PHOTO-ENHANCED ELECTRO-CATALYTIC (PEEC) PROCESS
20220307144 · 2022-09-29
Assignee
Inventors
Cpc classification
International classification
B01J19/08
PERFORMING OPERATIONS; TRANSPORTING
B01J19/12
PERFORMING OPERATIONS; TRANSPORTING
Abstract
A photo-catalyst (E.sub.p) is regarded as an alternate method to replace the plasma chemical process and as an additional catalytic processing scheme on top of a micro- or nano-structured catalyst (E.sub.c) and electro-catalyst (E.sub.v). The potential energy reduction that results from the effect of photo-enhanced electro-catalyst (PEEC) is significant.
Claims
1. A chemical reactor for use in the reaction and dissociation of aqueous and gaseous compounds, the reactor comprising: a vessel; an electro-catalytic medium fixed inside the vessel and a DC power source to create a cathode side of the electro-catalytic medium and an anode side of the electro-catalytic medium; a high energy photon emission source wherein the source emits photons having a wavelength greater than 100 nm, and wherein the source is configured to be adjacent the electro-catalytic medium; a source pump to inject reaction materials into the vessel to pass through the electro-catalytic material and subject it to the photons from the photon emission source; and An extraction port to collect the reaction or dissociation products from the vessel.
2. A chemical reactor as described in claim 1, wherein the electro-catalytic medium is formed of one or more transition metals or alloy of transition metals.
3. A chemical reactor as described in claim 1, wherein the electro-catalytic medium comprises a porous and foamy nano-structure.
4. A chemical reactor as described in claim 1, wherein the high energy photon emission source is embedded in the electro-catalytic medium.
5. A chemical reactor as described in claim 1, wherein the high energy photon emission source is a deuterium lamp.
6. A chemical reactor as described in. claim 1, wherein the high energy photon emission source is a cobalt-60 source.
7. A chemical reactor as described in claim 1, wherein the high energy photon emission source is a cesium-137 source.
8. A chemical reactor as described in claim 1, wherein the reaction materials are component atoms used to form a molecule.
9. A chemical reactor as described in claim 1, wherein the reaction materials are molecules used to form individual component atoms.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
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DETAILED DESCRIPTION
[0030] In the present invention, a photo-catalyst (E.sub.p) is regarded as an alternate method to replace the plasma chemical process and as an additional catalytic processing scheme on top of the micro- or nano-structured catalyst (E.sub.c) and electro-catalyst (E.sub.v) as described in
[0031] The diagram 10 plots energy 12 on its vertical axis versus reaction progress 14 on its horizontal axis. The presence of the localized perturbed electrical field by the emitted electrons by photons in addition to the electrical charge density on the surface of catalyst lowers the energy required for catalytic reaction further from the energy maxima of electro-catalyst. The photo-catalyst offers a different reaction pathway by lowering further the activation energy (E.sub.a) by E.sub.c+E.sub.v+E.sub.p. The final result and the overall thermodynamics are the same. Based on the energy requirement for dissociation process, it is greatly beneficial to adopt the electro-catalytic method to enhance the breakdown rate of gaseous and aqueous molecules. The photo-catalyst (E.sub.p) as an additional catalytic process will add a great role to reduce the required energy of chemical process. If the breakdown process of carbon dioxide is, in one particular example, contemplated for application-oriented products, such as propellant for rockets, the only limiting factor in space operation will be the power and the morphologic structure of the selected electro-catalytic material. Clearly it is preferable to have a low energy required process with a simple dissociation mechanism. Potential energy diagram shows the effect of an electro-catalyst (E.sub.v) in a hypothetical exothermic chemical reaction A+B to give C. The presence of the additional electrical charge density on the surface of catalyst opens a different reaction pathway (shown in broken line with dots) by lowering the activation energy (E.sub.a) by the sum of E.sub.c+E.sub.v. The result of process and the overall thermodynamics are the same, but the accumulated electrical charge density at the fine porous foamy surface structure of catalyst increases the surface energy. Any molecules adhered or adsorbed or positioned in the close proximity of catalyst can experience energy transfer from the atoms with high charge density at surface of catalyst. The energy gained by the adsorbed, adhered, or positioned molecules adjacent to the catalytic surface almost equally increase their stress energy. If this stress energy is higher than the binding energy, it causes dissociation of molecules by high stress energy. In the same manner, the contrary is true. Those atoms or molecules which have high stress energy or activation energy can undergo endothermic process for chemical bindings. Clearly, electro-catalytic effect can reduce the energy by E.sub.v further from the energy required for endothermic or exothermic process. The electro-catalytic process was well proven by the test made with the porous foamy Ni—Fe catalytic material to breakdown carbon dioxide molecules.
