic biomass, which hinder its interaction and electron transfer with heterogeneous photocatalysts. Moreover, the intrinsic limitations of conventional photocatalysts, such as narrow light absorption and rapid charge recombination, call for advanced material design^[179]. Therefore, the pursuit of more efficient and sustainable photocatalytic routes for biomass valorization has intensified in recent years, with particular attention to innovations involving TiO₂-based composite materials.

Liu et al. report a composite of anatase-phase titanium dioxide (TiO₂) with carbon nanosheets (a-TiO₂@MC) applied for the photoreforming of xylose^[182]. This approach addresses classic limitations of pure TiO₂, such as its wide bandgap and slow electron-transfer dynamics. The developed method involves hybridizing TiO₂ with carbon nanosheets derived from chitosan biochar and sodium carboxymethylcellulose, resulting in a reduced bandgap (2.55 eV) and notable improvements in charge separation and transfer, evidenced by techniques such as ultraviolet photoelectron spectroscopy (UPS) and Mott-Schottky plots. Xylose, a sugar derived from lignocellulosic biomass, was used as the substrate for selective conversion into xylonic acid and lactic acid, both high-value products. The proposed mechanism was based on a selective oxidation of xylose, with holes (h⁺) acting as the primary oxidizing agents alongside hydroxyl radicals (^•OH) and singlet oxygen (¹O₂). Regarding performance, the authors report yields of 52% for xylonic acid under low alkalinity conditions (0.2 M KOH, 50 °C) and 49% for lactic acid under high alkalinity (3 M KOH) and elevated temperatures. Another notable aspect is the operational stability of the photocatalyst, retaining 99% of its activity after nine cycles, as well as its industrial potential, demonstrated in scaled-up solar experiments, achieving 69% of the laboratory-scale yield.

Enhancing the efficiency of photocatalysts for the conversion of solid biomass, such as cellulose, has relied on both support engineering and the optimization of active metal dispersion. Therefore, Lan et al. aimed to elucidate the impact of TiO₂ composition (pure anatase vs. anatase/rutile mixture) and platinum loading on the performance of Pt/TiO₂ catalysts for hydrogen production via cellulose photoreforming^[33]. The photocatalysts were prepared by the impregnation method and tested in aqueous photoreforming under UV-A irradiation at 40 °C, with Pt loadings ranging from 0.16% to 1.00%. The authors reported that the TiO₂ support significantly influences the structure of Pt species, especially at low loadings (0.16%), promoting the formation of sub-nanometric particles and enhancing charge separation. This results in higher hydrogen production rates, particularly for mixed-phase TiO₂ (80% anatase, 20% rutile). Conversely, increasing the Pt loading leads to the growth of metallic particles (> 1-2 nm), promoting charge recombination and a marked decrease in catalytic activity for both supports. Mechanistic studies revealed that H₂ is generated via a formic acid-driven pathway, which was primarily formed during cellulose degradation. More recently, the group also conducted an in-depth mechanistic study of glucose photoreforming for hydrogen production, employing a combined approach of product analysis (HPLC, GC) and in situ spectroscopic techniques, such as attenuated total reflectance infrared spectroscopy (ATR-IR) and isotopic labeling, to compare the activity of TiO₂ and Pt/m-TiO₂ photocatalysts^[183]. The results confirmed that glucose oxidation occurs predominantly via an α-cleavage mechanism, leading sequentially to the formation of arabinose (a C₅ sugar) and formic acid. The platinum-modified catalyst (Pt/m-TiO₂) exhibited an activity 13.4 times higher than that of pure TiO₂, attributed to its superior efficiency in separating photogenerated electron-hole pairs. Another contribution of the work was the identification of the central role of formic acid, elucidated by ATR-IR analysis. This intermediate preferentially adsorbs on the catalyst surface, and its subsequent oxidation at Pt-TiO₂ interfaces is the rate-determining step. Additionally, isotopic studies revealed that at low glucose concentrations, the protons for H₂ generation are predominantly derived from water molecules. Therefore, this study highlights the system’s efficiency dependency, not only on the degradation of the initial substrate, but critically on the catalyst’s ability to oxidize key intermediates adsorbed on its surface.

