PHOTOCATALYST FOR EFFICIENT HYDROGEN GENERATION
20200002826 ยท 2020-01-02
Inventors
Cpc classification
C25B11/091
CHEMISTRY; METALLURGY
Y02P20/133
GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
Y02E60/36
GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
International classification
C25B1/00
CHEMISTRY; METALLURGY
Abstract
Certain embodiments of the invention are directed to a water splitting photo electrochemical (PEC) thin film comprising metal nanostructures positioned between a Cd.sub.xZn.sub.1xS semiconductor and a ZnO semiconductor to form a Z-scheme for total water splitting.
Claims
1. A water splitting photoelectrochemical (PEC) catalyst comprising metal (M1) nanostructures positioned between a Cd.sub.xZn.sub.1xS semiconductor and a ZnO semiconductor to form a Z-scheme catalyst having the structure ZnO/M1/Cd.sub.xZn.sub.1xS, where x is less than 1.
2. The PEC catalyst of claim 1, wherein the M1 nanostructures comprise a transition metal.
3. The PEC catalyst of claim 3, wherein the M1 nanostructures comprise Pt, Ni, Cu, Fe, Au, Pd, or Ag or combinations thereof.
4. The PEC catalyst of claim 3, wherein the M1 nanostructures is Pt, AuPd, Au, or Pd.
5. The PEC catalyst of claim 2, wherein the M1 nanostructures are core-shell nanoparticles.
6. The PEC catalyst of claim 3, wherein the M1 nanostructures comprise Cu, Fe, Au, Pt, Pd, Ni, Ag metals, alloys of two or three metals, or core-shell nanostructures.
7. The PEC catalyst of claim 1, wherein the ZnO to M1 nanostructure ratio is 50:1 to 1000:1.
8. The PEC catalyst of claim 1, wherein ZnO to S ratio is 4:1 to 1:2.
9. The PEC catalyst of claim 1, wherein the catalyst is ZnO/1 wt. % Pt/Cd0.82Zn.sub.0.1S or [ZnO].sub.4/1 wt. % Pt/Cd.sub.0.9Zn.sub.0.1S.
10. A photocatalytic reactor comprising a reactor having an inlet for feeding water or aqueous solution to a reactor chamber, the reaction chamber comprising: (i) a photo electrochemical (PEC) assembly comprising a PEC photocatalyst of any one of claims 1 to 8; (ii) a H.sub.2 gas product outlet; and (iii) O.sub.2 gas product outlet.
11. The reactor of claim 9, wherein the Cd.sub.xZn.sub.1xS semiconductor is deposited on a conductive support.
12. The reactor of claim 11, wherein the conductive support has a base coat of a hydrogen catalyst.
13. The reactor of claim 12 wherein the hydrogen catalyst comprises Pt, Pd, Au, Ag, Ir, Ru, Rh, Mo, Ni, Ce, Co, Fe, W, Sn, and combinations thereof.
14. The reactor of claim 13, wherein the catalyst comprises two metals at a ratio of between 10:1 to 1:10.
15. The reactor of claim 11, wherein the conductive support can be a stainless steel, molybdenum, titanium, tungsten, or tantalum, or combinations thereof.
16. The reactor of claim 10, wherein the ZnO semiconductor further comprises a hole transporting thin film.
17. The reactor of claim 10, further comprising an oxygen co-catalyst comprising a metal oxide having the general formula of AO.sub.y or B.sub.zN.sub.1zO.sub.y, where A and B are metals, and z is <1 and y is a value that balances the valence of the oxide.
18. The reactor of claim 17, wherein the oxygen co-catalyst is a nickelate (IrNiO.sub.3).
19. A method of producing hydrogen comprising irradiating a photo electrochemical (PEC) thin film with light in the presence of water, the PEC thin film comprising the photocatalyst of claim 1.
20. The method of claim 19, wherein the metal nanoparticle is Pt, Au, Pd, Ni, Fe, Cu, or Ag; alloys of two or three metals; or core-shell nanostructures.
