EP1723267A2 - Photoelectrochemical reaction cell - Google Patents
Photoelectrochemical reaction cellInfo
- Publication number
- EP1723267A2 EP1723267A2 EP05700999A EP05700999A EP1723267A2 EP 1723267 A2 EP1723267 A2 EP 1723267A2 EP 05700999 A EP05700999 A EP 05700999A EP 05700999 A EP05700999 A EP 05700999A EP 1723267 A2 EP1723267 A2 EP 1723267A2
- Authority
- EP
- European Patent Office
- Prior art keywords
- reaction cell
- electrode
- electrodes
- cell according
- reaction
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Withdrawn
Links
- 238000006243 chemical reaction Methods 0.000 title claims abstract description 129
- 239000003792 electrolyte Substances 0.000 claims abstract description 56
- 239000007789 gas Substances 0.000 claims abstract description 54
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims abstract description 42
- 229910052739 hydrogen Inorganic materials 0.000 claims abstract description 25
- 229910052751 metal Inorganic materials 0.000 claims abstract description 21
- 239000002184 metal Substances 0.000 claims abstract description 21
- 238000004519 manufacturing process Methods 0.000 claims abstract description 10
- 239000004065 semiconductor Substances 0.000 claims description 64
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 33
- 239000000446 fuel Substances 0.000 claims description 29
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 claims description 27
- 239000000463 material Substances 0.000 claims description 20
- 239000013078 crystal Substances 0.000 claims description 15
- 229910052697 platinum Inorganic materials 0.000 claims description 14
- 229910052802 copper Inorganic materials 0.000 claims description 6
- 239000012780 transparent material Substances 0.000 claims description 6
- VVQNEPGJFQJSBK-UHFFFAOYSA-N Methyl methacrylate Chemical compound COC(=O)C(C)=C VVQNEPGJFQJSBK-UHFFFAOYSA-N 0.000 claims description 5
- 229920005372 Plexiglas® Polymers 0.000 claims description 5
- 229910001218 Gallium arsenide Inorganic materials 0.000 claims description 4
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 4
- 229910052782 aluminium Inorganic materials 0.000 claims description 4
- 229910052737 gold Inorganic materials 0.000 claims description 4
- 229910052759 nickel Inorganic materials 0.000 claims description 4
- 239000005388 borosilicate glass Substances 0.000 claims description 3
- 229910052594 sapphire Inorganic materials 0.000 claims description 3
- 239000010980 sapphire Substances 0.000 claims description 3
- SBIBMFFZSBJNJF-UHFFFAOYSA-N selenium;zinc Chemical compound [Se]=[Zn] SBIBMFFZSBJNJF-UHFFFAOYSA-N 0.000 claims description 3
- 230000002528 anti-freeze Effects 0.000 claims description 2
- UHYPYGJEEGLRJD-UHFFFAOYSA-N cadmium(2+);selenium(2-) Chemical compound [Se-2].[Cd+2] UHYPYGJEEGLRJD-UHFFFAOYSA-N 0.000 claims description 2
- 229910052804 chromium Inorganic materials 0.000 claims description 2
- 229910052741 iridium Inorganic materials 0.000 claims description 2
- 230000001678 irradiating effect Effects 0.000 claims description 2
- 229910052763 palladium Inorganic materials 0.000 claims description 2
- 229910052703 rhodium Inorganic materials 0.000 claims description 2
- 229910052707 ruthenium Inorganic materials 0.000 claims description 2
- 238000011144 upstream manufacturing Methods 0.000 claims description 2
- 239000004020 conductor Substances 0.000 abstract description 2
- 239000001257 hydrogen Substances 0.000 description 20
- OGIDPMRJRNCKJF-UHFFFAOYSA-N titanium oxide Inorganic materials [Ti]=O OGIDPMRJRNCKJF-UHFFFAOYSA-N 0.000 description 17
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 14
- 229910001882 dioxygen Inorganic materials 0.000 description 14
- 230000005855 radiation Effects 0.000 description 13
- 239000001301 oxygen Substances 0.000 description 12
- 229910052760 oxygen Inorganic materials 0.000 description 12
- 239000012528 membrane Substances 0.000 description 11
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 10
- -1 hydrogen ions Chemical class 0.000 description 10
- 230000005684 electric field Effects 0.000 description 6
- 238000000034 method Methods 0.000 description 6
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 5
- 229910010413 TiO 2 Inorganic materials 0.000 description 5
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 5
- 230000015572 biosynthetic process Effects 0.000 description 5
- 239000002800 charge carrier Substances 0.000 description 5
- 230000008901 benefit Effects 0.000 description 4
- 238000010276 construction Methods 0.000 description 4
- 239000010949 copper Substances 0.000 description 4
- 239000007788 liquid Substances 0.000 description 4
- 238000007254 oxidation reaction Methods 0.000 description 4
- 230000008569 process Effects 0.000 description 4
- 238000006722 reduction reaction Methods 0.000 description 4
- 230000003595 spectral effect Effects 0.000 description 4
- 230000032258 transport Effects 0.000 description 4
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 3
- 238000011109 contamination Methods 0.000 description 3
- 238000005868 electrolysis reaction Methods 0.000 description 3
- 239000010931 gold Substances 0.000 description 3
- 238000002156 mixing Methods 0.000 description 3
- 238000000926 separation method Methods 0.000 description 3
- 229910001369 Brass Inorganic materials 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 2
- 239000010951 brass Substances 0.000 description 2
- 238000000354 decomposition reaction Methods 0.000 description 2
- 230000007547 defect Effects 0.000 description 2
- 239000012153 distilled water Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000001704 evaporation Methods 0.000 description 2
- 230000008014 freezing Effects 0.000 description 2
- 238000007710 freezing Methods 0.000 description 2
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 description 2
- 150000002500 ions Chemical class 0.000 description 2