Another strategy to enhance the efficiency of sugar photoreforming is the morphological engineering of TiO₂-based catalysts, particularly by improving mass diffusion and catalytic accessibility^[181]. Shi et al. report the development of three-dimensional hierarchical TiO₂ microspheres (THM), obtained via a template-free hydrothermal route, aimed at optimizing the photocatalytic conversion of glucose into hydrogen and high-value compounds such as arabinose and formic acid^[61]. The study explores the influence of synthesis parameters, such as TiCl₄ concentration, reaction time, and temperature, on the growth mechanism and microsphere structure, elucidated as a “nucleation-dissolution-recrystallization-assembly” process. The resulting THMs exhibit a “sea urchin” morphology, an average diameter of approximately 5 μm, a high specific surface area, and the presence of O_v, which significantly reduce the optical bandgap (2.92 eV). The presence and concentration of O_v were quantified by EPR, showing a direct correlation between defect density, enhanced electron-hole separation, and improved photocatalytic efficiency. Photocatalytic tests were performed with Pt as a cocatalyst, in a H₂O/MeCN solvent mixture, and demonstrated an H₂ production rate of 9.44 mmol g cat^-1 h^-1, glucose conversion of 86%, arabinose selectivity of 11%, and formic acid selectivity of 47%. Modulation of reaction conditions, particularly the use of the H₂O/MeCN solvent and pH adjustment with Na₂CO₃, was crucial to favor glucose adsorption and stabilize reactive intermediates, directly contributing to the observed selectivity. These results reflected in substantially superior photocatalytic performance compared to commercial TiO₂, showing up to a 135-fold increase in H₂ production. The reaction mechanism involves glucose oxidation mainly via ROS (^•O₂^- and ^•OH), promoting α C1-C2 cleavage and Ruff degradation, which favors the formation of highly selective products. The study emphasizes that the 3D hierarchical architecture, combined with structural defects (O_v, Ti³⁺), not only enhances light absorption and charge separation but also facilitates glucose accessibility to active sites, making the photocatalytic process more efficient, sustainable, and applicable under mild operating conditions.

Interestingly, the introduction of O_v combined with thermal and photonic energy was studied by Wu et al., who performed the thermo-photocatalytic reforming of lignin using Pt/TiO₂ nanosheets with varying concentrations of O_v^[67]. Through controlled synthesis and advanced characterizations, including DFT calculations, the authors investigated how O_v modulate the material’s electronic structure to simultaneously produce H₂ and value-added chemicals, such as aromatic aldehydes. It was demonstrated that O_v promote electron delocalization, shifting the Pt d-band center to lower energy levels. This modulation results in charge redistribution, with TiO₂ becoming electron-deficient and Pt electron-enriched, which facilitates charge separation and the desorption of reactive intermediates. Consequently, the combination of thermo-photocatalytic catalysis (at 473 K) with defect engineering resulted in a remarkable H₂ production rate close to 1 mmol g^-1 h^-1 from lignin, an 18.2-fold increase compared to the purely photocatalytic process, along with high selectivity toward value-added aromatic aldehydes. The synergy between energy sources was crucial for enhancing performance. Thermal energy accelerates the kinetics of radical formation (^•OH, h⁺, e^-) and mass transfer, promoting the selective cleavage of C-O bonds in lignin, while photonic energy initiates the process. The study concludes that oxygen vacancy engineering creates a bifunctional catalyst, optimizing oxidation on TiO₂ and reduction on Pt, whereas the thermo-photocatalytic approach overcomes kinetic barriers, establishing an effective strategy for lignin valorization into H₂ and sustainable chemicals.

The combination of hierarchical architectures with the optical properties of metallic nanoparticles was also explored by Zhao et al. Three-dimensional ordered macroporous titanium dioxide (3DOM TiO₂) was functionalized with gold nanoparticles (Au) and applied for glucose photoreforming, with coproduction of arabinose and gaseous fuels (H₂, CH₄, CO) in pure aqueous medium^[69]. The 3DOM TiO₂-Au composite exhibited significantly superior photocatalytic performance, achieving 37% glucose conversion and 0.2 g/L arabinose production, corresponding to increases of 2.8 and 10 times, respectively, compared to pure TiO₂. The enhancement in activity was attributed to the synergy between the 3DOM structure, which facilitates mass diffusion and optimizes light harvesting, and the Au nanoparticles, which promote more efficient charge separation and intensify light absorption via the localized surface plasmon resonance (LSPR) effect. The proposed reaction mechanism involves α-cleavage of the C1-C2 bond in the glucose molecule, resulting in the selective formation of arabinose and formic acid. The latter acts as an intermediate that is subsequently decomposed to generate the gaseous fuels (H₂, CH₄, CO). Zhong et al. showed the performance of a ternary TiO₂-Au-CdS photocatalyst featuring a hierarchical 3DOM architecture^[184]. It achieves a high hydrogen production rate from glucose (645.1 μmol h^-1 g^-1), which decreases with increasing substrate complexity, from cellobiose (273.9 μmol h^-1 g^-1) to dissolving pulp (79.7 μmol h^-1 g^-1). The generation of CO and CH₄ further confirmed the partial conversion of biomass during photoreforming.