Description
DESCRIPTION OF THE DRAWINGS
[0028] The following drawings form part of the present specification and are included to further demonstrate certain aspects of the present invention. The invention may be better understood by reference to one or more of these drawings in combination with the detailed description of the specification embodiments presented herein.
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DETAILED DESCRIPTION OF THE INVENTION
[0042] A solution to at least some of the problems associated with light harvesting associated with photocatalytic systems has been discovered. The solution is premised on an integrated photocatalyst that shows a redox potential scheme corresponding to the Z-scheme, the total potential difference of which is sufficient to permit cleavage of water into hydrogen and oxygen when the catalyst is irradiated with light (e.g., sun light) that includes a wavelength of at least 420 nm, 430 nm, 440 nm, 450 nm, and up to 700 nm. An integrated photocatalyst described herein can be in the form of a plate, a film, or a tube. In certain aspects the integrated photocatalyst is a photo electrochemical (PEC) thin Film. A water splitting PEC thin film described herein can comprise metal nanoparticles positioned between a first semiconductor and a second semiconductor to form a Z-scheme for total water splitting.
[0043] Semiconductor materials can include: elements from Column 4 of the Periodic Table; materials including elements from Column 3 and Column 5 of the Periodic Table; materials including elements from Columns 2 and 4 of the Periodic Table; materials including elements from Columns 1 and 7 of the Periodic table; materials including elements from Columns 4 and 6 of the Periodic Table; materials including elements from Columns 5 and 7 of the Periodic Table; and/or materials including elements from Columns 2 and 5 of the Periodic Table. Other materials with semiconductive properties can include layered semiconductors, metallic alloys, miscellaneous oxides, some organic materials, and some magnetic materials.
[0044] First semiconductorIn certain aspects, the first semiconductor can include cadmium-based materials having a band gap that from 1.7 to 2.8 eV, or 2.0 to 2.5, or 2.1 to 2.3 eV, or any range or value there between. In certain aspects a first semiconductor is a Cd.sub.xZn.sub.1xS (2.4 eV) semiconductor, where x is less than 1, from 0.01 to 0.99, from 0.7 to 0.9, or any value at least, equal to, or between any two of 0.01, 0.05, 0.1, 0.15, 0.2, 0.25, 0.3, 0.35, 0.4, 0.45, 0.5, 0.55, 0.6, 0.65, 0.70, 0.75, 0.8, 0.81, 0.82, 0.83, 0.84, 0.85, 0.9, 0.95, and 0.99, but less than 1. In one embodiment the Cd:Zn molar ratio is 1:9 to 9:1, or 1:9, 1:8, 1:7, 1:5, 1:1, 2:1, 3:1, 3.5:1, 4:1, 4.5:1, 5:1, 5.5:1, 6:1, 7:1, 8:1, 9:1 or any range or value there between. In a preferred embodiment x is about 0.82.
[0045] Second semiconductorA second semiconductors is a semiconducting material with a wider band gap that the first semiconductor, that is for example from 2.4-3.2 eV. Non-limiting examples of semiconductors include ZnO, TiO.sub.2, SrTiO.sub.3 and BiVO.sub.4. In certain aspects the second semiconductor is ZnO.
[0046] Metal nanoparticlesThe amount of M1 loading in the Z-scheme catalysts can be from 0.05 wt. % to 1 wt. %, or 0.1 wt. % to 0.8 wt. %, or at least, equal to, or between any two of 0.05 wt. %, 0.1 wt. %, 0.15 wt. %, 0.2 wt. %, 0.3 wt. %, 0.4 wt. %, 0.5 wt. %, 0.6 wt. %, 0.7 wt. %, 0.8 wt. %, 0.9 wt. %, and 1 wt. %. In some embodiments, the nanostructures are nanoparticles. The present invention provides the advantage of using less expensive metals (Ag, Pd, Cu, and Ni) as well as bimetallic systems (Au/Ni, Ag/Ni, Au/Pd, Ag/Pd, Au/Cu and Ag/Cu). The preparation of the Z-scheme catalyst can be done using known catalysts preparation methods. Referring to
[0047] The Z-scheme photocatalysts of the present invention can be used in a water-splitting system that include a hydrogen co-catalyst and an oxygen co-catalyst.