- 238000011031 large-scale manufacturing process Methods 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 230000003647 oxidation Effects 0.000 description 2
- 229920003023 plastic Polymers 0.000 description 2
- 239000004033 plastic Substances 0.000 description 2
- 230000009467 reduction Effects 0.000 description 2
- 229910001220 stainless steel Inorganic materials 0.000 description 2
- 239000010935 stainless steel Substances 0.000 description 2
- 238000001429 visible spectrum Methods 0.000 description 2
- 108010053481 Antifreeze Proteins Proteins 0.000 description 1
- 229910001252 Pd alloy Inorganic materials 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 239000003929 acidic solution Substances 0.000 description 1
- 230000003667 anti-reflective effect Effects 0.000 description 1
- 238000005452 bending Methods 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 239000011651 chromium Substances 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000010494 dissociation reaction Methods 0.000 description 1
- 230000005593 dissociations Effects 0.000 description 1
- 230000005518 electrochemistry Effects 0.000 description 1
- 239000007772 electrode material Substances 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000002803 fossil fuel Substances 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 238000005342 ion exchange Methods 0.000 description 1
- 230000037427 ion transport Effects 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 230000005012 migration Effects 0.000 description 1
- 238000013508 migration Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000003345 natural gas Substances 0.000 description 1
- 230000007935 neutral effect Effects 0.000 description 1
- 229910000510 noble metal Inorganic materials 0.000 description 1
- KDLHZDBZIXYQEI-UHFFFAOYSA-N palladium Substances [Pd] KDLHZDBZIXYQEI-UHFFFAOYSA-N 0.000 description 1
- 238000006303 photolysis reaction Methods 0.000 description 1
- 230000015843 photosynthesis, light reaction Effects 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 238000005215 recombination Methods 0.000 description 1
- 230000006798 recombination Effects 0.000 description 1
- 238000006479 redox reaction Methods 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 238000001228 spectrum Methods 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 229910052715 tantalum Inorganic materials 0.000 description 1
- 230000008646 thermal stress Effects 0.000 description 1
- 239000004408 titanium dioxide Substances 0.000 description 1
- 229910052721 tungsten Inorganic materials 0.000 description 1
- 238000007740 vapor deposition Methods 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- 239000012463 white pigment Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
- C25B1/00—Electrolytic production of inorganic compounds or non-metals
- C25B1/50—Processes
- C25B1/55—Photoelectrolysis
-
- Y—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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/36—Hydrogen production from non-carbon containing sources, e.g. by water electrolysis
-
- Y—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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
- Y02P20/133—Renewable energy sources, e.g. sunlight
Definitions
- the invention relates to a reaction cell for the photoelectrochemical production of hydrogen gas with a housing filled with an aqueous electrolyte, with a pair of electrodes consisting of a first electrode immersed in the electrolyte made of a doped semiconductor and an immersed in the electrolyte and electrically conductively connected to the first electrode second electrode made of a metal, and with a light source irradiating the pair of electrodes.
- Hydrogen is considered to be the energy source of the future due to its ecological advantages - only water vapor is produced during combustion.
- Another option for hydrogen production is the separation of the hydrogen gas components, some of which are highly concentrated, in the exhaust gases from refineries, industrial furnaces or chemical plants.
- a highly efficient way of producing hydrogen gas can be seen in water electrolysis, ie in the splitting of the water molecules into hydrogen and oxygen gas by means of an electrical current conducted through the water.
- An economical large-scale implementation of the electrolysis of water using sunlight has so far failed due to the low efficiency of available solar cells. The objective is therefore to develop reaction cells that can be used to produce hydrogen gas directly from an aqueous electrolyte by using the radiation energy from sunlight.
- Reaction cells of the type mentioned at the outset are known at least in terms of their basic structure from the scientific literature.
- An electrochemical cell is described in the article "Electrochemical Photolysis of Water at a Semiconductor Electrode” (Nature Vol. 238, July 7, 1972), which consists of two individual containers connected by a line, each of which is filled with water as the electrolyte , In the first container, an electrode consisting of a semiconductor in the form of an n-doped TiO 2 crystal is immersed in the electrolyte. This electrode is electrically connected to a platinum electrode located in the second container via an external load resistor.
- the ion concentration between the two containers is equalized via the line connecting the containers, which is provided with an ion-permeable membrane in order to prevent liquid exchange between the containers.
- each include a container, for example a glass tube, which consists of a plurality of plate-shaped pairs of electrodes which are in contact with one another, each consisting of a doped semiconductor electrode (for example n-Ti0 2 , n-Pb 3 0 4 or n-CdSe) and a counter-electrode made of platinum, Lead, CoS or another material that is divided into individual chambers.