[0032] The process and system described herein are summarily shown in
[0033] In
[0034] The combined effects of photon injection on electro-catalytic reaction from (1) through (7) stated above can translate together into further reduction of the energy which is, otherwise, required either for the endothermic or exothermic processes. The benefit appears as further reduction of process energy at least by E.sub.p as shown in
[0035]
[0036] The energy of incident photon flux is partially absorbed by porous material and the rest is reflected, trapped into porous space, and eventually absorbed into material as shown in the right of
[0037] The systems and processes described herein are based on the photo-enhanced electro-catalyst (PEEC) concept that uses any light source(s) with emission capability of ultraviolet, vacuum ultraviolet (VUV), soft X-rays, X-rays, and even gamma rays (>100 keV). Based on the customary scientific notation 70 as shown in
[0038] The generation of soft X-rays requires more intensive energy to excite and ionize the electrons of the inner shell of atoms through the process of bound-to-free transition. The emission rate or flux density of soft X-rays is, basically, dependent on the radiative recombination rate while undergoing the level transition through recombination (free-to-bound) of excited and ionized electrons downward to the inner-shell ground state.
TABLE-US-00002 TABLE II Photon sources for PEEC applications Photons Specifications VUV X-Ray Gamma Ray Conventional Name FUV EUV Soft X-ray Hard X-Ray Cs-137 Co-60 Energy 6~30 eV 30~700 eV 700 eV~3 keV 3 keV~100 keV 660 keV 1.3325 MeV Spectral Range 200~40 nm 40~2 nm 2~0.4 nm 0.4~0.012 nm 0.00188 nm 0.00093 nm Sources Deuterium D.sub.2-Ar D.sub.2-Ar D.sub.2-Ar Radioisotope Radioisotope Lamp Diffusion Arc Discharge High Voltage Arc Discharge Key Aspects for D-Orbital Plus Plus Plus Plus Plus Catalytic Interaction Electrons on Electrons on Electrons on Electrons on Electrons on Electrons on Outermost Outer/Inner Inner Shells Intra-bands Intra-bands Intra-bands Shell shells (bound-to-free) (bound-to-free & (bound-to-free & free-to-free) free-to-free) Catalytic Effects Better with Better with Better with Better with Better with Better with (w/o PGM) Transition Transition Any Metals Any Metals Any Metals Any Metals Metals Metals Lifetime Mega Cycles Mega Cycles Kilo Cycles Kilo Cycles 30 yrs CW 5 yrs CW
[0039] Table II shows a tabulation of examples of photon sources that may be used in the systems and processes described herein. Radioisotopes, Cs-137 and Co-60, offer very attractive features for not only long-term operation, but also high energy photons to excite and liberate the intra-band electrons of atoms in catalytic medium which will exceed the dissociation energy of aqueous or gaseous molecules.
[0040] An aspect of the processes and systems herein is to use any transition metals as an electro-catalyst for dissociation of gaseous molecules under at least the seven benefits described below: [0041] (1) Energized aqueous or gaseous molecules by photon coupling require a reduced breakdown energy through an added process of increasing collision frequency between aqueous or gaseous molecules and excited electro-catalytic body, [0042] (2) Energized aqueous or gaseous molecules by the energy gain from photon coupling loosen the bonding structures of aqueous or gaseous molecules, [0043] (3) The photo-dissociation of aqueous or gaseous molecules that requires only a few electron-volt level, also see Table I, can be pretty much done by VUV and soft X-rays even before interacting with ECM, [0044] (4) The enhanced electro-catalytic process is enabled by adding the increased number of the excited or energized conduction electrons within the electro-catalytic body of sharp and tiny structure by incident photon agitation, [0045] (5) The increased collision frequency of atoms and gaseous molecules energized by photon coupling improves the reactive function of electro-catalyst by the increased collision contact rate to the excited electro-catalytic body under the dynamic field fluctuation which is caused by the perturbed free electron motions as shown in
Therefore, in order to maximize these seven potential benefits described above, a catalytic system is integrated with any emission sources of high energy photons, such as ultraviolet, vacuum ultraviolet (VUV), soft X-rays, X-rays, and even gamma rays (>100 keV), as shown in
[0048] In
[0049] The energy carried by VUV is much more than the bonding energy of aqueous or gaseous molecules. Accordingly, the VUV alone has significant impacts on the activation and reaction rate of ECM for even meeting the seven benefits by the physical aspects of VUV.
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[0051] The structure 150 of the system shown in
[0052] A certain number of liberated energetic electrons at an ECM surface departs and is emitted. These emitted electrons still carry a lot of kinetic energy and have a great probability of collision with molecules in the vicinity that gives also rise to the increase in the stress level toward the bonding structures. Or even is able to break down molecules if kinetic energy is sufficient. The high energy photons that penetrate through the ECM have also a great probability of coupling with atoms and molecules that lead to the ionization and dissociation of molecules even before reaching to the ECM for catalytic reaction.