[0048] Hydrogen co-catalyst 204 can be deposited on a second portion of support material 214 opposite of Z-scheme photocatalyst 202. A thickness of hydrogen co-catalyst can be 0.01 to 50 nm, 1 to 30 nm or 5 to 15 nm, or any value or range there between, or about 10 nm. The hydrogen generation catalyst can have two metals at a ratio of 10:1, 9:1, 8:1, 7:1, 6:1, 5:1, 4:1, 3:1, 2:1, 1:1, 1:2, 1:3, 1:4, 1:5, 1:6, 1:7, 1:8, 1:9, to 1:10. Non-limiting examples of hydrogen production co-catalysts can include Pt, Pd, Au, Ag, Ir, Ru, Rh, Mo, Ni, Ce, Cu, Co, Fe, W and Sn as well as combinations thereof (e.g., Mo:Ni catalyst in a 1:1 weight ratio). In certain aspect, the Mo/Ni hydrogen catalyst can have a Mo:Ni a ratio of 10:1 to 1:10, including all values and ranges there between.
[0049] Oxygen producing co-catalyst 206 can be deposited on a portion of the second semiconductor 212 (e.g., metal oxide or carbon nitride material). A thickness of oxygen producing co-catalyst 206 can be 0.01 to 50 nm, 1 nm to 40 nm or 10 to 30 nm, or any range or value there between, or about 30 nm. Oxygen co-catalyst 206 can be a metal oxide (AO.sub.y) or (A.sub.zB.sub.1zO.sub.y) where z<1 and y is a value sufficient to balance the valence of the metal. The metals (A) and/or (B) can be Pt, Pd, Au, Ag, Ir, Ru, Rh, Mo, Ni, Cu, Co, Fe, W, Sn, and combinations thereof. The metals can be deposited, for example, on ZnO/M1/Cd.sub.xZn.sub.1xS by the light deposition, electrochemical deposition, pulse laser deposition and chemical vapor deposition methods. A wireless total water splitting system can be fabricated using a ZnO/M1/Cd.sub.xZn.sub.1xS base.
[0050] An apparatus or system for the production of hydrogen from water or aqueous solutions of organic compounds by using the Z-Scheme photocatalyst of the present inventions or apparatus described herein can include one or more of (i) a light source (such as a visible light source), (ii) a reactor (optionally a transparent portion for light if the light source is external to the reactor), (iii) an inlet for feeding water or aqueous solution to the reactor, and (iv) a gas product outlet for releasing hydrogen liberated in the reaction chamber. The photocatalyst described herein can be located inside the reactor. The apparatus or system for the production of hydrogen can also include a storage chamber for collecting and storing the molecular hydrogen produced. The storage chamber can be in communication with the reaction chamber via the gas or product outlets. The storage chamber may be pressurized.
[0051] Valves may also be present, to control the flow of water or aqueous solution into the reactor via the inlet and release of gas via the outlet. Control means may also be present to adjust the light source intensity or even switch it on or off (e.g., provide access or block sunlight) as required. The reaction chamber or reactor may further comprise a waste outlet for removal of waste or by-products or unreacted water or aqueous solution, the waste outlet optionally having a valve. Still further, the hydrogen production device may comprise control means operably linked to the valves for controlling the flow of water or aqueous solution into the reaction chamber, the flow of molecular hydrogen through the outlet (and into the storage chamber if present), and/or the flow of waste or by-products or unreacted water or aqueous solution through the waste outlet.