Moreover, the complex relationship between photocatalyst’s properties and its activity in biomass conversion remains a field of intense investigation. For instance, Umair et al. present a comprehensive comparative study on the activity of modified TiO₂ photocatalysts (with Pt, Cu₂O, and Nb) for the photoreforming of glucose and fructose under simulated sunlight and ambient temperature^[34]. The main goal of the study was to correlate photoactivity with the structural and surface characteristics of the materials, aiming to elucidate the factors governing efficiency in H₂ production and selective substrate oxidation. To achieve this, the authors investigated different TiO₂ polymorphs (anatase, rutile, and brookite) modified via Pt deposition, Nb doping, and coupling with Cu₂O. Photocatalytic tests revealed that activity depends on a complex interplay of factors. While pure TiO₂ was inactive for H₂ production, the modified photocatalysts exhibited significantly higher rates compared to commercial benchmarks. Cu₂O modification emerged as a more economical alternative to platinum for this purpose. Nb doping, although improving charge separation, resulted in lower H₂ production than Pt and Cu₂O. Additionally, the study illustrated platinum’s multifaceted role. Beyond its well-established function as an electron sink that minimizes charge recombination (confirmed by EPR analyses), Diffuse reflectance infrared Fourier transform spectroscopy (DRIFTS) and TPD analyses revealed that Pt also significantly modifies the acid-base properties of the TiO₂ surface. Although no direct or monotonic correlation was established, this surface modulation affects substrate interactions and, consequently, reaction selectivity, with home-prepared Pt (Pt-HP) standing out for partial sugar oxidation. Therefore, this work shows that optimizing photocatalysts for biomass valorization relies on a delicate balance between crystal phase, surface properties, and charge separation efficiency, highlighting the unusual and significant role of platinum in modulating surface acidity. Interestingly, Umair et al. reported that the combined presence of Pt and Nb₂O₅ on TiO₂ generated strong basic sites^[34]. The photoreforming of glucose and fructose was examined using TiO₂ combined with 0.5 wt% Pt and 4 wt.% of Nb₂O₅, in which Pt improved charge separation and introduced additional basic sites, while niobium oxide reduced electron-hole recombination and modified surface acidity. Together, Pt and Nb₂O₅ created an optimal balance of acid-base properties and electronic structure, facilitating efficient partial oxidation of sugars and hydrogen evolution.

Similarly to other photocatalytic processes, the use of non-noble metals for biomass photoreforming is a highly explored approach aiming at reduced implementation costs^[185-187]. Belda-Marco et al. present an investigation on hydrogen and organic acid production from cellulose applying commercial TiO₂ (P25) modified with bimetallic cocatalysts composed of copper and nickel^[188]. The study focused on optimizing photocatalyst preparation by evaluating the impact of two main variables: the total metal loading (1 and 5wt.%) and the sequence of metal deposition (simultaneous or sequential). Under UV light irradiation (365 nm), the TiO₂ semiconductor is excited, generating electron-hole pairs (e^-/h⁺). The Cu and Ni nanoparticles on the surface act as cocatalysts, forming a Schottky barrier that facilitates electron transfer from TiO₂ to the metals. Simultaneously, holes (h⁺) on the TiO₂ surface promote the oxidation of cellulose and its byproducts (such as glucose and other sugars), producing value-added organic acids (formic, acetic, oxalic) and, to a lesser extent, CO₂. The results show that process efficiency is strongly influenced by both metal loading and deposition sequence. Photocatalysts with lower metal loading (1 wt.%) were significantly more active than those with higher loading (5 wt.%), attributed to reduced surface coverage of TiO₂, which allows for greater light absorption. Furthermore, sequential metal deposition outperformed simultaneous deposition, indicating that the order of addition promotes a more favorable interaction between Cu-Ni and the support. The best-performing catalyst was P25-NiCu-L, prepared with 1wt.% metal loading and sequential deposition of nickel followed by copper, achieving a remarkable hydrogen production of 489 μmol h^-1·g^-1. This value is among the highest reported for non-noble metal catalysts, highlighting the potential of this strategy for clean energy production from biomass.