- a container for example a glass tube, which consists of a plurality of plate-shaped pairs of electrodes which are in contact with one another, each consisting of a doped semiconductor electrode (for example n-Ti0 2 , n-Pb 3 0 4 or n-CdSe) and a counter-electrode made of platinum, Lead, CoS or another material that is divided into individual chambers.
- the electrode pairs themselves are arranged in the container in the manner of bulkheads, so that no liquid or gas exchange is possible between the individual chambers.
- the surfaces of the semiconductor electrode face each
- the chambers are filled with differently composed aqueous electrolytes.
- the two outer chambers are connected to each other via a salt bridge to form a closed circuit. During operation, only a charge carrier transport takes place through the respective electrolyte in the individual chambers, while in the two outermost chambers oxygen gas is formed on one side in an oxidation reaction and on the other side of the cell in a reduction reaction hydrogen gas.
- a disadvantage of the cell described above is primarily its complicated structure and the fact that different electrolytes are used in the different chambers, which increases the operating effort. In addition, they are purely laboratory structures whose usability on a large scale is questionable.
- the invention is accordingly based on the object of creating a reaction cell of the type mentioned at the outset which enables the production of hydrogen gas in a photoelectrochemical reaction in a reliable and reproducible manner and is distinguished by a particularly simple structure which is suitable for industrial series production.
- KN / be 031037 O The object is achieved in a reaction cell according to the preamble of claim 1 in that the electrodes are in surface contact with one another, in that the pair of electrodes divides the reaction cell into two chambers, the chambers being connected to one another in an ion-conducting manner, and in that the housing has at least one gas outlet opening.
- the reaction cell constructed according to the invention can be used to produce hydrogen gas from an aqueous electrolyte in continuous operation.
- the decisive reason for the reliable course of the photoelectrochemical reaction lies in the direct contacting of the two electrodes without the interposition of an electrical conductor, for example a copper wire or a load resistor, as in the case of the prior art.
- the decisive factor is that in the case of a metallic second electrode , an ohmic contact is formed between the semiconductor electrode and the metal electrode, which enables free charge carrier exchange between the two electrodes.
- a second electrode consisting of a semiconductor doped in the opposite direction to the first electrode a pn junction is formed at the boundary layer between the electrodes.
- the reaction cell is characterized by a particularly simple construction, which requires only a few very simply constructed and robust components and is also suitable for low-maintenance continuous use for the large-scale production of hydrogen gas.
- the arrangement of the pair of electrodes allows the partial reactions to take place spatially separated from one another, so that mixing of the resulting gases during their production and thus contamination of the hydrogen gas produced is avoided.
- an unhindered ion transport through the electrolyte can take place.
- the two chambers are connected to one another in a liquid-conducting manner. It is also possible to implement the ion-conducting connection between the two chambers by means of an ion-permeable membrane.
- the pair of electrodes can also be arranged relative to the light source in such a way that the metallic second electrode is irradiated and — assuming a sufficiently small thickness of the second electrode — largely transmits the radiation.
- the radiation penetrates through the contacted surface of the first electrode (semiconductor), where it is then absorbed to form electron-hole pairs.
- a two-dimensional contacting of the two electrodes can in principle be achieved by pressing, screwing or by another common method for the two-dimensional connection of two surfaces.
- Flat contacting can, however, be achieved particularly well if the second electrode, in the case of a metallic electrode material, is evaporated onto one side of the first electrode.
- this also has the advantage that the material used for the second electrode can be used particularly economically, which contributes to a reduction in the production costs of the reaction cell.
- An extremely thin metal layer can be produced on the first electrode by vapor deposition of the metal of the second electrode, which is particularly advantageous if the second electrode is irradiated by the light source, since it is important that a large part of the radiation in the underlying semiconductor electrode is conducted.
- the first electrode semiconductor
- the second electrode metal or semiconductor
- the two electrodes themselves can be shaped in different ways. It proves to be particularly expedient if the electrodes are each flat, in particular plate-shaped, with a front and a back, the front of the first electrode being irradiated by the light source and the back of the first electrode making contact with the front of the second electrode is.
- any light source which emits light quanta with a photon energy which supply the photo voltage (eg water: 1.23 V) required for the decomposition of the electrolyte, is suitable as the light source.
- the photon energy must be matched to the bandgap of the semiconductor material used.
- the light source can be arranged outside the reaction cell, but can also be located inside the cell. In order to enable particularly economical and environmentally friendly operation of the reaction cell, sunlight is preferably used as the light source.
- an external light source can radiate into the cell from above onto the surface of the first electrode.
- the light irradiation through the housing wall is particularly advantageous.
- this is either made of a light-transparent material, for example plexiglass, or of an opaque material and in this case has a window for light irradiation.
- Suitable housing materials are, for example, stainless steel or various plastics. In addition, metals such as copper, aluminum, gold, brass or nickel are also suitable.
- the housing material chosen should not be permeable to the gas produced, in particular the hydrogen gas. Likewise, he should not be able to store the gas.
- the window should also happen UV components of the incident light absorption-free as possible, as large by UV photon electron-hole pairs in semiconductors with particularly
- the window should therefore be made of a UV-transparent material, for which quartz glass, plexiglass, ZnSe, ZnS, borosilicate glass, MgF 2 or sapphire are particularly suitable.