EXAMPLES
[0052] The following examples as well as the figures are included to demonstrate preferred embodiments of the invention. It should be appreciated by those of skill in the art that the techniques disclosed in the examples or figures represent techniques discovered by the inventors to function well in the practice of the invention, and thus can be considered to constitute preferred modes for its practice. However, those of skill in the art should, in light of the present disclosure, appreciate that many changes can be made in the specific embodiments which are disclosed and still obtain a like or similar result without departing from the spirit and scope of the invention.
[0053] Stock solution used in the Examples are listed in Table 1.
TABLE-US-00001 TABLE 1 MW Mass V(mL) in Molar Purity Chemicals (g/mol) (g) Mole (mmol/ml) MeOH conc. (%) Zn(CH.sub.3CO.sub.2)2H.sub.2O 220 1.76 0.08 100 0.08M 99 Cd(CH.sub.3CO.sub.2)2H.sub.2O 266.5 0.08 100 0.08M 99 Na.sub.2SxH.sub.2O 78 1.3 0.1 100 0.1M 60 KOH 56 1.5 30 99 NaBH.sub.4 38 0.152 0.04 100 0.04M 99 HAuCl.sub.43H.sub.2O 393.8 0.394 0.01 (1.9 100 0.01M 99 mg (Au)/mL) AgNO.sub.3 169.8 0.79 1 mg (Ag)/mL 500 0.0093M 99 H.sub.2PtCl.sub.66H.sub.2O 409 0.961 1.9 mg (Pt)/mL 200 0.012M 99.9
Example 1
Synthesis of ZnO
[0054] Zn(CH.sub.3COO).sub.2.2H.sub.2O (2.64 g, 12 mmol) was added to methanol (210 mL) in a 500 mL 3 neck RBF and the temperature was raised to about 60 C. After 10 minutes, methanolic solution of KOH (1.50 g, 26.7 mmol) in 30 mL of water was added drop wise to the reaction solution while stirring and then the stirring was continued for 2 h at 60 C. The color of the solution became turbid at the initial stages and then changed to colorless after 30 min. After 2 h, the solution slowly turned to white color (the particle size also depends on the size of the magnetic bead and rpm of stirring e.g., 600 rpm). Formed ZnO nanoparticles were precipitated out by addition of water and the excess ions were removed by centrifugation. The resulting product was washed with methanol and dried at about 60 C. for 2 hours to give ZnO.
Example 2
Synthesis of M1 on ZnO
[0055] Synthesis of Au@ZnO. HAuCl.sub.4 (1.97 mg (Au)/mL, 1.7 mL) was added drop-wise to a methanolic solution of ZnO (0.33 g, 4.1 mmol) nanocrystals, followed by 5 mL of NaBH.sub.4 (40 mM) aqueous solution. The solution was stirred for 10 min. The solution color became black due to the formation of gold on ZnO nanoparticles. The resulting solution was centrifuged, filtered and dried in air to give Au@ZnO.
[0056] Synthesis of Ag@ZnO. HAgCl.sub.4 (1 mg (Ag)/mL, 4 mL) was added drop-wise to a methanolic solution of ZnO (0.33 g, 4.1 mmol) nanocrystals, followed by 5 mL of NaBH.sub.4 (40 mM) aqueous solution. The solution was stirred for 10 min. The solution color became black due to the formation of silver on ZnO nanoparticles. The resulting solution was centrifuged, filtered and dried in air to give Ag@ZnO.
[0057] Synthesis of Au/Pd@ZnO. A mixture of HAuCl.sub.4 (1.97 mg (Au)/mL, 0.76 mL) and PdCl2 (1.2 mg (Pd)/mL, 1.3 mL) was added drop-wise to a methanolic solution of ZnO (0.33 g, 4.1 mmol) nanocrystals, followed by 5 mL of NaBH.sub.4 (40 mM) aqueous solution. The solution was stirred for 10 min. The solution color became black due to the formation of PdAu on ZnO nanoparticles. The resulting solution was centrifuged, filtered and dried in air to give AuPD@ZnO.