Eqi et al. reported the synergistic effect of bimetallic Ni-Au nanoparticles for glucose photoreforming over TiO₂^[68]. Under light irradiation, electrons are transferred from TiO₂ to the Au and Ni nanoparticles, which have high work functions, facilitating charge separation for photocatalysis. The presence of Au nanoparticles also enhances visible-light absorption through the LSPR effect. During the oxidation process, glucose is primarily converted into gluconic acid via the action of superoxide radicals (^•O₂^-). Subsequently, gluconic acid undergoes decarboxylation through C1-C2 bond cleavage. This step is specifically promoted by the Ni nanoparticles, which are effective in breaking carbon-carbon bonds, resulting in the selective formation of arabinose. Simultaneously, the electrons accumulated on the metallic nanoparticles reduce protons in the aqueous solution to produce gaseous hydrogen. The results demonstrated superior catalytic performance of the bimetallic material compared to monometallic catalysts and pure TiO₂. The optimized catalyst, Ni_0.05Au_0.45/TiO₂, exhibited the highest hydrogen production rate, reaching 64 mmol h^-1 g^-1. This value is almost 120 times higher than pure TiO₂, 31 times higher than Ni/TiO₂, and almost two times higher than Au/TiO₂. In addition, glucose conversion reached 95%, with an arabinose selectivity of 36%. The success of the process was attributed to the synergistic effect between Ni and Au, as well as the three-dimensional hierarchical structure of TiO₂, which facilitates mass transport and accessibility of glucose to the active sites of the catalyst.

Moreover, the search for efficient and low-cost photocatalysts, free of noble metals, has driven the development of semiconductor heterojunctions. Zhao et al. developed an ultrathin n-p core-shell heterojunction nanostructure composed of TiO₂ and NiO, synthesized via a one-pot hydrothermal method^[70]. The main objective was to enhance the separation of photogenerated charges and, consequently, improve the efficiency of H₂ production from the photocatalytic reforming of lignin. The optimized material, containing 3.25% NiO, exhibited a H₂ production rate of 23.5 mmol h^-1 g^-1 in a water-methanol solution, significantly outperforming pure TiO₂. When applied to lignin photocatalytic reforming in an alkaline medium, the catalyst was able to coproduce H₂ (0.45 mmol h^-1 g^-1) and methane (CH₄), in addition to converting the biomass into long-chain fatty acids, such as palmitic and stearic acids. This superior performance was attributed to the synergy between high crystallinity, the core-shell architecture, and, critically, the formation of an internal electric field at the n-p heterojunction interface, which efficiently suppresses charge carrier recombination. The study concludes that the ultrathin TiO₂-NiO n-p heterojunction represents an effective strategy for solar-to-chemical energy conversion without the need for noble-metal cocatalysts.

This review has shown that significant progress has been achieved in the field of TiO₂-based photoreforming of alcohols and biomass-derived substrates as a viable pathway for low-carbon hydrogen production. Deep understanding of fundamental aspects concerning the selectivity of the oxidation reactions and the overall mechanism of the consecutive reactions following initial light-induced charge transfer steps has been described for several alcohols based on advanced spectroscopic techniques. Photoreforming of model alcohols such as methanol and ethanol has provided valuable insights into reaction mechanisms, charge carrier dynamics, and the identification of intermediate species. Such studies have guided the development of new photocatalyst systems with improved efficiency compared with pristine TiO₂. This includes doping, heterojunction formation, and the use of co-catalysts, which enable enhanced charge separation, visible-light harvesting, and improved hydrogen evolution rates, although few reports deal with the challenge of tuning the photocatalytic oxidation selectivity.

The extension of photoreforming studies from methanol to more complex substrates, such as C2+ alcohols, glycerol, and other biomass derivatives, reveals the increasing challenges associated with molecular complexity. These include more intricate reaction pathways, formation of a wider range of intermediates, and a greater dependence on catalyst surface properties. Future research should focus on surface engineering to enhance the formation/stabilization of key radical intermediates to drive selectivity, as well as a deeper understanding of the role of physicochemical conditions (pH, ionic strength, etc.) on the overall efficiency and selectivity of the process.

Such advances can facilitate the design of systems capable of operating on real and complex biomass-derived streams. A deeper understanding of reaction mechanisms, particularly for more complex substrates, will be crucial for guiding photocatalyst design and improving selectivity toward desirable products. Moreover, integrating photoreforming processes with waste valorization strategies and renewable energy inputs could further enhance their sustainability and practical relevance. Overall, TiO₂-based photoreforming of alcohols represents a promising and versatile approach for sustainable hydrogen production. Continued efforts in photocatalyst development, mechanistic understanding, and process integration will be key to advancing this technology toward practical and scalable applications in a future low-carbon energy landscape.