- housing geometry can also be designed to be very variable. Cuboid geometries are suitable, for example.
- Reaction cells whose housing is closed on all sides except for at least one gas outlet opening have proven particularly robust.
- the gas produced during the photoelectrochemical reaction taking place in the cell can easily be removed through the gas outlet opening.
- the gas outlet opening can expediently be closed gas-tight by a valve. This enables, for example, easy transport of the reaction cell without the risk of contamination of the electrolyte.
- KN / be 031037WO Hydrogen-permeable membrane can be arranged. This can consist in particular of a metal layer which allows hydrogen molecules to pass through while other gas molecules are retained. Membranes made of palladium alloys are particularly suitable for this.
- Another structurally simple possibility of completely separating the gases formed on the two electrode surfaces is that the two chambers formed by the pair of electrodes in the cell each have a gas outlet opening through which the gases can be discharged separately from one another.
- the reaction cell has a heat exchanger.
- heat of reaction can be removed by means of a heat exchanger.
- the heat exchanger should be installed on the side away from the light in the reaction cell.
- the aqueous electrolyte used in each case can be composed differently.
- the reaction cell can also be operated with water as the electrolyte without any problems and permanently, hydrogen and oxygen gas being produced.
- water to produce a particularly pure gas, it should be distilled water (aqua bidest). Also conceivable
- electrolytes for example aqueous acidic solutions
- hydrogen also other gases can be produced instead of oxygen.
- the position of the element in question in the electrochemical series is decisive.
- an anti-freeze can also be added to prevent freezing at low temperatures, similar to the use of a heat exchanger.
- the first electrode of the reaction cell consists of a doped semiconductor.
- the first electrode can consist of a semiconductor from the group Ti0 2 , SrTi0 3 , Ge, Si, Cu 2 S, GaAs, CdS, MoS 2 , CdSeS, Pb 3 0 4 or CdSe.
- Titanium dioxide which is produced in large quantities at low cost, for example for use as a white pigment, has proven particularly suitable.
- the Ti0 2 can be used in various modifications as a semiconductor electrode in the reaction cell. Ultrathin Ti0 2 layers, Ti0 2 films, polycrystalline Ti0 2 , sintered Ti0 2 powder and special Ti0 2 crystal structures such as rutile, anatase or brookite are conceivable.
- the doping of the semiconductor causes, inter alia, that above the valence band or below the conduction band in the
- KN / be 031037 O forbidden zone (energy gap, band gap), further states that can be occupied by charge carriers are formed, so that there is a practically reduced band gap in the semiconductor.
- This can be used to the effect that even with semiconductors with a large band gap, such as Ti0 2 (band gap 3.1 eV, this corresponds to a cut-off wavelength of approx. 400 nm), low-energy components of the visible spectrum can also be used. Both n-doping and p-doping can be considered.
- an electrical field forms at the interface with the electrolyte in the semiconductor, which causes the electron-hole pairs formed in the semiconductor surface upon irradiation to be separated in such a way that the negatively charged electrons enter the interior of the semiconductor and continue to flow into the surface-contacted second electrode, while the positively charged holes or defect electrons remaining on the surface oxidize the electrolyte.
- hydrogen gas is formed on the surface of the second electrode by reducing the electrolyte.
- the irradiated surface of this electrode is advantageously designed as a (110) or (100) crystal surface. This promotes dissociation
- Another way of expanding the usable light spectrum is to adsorb platinum atoms, preferably in the form of clusters, on the surface of the first electrode, as a result of which interface states, i.e. Additional permitted energy states arise within the forbidden zone of the respective semiconductor, which expand the usable wavelength range to low-energy light. It goes without saying that the surface of the first electrode must not be completely coated with platinum, since this would result in a metal-semiconductor-metal system which cannot be used for a photoelectrochemical reaction.
- the second electrode which is in contact with the surface of the first electrode, is made of a metal or one opposite
- KN / be 031037 O first electrode oppositely doped semiconductor In the case of a semiconductor, the above-mentioned semiconductor materials are also suitable. A pn junction is formed between the two semiconductor electrodes. If a metal is used, it must form an ohmic contact when making contact with the semiconductor material of the first electrode. When selecting a suitable metal, it must also be taken into account that this does not react with the reaction products or the electrolyte, for example, so that it forms no or only with difficulty oxides.
- the elements Ru, Rh, Pd, Ag, Os, Ir, Pt, Au, Al, Cr, Cu, Ni, Mo, Pb, Ta and W. are therefore particularly suitable, as already mentioned, a particularly advantageous method of contacting of the two electrodes consists of evaporating the metallic second electrode onto the first one, the noble metal can be used accordingly sparingly and therefore relatively inexpensively.
- a plurality of electrode pairs are provided in the reaction cell, the respective first electrodes of the electrode pairs being made of different semiconductor materials.
- the semiconductor materials should be selected with respect to their respective bandgap such that they absorb in different spectral ranges, so that the widest possible wavelength range of the light source, in particular sunlight, is used to form electron-hole pairs and thus to initiate the reduction and oxidation reactions can be.
- three pairs of electrodes can be provided, the first electrode in each case in the first pair of electrodes made of TiO 2 ,
- the second pair of electrodes is made of SrTi0 3 and the third is made of GaAs and the second electrodes are made of evaporated platinum.