[0058] Synthesis of Pt@ZnO. H.sub.2PtCl.sub.66H.sub.2O (1 mg (Pt)/mL, 12 mL or 0.1 mg (0.12 mL for 0.1 wt. %) was added drop-wise to a methanolic suspension of Zn (1 g, 12.3 mmol) nanocrystals, followed by 1.5 mL of NaBH.sub.4 (40 mM) aqueous solution. The solution was stirred for 10 min. The solution color became black due to the formation of platinum on ZnO nanoparticles. The resulting solution was centrifuged, filtered and dried in air to give Pt (1 wt %) @ ZnO2.
Example 3
Synthesis of ZnO.SUB.2.@M1@Cd.SUB.0.8.Zn.SUB.0.2.S Compounds
[0059] Zn/M1 (0.2 g, 2.5 mmol) nanoparticles of Example 2 were re-dispersed in 70 mL methanol and the temperature was raised to 60 C. In order to form Cd.sub.0.8Zn.sub.0.2S layer of the particles, zinc acetate (0.5 mmol) from zinc acetate stock solution (80 mM, 6.25 mL) was added to the dispersion and then the cadmium acetate (2 mmol) from (80 mM, 25 mL) stock solution and sodium sulfide (3 mmol) from (100 mM, 30 mL) methanolic stock solutions were added drop wise simultaneously while stirring the solution. Stirring was continued for 30 min more. Products were separated by centrifugation and washed with H.sub.2O/MeOH mixture and dried at 60 C. overnight to give the final product.
[0060] ZnO/Pt/Cd.sub.0.8Zn.sub.0.2S. ZnO/Pt (0.32 g, 4 mmol) nanoparticles were dispersed in 70 mL methanol and temperature was raised to 60 C. In order to form Cd.sub.0.8Zn.sub.0.2S layer on the particles, the required amount of zinc acetate (0.2 mmol) from zinc acetate stock solution (80 mM, 2.5 mL), the cadmium acetate (0.8 mmol) from (80 mM, 10 mL) stock solution were added to the suspension and stirred for 15 min at 60 C. then sodium sulfide (2 mmol) from (100 mM, 20 mL) methanolic stock solution was added dropwise. The resulting suspension was stirred for 1 h. The precipitates were separated by centrifugation, washed with H.sub.2O/MeOH (1:1) mixture and dried at 80 C. overnight to give the final product of [ZnO].sub.4/1 wt. % Pt/Cd.sub.0.8Zn.sub.0.2S (0.4 g, 88% in yield).
[0061] Pt/Cd.sub.0.8Zn.sub.0.2S. Zinc acetate (0.2 mmol) from zinc acetate stock solution (80 mM, 2.5 mL), the cadmium acetate (0.8 mmol) from (80 mM, 10 mL) stock solution were mixed and stirred for 15 min at 60 C. then sodium sulfide (2 mmol) from (100 mM, 20 mL) methanolic stock solution was added dropwise. The resulting suspension was stirred for 1 h. The precipitates were separated by centrifugation, washed with H.sub.2O/MeOH (1:1) mixture, and dried at 60 C. overnight to give the final product of Cd.sub.0.8Zn.sub.0.2S in quantitative yield. Photo deposition of Pt on Cd.sub.0.8Zn.sub.0.2S was carried out by mixing of Cd.sub.0.8Zn.sub.0.2S (100 mg) with 1 mL stock solution of H4PtCl.sub.6 (1 mg/mL (Pt)) in BnOH/AcOH (2.5-2.5 v/v %). The resulting mixture was illuminated under UV (=360 nm) light with a light intensity of 5 mW/cm.sup.2 for 4 h. The resulting solution was filtered, washed with water, and dried at 80 C. overnight to obtain the desired product 1 wt. % Pt/Cd.sub.0.8Zn.sub.0.2S in quantitative yield.