- the electrode pairs are arranged one behind the other in the direction of incidence of the light, the first and the second electrodes of the electrode pairs in each case being opposite one another, which means that, in the case of at least one pair of electrodes, the second electrode faces the light source.
- the respective metal electrodes in particular are to be made sufficiently thin to prevent excessive absorption of the radiation in the metal. This can easily be achieved by evaporating an extremely thin metal layer on the respective semiconductor electrodes.
- the first and the second electrodes of the electrode pairs each face each other, only one type of gas is produced in each of the individual chambers formed by the electrode pairs.
- the first electrode of the pairs of electrodes arranged one behind the other in the direction of radiation should be one in relation to the first electrode of the pair of electrodes arranged upstream in the radiation direction
- KN / be 031037 O have a smaller band gap.
- the first electrode (second pair of electrodes) following in the direction of radiation which has a smaller band gap, absorbs photons of lower energy as well as the high-energy photons which were transmitted through the first electrode of the first pair of electrodes.
- the subsequent first electrode (third electrode pair) which in turn has a smaller band gap, photons with in turn lower photon energy are absorbed as well as all higher-energy photons that penetrate into this electrode. This continues up to the first electrode of the last pair of electrodes in the direction of irradiation, whereby an optimal utilization of the energy of the irradiated light is achieved.
- a device for converting light energy into electrical energy with a reaction cell according to one of claims 1 to 27 in that an anode-cathode- in the reaction cell or in another cell connected to the reaction cell via at least one gas line. Arrangement is provided, the anode and the cathode via an outer
- KN / be 031037 O Circuit to which an electrical consumer can be connected are conductively connected to one another and the anode and the cathode are arranged such that they are flushed by the gases produced on the first and second electrodes of the pair of electrodes.
- hydrogen gas is initially generated in the manner described above on the electrodes of the pair of electrodes and, for example, oxygen gas is also generated when water is used as the electrolyte.
- an additional anode-cathode arrangement is provided in the device, which is arranged such that the anode and cathode are flushed by the gases.
- the anode-cathode arrangement can be arranged in the reaction cell.
- the gases washing around them are then reduced or oxidized in the redox reactions reversed to the reactions taking place in the reaction cell, the charge carriers obtained in the oxidation flowing to the counterelectrode via the external circuit connecting the cathode to the anode.
- An electrical consumer can be connected to this circuit and is thus supplied with electrical energy.
- the ions generated by the oxidation or reduction reaction react with one another to form molecules of the electrolyte located in the reaction cell. Is considered
- the cathode-anode arrangement is designed as a fuel cell.
- the two electrodes are connected to one another by an exchange membrane through which the hydrogen ions which are generated at the anode can migrate to the cathode. There they can react to water with negatively charged oxygen ions, for example.
- charge equalization takes place via the external circuit.
- the particular advantage of the fuel cell is that it can be easily integrated into the reaction cell, it should preferably be arranged above the pair of electrodes, so that the gases formed on the surfaces of the electrodes of the pair of electrodes wash them particularly intensively.
- the use of a low-temperature fuel cell which has a working temperature of 80 ° C., is also particularly advantageous for the use of the fuel cell in the reaction cell. As a result, the reaction cell is not subjected to excessive thermal stress.
- a plurality of electrode pairs and a plurality of fuel cells are arranged next to one another in an alternating sequence in the reaction cell, an external consumer being connectable to the respective external circuit of the fuel cells.
- the anode-cathode arrangement is arranged in a further cell and is designed as a galvanic cell.
- the anode and the cathode which preferably consist of platinum, are washed around separately by the gases emerging from the reaction cell, for example hydrogen and oxygen gas.
- the gases from the reaction cell are passed via a common line into the further cell, where they are separated on a membrane in the manner described above.
- the gases are preferably passed separately into the further cell via two lines, so that subsequent separation can be omitted.
- Both electrodes, anode and cathode are immersed in an electrolyte, for example dilute sulfuric acid. Hydrogen gas is oxidized to hydrogen ions at the anode.
- FIG. 2 shows the reaction cell of FIG. 1 in an embodiment modified from FIG. 1 with three pairs of electrodes in a side sectional view
- Fig. 3 shows the reaction cell of Fig. 1 in a construction example in front view
- FIG. 4 shows a side sectional view of the reaction cell of FIG. 3 along the line IV-IV of FIG. 3,
- Fig. 5 shows the reaction cell of Fig. 1 with an integrated fuel cell
- FIG. 6 shows the reaction cell of FIG. 5 in an embodiment modified from FIG. 1 with three pairs of electrodes and three fuel cells in a side sectional view.
- 1 has a housing 1 which is closed on all sides and has two gas outlet openings 1a, 1b
- the irradiation window consists of a UV-transparent material, for example quartz glass, which advantageously also has an anti-reflective layer.
- the light L from an external light source, preferably sunlight, can enter the housing through the incident window 2.
- the housing 1 is filled with an aqueous electrolyte 3, in the present case distilled water (aqua bidest).
- the first electrode 4 consists of an n-doped plate-shaped Ti0 2 crystal
- the second electrode 5 consists of a platinum layer which is vapor-deposited onto the Ti0 2 crystal on one side, so that there is a flat contact between the two electrodes 4, 5 consists.
- the pair of electrodes is arranged in the reaction cell 1 such that the non-vaporized surface 4a of the first electrode is irradiated by the light L incident in the reaction cell 1 and the cell is divided into two chambers A, B which are connected to one another in a liquid-conducting manner.
- Surface 4a of the first electrode 4 now irradiated with light electron-hole pairs are formed in the entire semiconductor crystal of the first electrode. While almost all of the crystal disappears through recombination, the electrons are separated from the holes in the area of boundary layer I, where the electric field acts.
- the electrons pass through the boundary layer II between the first and second electrodes and reduce the hydrogen ions (protons) to hydrogen gas at the boundary layer III of the second electrode 5 to the electrolyte 3:
- the hydrogen ions which combine with neutral water molecules to form positively charged oxonium ions H 3 0 + , have to migrate through the electrolyte 3 from the boundary layer I to the boundary layer III, which is easily possible due to the liquid-conducting connection between the chambers A, B.
- the gases formed in the photoelectrochemical reaction, hydrogen and oxygen, can then escape separately from the reaction cell via the gas outlet openings 1a, 1b and are stored in gas stores (not shown)
- mixing of the gases is excluded.
- reaction cell with a pair of electrodes, the first electrode of which consists of an n-doped semiconductor and the second electrode of which is made of a p-doped semiconductor.
- An electric field is formed at each of the boundary layers of electrolyte-n-semiconductor, pn-layer and p-semiconductor-electrolyte, which leads to a step-like band bending over the entire width of the pair of electrodes.
- electron-hole pairs formed by the incident radiation can be separated in the manner described above, the electrons migrating to the surface of the second electrode and the holes to the surface of the first electrode.
- the reaction cell shown in FIG. 2 likewise has a housing 1 which is closed on all sides and a side radiation window 2 and is filled with water as the electrolyte 3.
- the cell in FIG. 2 has three pairs of electrodes 6, 7, 8, the first electrodes 9, 10, 11 of the three pairs of electrodes 6, 7, 8 being made of different semiconductor materials, namely n Ti0 2 , n-SrTi0 3 and n-GaAs exist.
- the second electrodes 12, 13, 14 of the electrode pairs 6, 7, 8 each consist of a thin platinum layer that is vapor-deposited onto the first electrode 9, 10, 11.
- the electrode pairs 6, 7, 8 divide the reaction cell into a total of four chambers C, D, E, F, which are connected to one another in a liquid-conducting manner, each chamber having a gas outlet opening lc, ld, le, lf
- electrode pairs 6, 7, 8 are arranged one behind the other in the direction of incidence of the light, the first and second electrodes of the electrode pairs 6, 7, 8 each being opposite one another.
- the middle pair of electrodes 7 is arranged mirror-inverted with respect to the outer pairs of electrodes 6, 8.
- the same electrochemical processes take place on the three electrode pairs 6, 7, 8 as in the case of the electrode pair of the reaction cell of FIG. at the respective first electrodes 9, 10, 11 the oxygen contained in the water molecules is oxidized to oxygen gas, while hydrogen gas is formed at the respective second electrodes 12, 13, 14.
- the layer thicknesses of the electrodes of the first and second pair of electrodes 6, 7 must be chosen to be sufficiently small so that the light radiated into the cell partially penetrates the cell and is finally completely absorbed in the third pair of electrodes 8.
- the particular advantage of the reaction cell shown in FIG. 2 is that due to the different bandgaps of the semiconductor materials of the first electrodes 9, 10, 11 of the electrode pairs 6, 7, 8, the light radiated into the cell in each electrode pair only in a certain one Spectral range is absorbed and converted into reaction energy, so that in total a very wide spectral range is used for the photoelectrochemical reaction and thus the reaction cell with a significantly higher efficiency than
- KN / be 031037 O a cell equipped with only one pair of electrodes can work.
- the construction example of the reaction cell according to the invention shown in FIGS. 3 and 4 has a substantially cuboid housing 15, which is made of an opaque material, preferably aluminum, stainless steel, nickel, brass, copper or gold.
- the housing 15 comprises an approximately cubic inner reaction space which is open on one side to the outside. This opening is tightly closed by an irradiation window 16.
- the window is transparent for visible light and especially for UV radiation. It is therefore preferably made of quartz glass, plexiglass, ZnSe, ZnS, borosilicate glass, MgF 2 and sapphire.
- a pair of electrodes is held in a holding arm 15g which extends vertically downward from the top of this space, the pair of electrodes being surrounded by an insulating layer, not shown, which prevents electrical contact between the electrodes 17, 18 and the holding arm 15g.
- the pair of electrodes is composed of a first electrode 17, which preferably consists of an n-doped TiO 2 crystal, and one thereon
- the holding arm 15g receiving the pair of electrodes is arranged in the reaction space in such a way that, together with the pair of electrodes, it divides the space into two essentially identical chambers G, H.
- the housing has bores 15a, 15b running from the top of the reaction space to the top of the housing, into which bores 15c, 15d are inserted in a sealed manner. Gases which are produced in the chambers G, H can flow through these into gas reservoirs (not shown).
- the gas lines 15c, 15d can expediently be closed in a gas-tight manner by valves 15e, 15f, in order to avoid contamination of the reaction space when the reaction cell is being transported.