Example 4
Characterization
[0062] UV-vis absorption spectra of the powdered catalysts were collected over the wavelength range of 250-700 nm on a Thermo Fisher Scientific (USA) spectrophotometer equipped with praying mantis diffuse reflectance accessory. Absorbance (A) and reflectance (% R) of the samples were measured. The reflectance (% R) data were used to calculate the band gap of the samples using the Tauc plot (Kubelka-Munk function). XRD spectra were recorded using a Bruker D8 Advance X-ray diffractometer Cu K (=1.5406 {acute over ()} ) radiationover the range of 2 interval between 20 and 90 with a step size of 0.010 and a step time of 0.2 s/step were used. The XP spectra of the samples were collected by a Thermo Scientific Escalab 250 XI XP spectrometer with Al K X-ray source. The X-ray spot size was 650 m.sup.2. The charge compensation was carried out using a standard flood gun. Before collecting XPS data, samples were etched using Ar ions for 5 min at ion energy of 1000 eV. The data was acquired using the following settings listed in Table 2 before and after etching. All the peaks were corrected respect to the binding energy of adventitious C1s peak at 284.5 eV. All peaks were fitted using SMART background option and Lorentzian/Gaussian.
TABLE-US-00002 TABLE 2 # of Scan PE (eV) Dwell Time (ms) Step Size (eV) scans Survey 100 100 1 1 High Resolution 30 100 0.1 10-30
[0063] The concentrations of Zn, Cd, S and Pt were measured by ICP-OES on a Varian 720-ES instrument. TEM samples were dispersed in alcohol and a drop of the suspension was placed over a grid with holey-carbon film. The TEM images were collected using a FEI Tecnai F20 microscope operating at 200 kV.
[0064] XRD analysis. XRD patterns of various compositions are depicted in
[0065] UV-Vis analysis.
[0066] TEM Analysis.
TABLE-US-00003 TABLE 3 O1s O1s O1s Samples Cd3d.sub.5/2 Zn2p.sub.3/2 S2p.sub.3/2 Pt4f.sub.7/2 (ZnO) (OH) (H.sub.2O) 0.1% Pt/Cd.sub.0.8Zn.sub.0.2S 404.8 1022.1 161.1 72.0 531.3 532.9 1% Pt/Cd.sub.0.8Zn.sub.0.2S 404.8 1022.1 161.1 71.9 531.6 533.0 [ZnO].sub.4/0.1% Pt/Cd.sub.0.8Zn.sub.0.2S 404.7 1022.0 161.0 530.0 531.5 [ZnO].sub.4/1% Pt/Cd.sub.0.8Zn.sub.0.2S 404.8 1022.4 161.2 530.3 531.7
[0067] The range of binding energies of Zn 2p.sub.3/2 of all the Pt/CdZnS samples are between 1022.20.2 eV and were close to each other, which are similar to that of reported for ZnO.sup.17 and ZnS.sup.18 (
Example 5
Photocatalytic Tests
[0068] Photocatalytic reactions were performed in a 137-mL-volume Pyrex glass reactor using 6-30 mg of catalyst. 30 mL of various volume ratios of benzyl alcohol/acidic acid (BnOH/AcOH) aqueous solutions were used. The slurry was purged with N.sub.2 gas to remove any O.sub.2 and subjected to constant stirring before the reaction. The reactor was then exposed to UV light (100 Watt ultraviolet lamp H-144GC-100 Sylvania par 38 with a flux of 5 mW cm.sup.2 at a distance of 5 cm). Similarly, to evaluate the UV+visible light activity a Xenon lamp (Asahi spectra MAX-303) with a total flux of 42.5 mW cm.sup.2 (UV.Math.3.0 mW cm.sup.2 and visible (up to 650 nm) at a distance of 2 cm was used. Product analyses were performed by a gas chromatograph (GC) equipped with thermal conductivity detector (TCD) connected to Porapak Q packed column (2 m) at 45 C. and N.sub.2 was used as a carrier gas. Apparent quantum yield (AQY) at various wavelengths defined by equation (1) were calculated by data obtained using monochromatic LED (365 nm to 750 nm) at the distance of 2 cm. The corresponding light intensities were measured with a GL Spectics 5.0 Touch.