- reaction space of the reaction cell is filled with water and light is radiated into the reaction space, the photoelectrochemical reaction described in detail above takes place, in the chamber G on the surface of the semiconducting first electrode 17 for the formation of oxygen gas and in the chamber H on the surface of the second electrode 18 to form hydrogen gas.
- the pair of electrodes which divides the reaction cell into two chambers I, J is fastened to the lower inner surface of the housing 22 of the reaction cell by means of a holding arm, not shown, which does not allow liquid exchange, in particular ion exchange, between the two chambers I, J
- a radiation window 22a is also laterally integrated in the housing.
- An anode-cathode arrangement 27 designed as a fuel cell is provided above the pair of electrodes 23.
- the fuel cell is designed as a low-temperature fuel cell and comprises a cathode 28, an anode 29 and a proton-compatible membrane 30 arranged between them, preferably made of a perfluorinated plastic with a thickness of approximately 0.1 mm.
- the cathode 28 and the anode 29 are connected via an external, i.e. Arranged outside the reaction cell, circuit 31 conductively connected to one another.
- An electrical consumer 32 for example an incandescent lamp or an electric motor, is integrated in the circuit 31.
- the reaction cell is preferably filled with water as the electrolyte 26 to such an extent that the pair of electrodes 23 is completely immersed in it and the membrane 30 of the fuel cell preferably projects into the electrolyte 26.
- the system described establishes a closed cycle in which light energy is converted into electrical energy.
- the reaction cell filled with water 43 as an electrolyte according to FIG. 6 comprises a total of three electrode pairs 34, 35, 36 and three fuel cells 37, 38, 39 arranged in alternating order. Each fuel cell has an external circuit 42 with an electrical consumer. The function of this cell will be explained using the example of the fuel cell 37 and the two adjacent electrode pairs 34, 35:
- the hydrogen generated at the second electrode 34b of the pair of electrodes 34 is passed through the ring line 40 to the other side of the reaction cell, where it is oxidized at the anode 39a of the fuel cell 39 and reacts with oxygen to form water.
- This multiple arrangement creates a particularly powerful system which, depending on the number of fuel cell units used, provides several power sources which can also be connected in parallel.
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- Chemical & Material Sciences (AREA)
- Inorganic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
- Hybrid Cells (AREA)
Abstract
Description
Claims
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE102004012303A DE102004012303B3 (en) | 2004-03-11 | 2004-03-11 | Reaction cell for photo-electrochemical generation of hydrogen, useful particularly in conjunction with fuel cells, has two electrodes, in facial contact, and light source for irradiating the electrodes |
| PCT/EP2005/000425 WO2005088758A2 (en) | 2004-03-11 | 2005-01-18 | Photoelectrochemical reaction cell |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| EP1723267A2 true EP1723267A2 (en) | 2006-11-22 |
Family
ID=34673246
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| EP05700999A Withdrawn EP1723267A2 (en) | 2004-03-11 | 2005-01-18 | Photoelectrochemical reaction cell |
Country Status (6)
| Country | Link |
|---|---|
| US (1) | US20080213641A1 (en) |
| EP (1) | EP1723267A2 (en) |
| AU (1) | AU2005221010B2 (en) |
| CA (1) | CA2558226C (en) |
| DE (1) | DE102004012303B3 (en) |
| WO (1) | WO2005088758A2 (en) |
Families Citing this family (22)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106450591B (en) * | 2005-06-09 | 2019-09-03 | 阿图罗·索利斯埃雷拉 | Device for generating electric energy by photoelectrochemical reaction |
| DE102007028391A1 (en) * | 2007-06-15 | 2008-12-18 | Nano-X Gmbh | Particles or coating for splitting water |
| KR20110083607A (en) * | 2008-08-29 | 2011-07-20 | 칠룸 베타일리공스 게젤샤프트 엠베하 운트 코. 파텐테 Ii 카게 | Layer Systems for Solar Absorbers |
| DE102009007908A1 (en) | 2009-02-06 | 2010-08-12 | Zylum Beteiligungsgesellschaft Mbh & Co. Patente Ii Kg | Method for producing a thin-film photovoltaic system and thin-film photovoltaic system |
| CN102414118B (en) * | 2009-05-21 | 2014-07-23 | 松下电器产业株式会社 | Hydrogen generation system and hot water production system |
| DE102009036180A1 (en) * | 2009-08-09 | 2011-02-10 | Cfso Gmbh | Photocatalyst system for the generation of electricity |
| JP5663254B2 (en) * | 2010-02-08 | 2015-02-04 | シャープ株式会社 | Hydrogen production apparatus and hydrogen production method |
| US8840772B2 (en) * | 2010-05-17 | 2014-09-23 | Honda Motor Co., Ltd. | Solar fuel cell |
| US9180424B2 (en) * | 2010-09-11 | 2015-11-10 | Albert Chin-Tang Wey | Infrared assisted hydrogen generation |
| JP5719555B2 (en) | 2010-09-28 | 2015-05-20 | シャープ株式会社 | Hydrogen production apparatus and hydrogen production method |
| JPWO2012091045A1 (en) * | 2010-12-28 | 2014-06-05 | 株式会社豊田中央研究所 | Photochemical reaction device |
| AT511433B1 (en) * | 2011-11-03 | 2012-12-15 | Pro Aqua Diamantelektroden Gmbh & Co Kg | ELECTRODE, ITS USE AND ELECTROCHEMICAL CELL |
| WO2014104980A1 (en) * | 2012-12-31 | 2014-07-03 | Tum Create Limited | Electrochemical cell, method of fabricating the same and method of generating current |
| DE102013021771A1 (en) * | 2013-12-20 | 2015-06-25 | Forschungszentrum Jülich GmbH | Electrochemical electrolytic cell for water electrolysis and method for operating the same |
| EP3012351A1 (en) | 2014-10-22 | 2016-04-27 | Universität Stuttgart | Method for efficient use of polychromatic light in photocatalytic water splitting |
| US11673100B2 (en) | 2016-09-07 | 2023-06-13 | The Regents Of The University Of California | Systems and methods for integrated solar photodialysis |
| US11912589B2 (en) | 2018-11-02 | 2024-02-27 | The Regents Of The University Of California | Optically thin light-absorbers for increasing photochemical energy-conversion efficiencies |
| WO2020232143A1 (en) | 2019-05-13 | 2020-11-19 | The Regents Of The University Of California | Membranes for enhancing rates of water dissociation and water formation |
| US12230486B2 (en) | 2019-06-19 | 2025-02-18 | The Regents Of The University Of California | Ratchet-based ion pumping membrane systems |
| LU101512B1 (en) * | 2019-12-02 | 2021-06-04 | Herrera Arturo Solis | Motor based in mechanism of muscular contraction |
| EP3859050A1 (en) * | 2020-01-30 | 2021-08-04 | Ulrich Ulmer | Electrolysis devices using ionizing radiation and related methods |
| CN115896820A (en) * | 2022-11-29 | 2023-04-04 | 电子科技大学长三角研究院(湖州) | A three-electrode photoelectrochemical cell for photolysis of water to produce hydrogen |
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| US4094751A (en) * | 1976-09-30 | 1978-06-13 | Allied Chemical Corporation | Photochemical diodes |
| DE3635585A1 (en) * | 1986-10-20 | 1987-05-27 | Hermann Dr Rer Na Killesreiter | Electrochemical solar cell for water hydrolysis and desalination using a photoactive electrode made of organic materials |
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| FR2410506A1 (en) * | 1977-11-30 | 1979-06-29 | Dreyfus Bertrand | Photo-electrolysis cell with semiconductor elements - incorporates photovoltaic junction between electrodes, suitable for producing hydrogen from water |
| US4266338A (en) * | 1978-02-22 | 1981-05-12 | Grumman Aerospace | Method of manufacturing photoelectrochemical cell |
| JPS6033298B2 (en) * | 1978-05-26 | 1985-08-02 | 富士写真フイルム株式会社 | Electrode photoregenerative photorechargeable half cell and photochemical cell using the same |
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| US4793910A (en) * | 1987-05-18 | 1988-12-27 | Gas Research Institute | Multielectrode photoelectrochemical cell for unassisted photocatalysis and photosynthesis |
| US5268081A (en) * | 1992-08-04 | 1993-12-07 | Ceskoslovenska Akademie Ved | Electrolytic source of pressurized hydrogen |
| US5512145A (en) * | 1994-10-07 | 1996-04-30 | The Cooper Union For The Advancement Of Science And Art | Energy conversion system |
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| AU2003295937A1 (en) * | 2002-11-25 | 2004-06-18 | The University Of Toledo | Integrated photoelectrochemical cell and system having a solid polymer electrolyte |
| DE10332570B4 (en) * | 2003-07-13 | 2007-09-06 | Hahn-Meitner-Institut Berlin Gmbh | Photovoltaic system for direct hydrogen production and collection and use thereof |
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2004
- 2004-03-11 DE DE102004012303A patent/DE102004012303B3/en not_active Expired - Fee Related
-
2005
- 2005-01-18 AU AU2005221010A patent/AU2005221010B2/en not_active Ceased
- 2005-01-18 CA CA2558226A patent/CA2558226C/en not_active Expired - Fee Related
- 2005-01-18 EP EP05700999A patent/EP1723267A2/en not_active Withdrawn
- 2005-01-18 US US10/592,258 patent/US20080213641A1/en not_active Abandoned
- 2005-01-18 WO PCT/EP2005/000425 patent/WO2005088758A2/en not_active Ceased
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4094751A (en) * | 1976-09-30 | 1978-06-13 | Allied Chemical Corporation | Photochemical diodes |
| DE3635585A1 (en) * | 1986-10-20 | 1987-05-27 | Hermann Dr Rer Na Killesreiter | Electrochemical solar cell for water hydrolysis and desalination using a photoactive electrode made of organic materials |
Also Published As
| Publication number | Publication date |
|---|---|
| AU2005221010A1 (en) | 2005-09-22 |
| WO2005088758A3 (en) | 2006-03-30 |
| US20080213641A1 (en) | 2008-09-04 |
| AU2005221010B2 (en) | 2010-07-08 |
| WO2005088758A2 (en) | 2005-09-22 |
| DE102004012303B3 (en) | 2005-07-14 |
| CA2558226A1 (en) | 2005-09-22 |
| CA2558226C (en) | 2015-03-24 |
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