[0069]
TABLE-US-00004 TABLE 4 Apparent Apparent Wave- quantum Wave- quantum length yield length yield Catalysts (nm) (AQY %) (nm) (AQY %) CdZnS 365 3 460 9 0.1% Pt/CdZnS 365 20 460 16 1% Pt/CdZnS 365 14 460 10 [ZnO].sub.4/0.1% Pt/CdZnS 365 11 460 10 [ZnO].sub.4/1% Pt/CdZnS 365 34 460 16
[0070] The maximum hydrogen rate of [ZnO].sub.4/1% Pt/Cd.sub.0.8Zn.sub.0.2S was obtained with 33 mg of catalyst in 30 mL of sacrificial reagent (33 mg cat/30 mL sac.), which contained 10 mg of Cd.sub.0.8Zn.sub.0.2S and 23 mg of ZnO, respectively. From the data, it was determined that when the catalysts were illuminated at 365 nm, where both ZnO and Cd.sub.0.8Zn.sub.0.2S were activated at the same time, the AQY of [ZnO].sub.4/1% Pt/Cd.sub.0.8Zn.sub.0.2S (33 mg/30 mL) was over two times higher than that of 1% Pt/Cd.sub.0.8Zn.sub.0.2S (10 mg/30 mL), while 1% Pt/ZnO did not produce any hydrogen. Therefore, it was concluded that the [ZnO].sub.4/1% Pt/Cd.sub.0.8Zn.sub.0.2S hybrid system followed a Z-scheme mechanism at 365 nm as shown in
[0071] A proposed charge transfer mechanisms for the photocatalysts of the present invention are shown in
[0072] The steps are believed to be (1) charge generation in ZnO and Cd.sub.0.8Zn.sub.0.2S, (2) charge recombination on Pt, (3) oxidation of sacrificial reagent on the VB of ZnO and (4) hydrogen generation on CB of Cd.sub.0.8Zn.sub.0.2S. This process only happens when both semiconductors are activated at the same time. On the other hand, simple charge transfer happens when only Cd.sub.0.8Zn.sub.0.2S is excited as shown in
[0073] Femtosecond transient absorption (TA) analysis. To further validate the proposed mechanism, femtosecond transient absorption (TA) measurements were performed on ZnO, ZnO/Pt, Cd.sub.0.8Zn.sub.0.2S, Cd.sub.0.8Zn.sub.0.2S/Pt, and ZnO/Pt/Cd.sub.0.8Zn.sub.0.2S. Time-resolved absorption decays were measured with a pump-probe setup, in which a white light continuum probe pulse was generated in a 2 mm thick sapphire plate contained in an Ultrafast System LLC spectrometer using few microjoules energy of 800-nm pulse. The fundamental output delivered by a Ti:sapphire femtosecond regenerative amplifier operating at 800 nm with 35 fs pulses and a repetition rate of 1 kHz. Spectrally tunable (240-2600 nm) femtosecond pulses generated by an Optical Parametric Amplifier (Light Conversion LTD) and a white light continuum were used, respectively, as the pump (excitation) and probe beams in a pump-probe experimental setup (Helios).
[0074]
[0075] Although TB signals at 470 nm and 610 nm of Cd.sub.0.8Zn.sub.0.2S were stronger, overlapping signals with that of ZnO/Pt around same region made it difficult to analyze (
TABLE-US-00005 TABLE 5 System (, nm) .sub.1 (ps) .sub.2 (ps) ZnO (365 nm) 34.9 3.3 (63%) 634.2 90.6 (37%) PtZnO (392 nm) 0.2 0.05 (40%) 19.1 2 (60%) ZnO/Pt/CdZnS (392 nm) 0.118 0.05 (73%) 2.5 0.1 (27%) Pt/ZnO (538 nm) 1 0.06 (32%) 202.6 28.3 (68%) ZnO/Pt/CdZnS (538 nm) 1 0.07 (33%) 201 25.8 (67%)