[0053] Most of gamma ray sources have a long half-life to emanate high energy photons. For example, the half-life of Cs-137 is 30.17 years. A single installation of such a high energy photon source into ECM for catalytic process can sustain the catalytic process for a long period of time. Accordingly, the cost benefit is high.
[0054] Likewise, the X-ray and soft X-ray have a much higher impact than the VUV does. The energy and frequency of soft X-rays are sufficiently high that they can dissociate the aqueous or gaseous molecules and ionize the atoms and molecules. Also, they can penetrate the ECM much deeper than VUV.
[0055] For X-ray and gamma ray, the penetration depths are quite larger than that of soft X-ray as described in
TABLE-US-00003 TABLE III Penetration depth of soft X-rays through porous Ni, Fe, and Ni-Fe alloy Scattering Penetration Depth Penetration Depth Soft X-ray Porosity Cross-section - Solid - - Porous - Ni Density 1 keV 8.908 g/cm.sup.3 60% 7.812E-03 cm.sup.2/g 0.72 mm 1.8 mm 1.5 keV 8.908 g/cm.sup.3 60% 1.390E-02 cm.sup.2/g 1.24 mm 3.1 mm 2 keV 8.908 g/cm.sup.3 60% 1.960E-02 cm.sup.2/g 1.75 mm 4.38 mm Fe Density 1 keV 7.860 g/cm.sup.3 60% 8.777E-03 cm.sup.2/g 0.69 mm 1.73 mm 1.5 keV 7.860 9/cm.sup.3 60% 1.530E-02 cm.sup.2/g 1.20 mm 3.00 mm 2 keV 7.860 g/cm.sup.3 60% 2.124E-02 cm.sup.2/g 1.67 mm 4.18 mm Ni-Fe Density 1 keV 8.384 g/cm.sup.3 60% 8.295E-03 cm.sup.2/g 0.69 mm 1.73 mm 1.5 keV 8.384 g/cm.sup.3 60% 1.460E-02 cm.sup.2/g 1.34 mm 3.35 mm 2 keV 8.384 g/cm.sup.3 60% 2.042E-02 cm.sup.2/g 1.71 mm 4.23 mm
[0056] In one example, a combination of VUV and soft X-rays may be used for the enhancement of ECM performance. In this example, the thickness of Ni—Fe ECM can be kept larger than 4 mm, perhaps 5 mm. In other examples, using X-rays and gamma rays, the ECM thickness can be increased because of long penetration depths.
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[0060] The roles of high energy photons include the following: [0061] (1) to increase the charge density of ECM surface by liberating the electrons in intra-bands of atoms, [0062] (2) to sustain the emitted energetic electrons from the ECM's porous foamy surface in order to couple with aqueous or gaseous molecules and energize or increase the stress level of molecules, [0063] (3) to induce direct dissociation of molecules by the emitted energetic electrons, [0064] (4) to keep the high energy photons to couple directly with and break down molecules a priori catalytic reaction by molecules reaching to the ECM surface or to ionize molecules.
[0065] The PEEC cathode 222, as shown in
EXAMPLE ONE
Dissociation of CO.SUB.2
[0066]
[0067] There are several electro-catalysts available but generally the breakdown rate is very low. For example, the electro-catalyst made with nano-structure coated by depositing atomic layers of tin oxide on copper oxide nanowires shows only 13.4% breakdown rate of carbon dioxides with 90% Faradaic efficiency. Another electro-catalyst is a metallic Ni—Fe composite foam that demonstrates 97% Faradaic efficiency.
[0068] For the Ni—Fe electro-catalyst, when it is applied with 2.13 V and current density of 10 mA/cm.sup.2, it performed high electricity-to-chemical fuel efficiency of 59%. The systems and processes herein, there is not only a Ni—Fe metal compound as electro-catalyst, but also other transition metal compounds as electro-catalysts for the breakdown of carbon dioxides, water, or even other chemical compounds for energy and cost-effective catalytic process. In this case, 41% of unbroken CO.sub.2, after separation, is fed back to the Ni—Fe electro-catalyst.
[0069] The total benefit from this integrated system is to reduce the environmental gas, CO.sub.2, and at the same time to convert it into chemically very useful oxygen, hydrogen, methane, and polymers through the described synthetic processes.
[0070] Table IV tabulates the catalytic processes of CO.sub.2 which have been so far practiced in the university and industry laboratories, including comparatively the present PEEC process with the parameters estimated for the case when the injection of high energy photons is considered.
TABLE-US-00004 TABLE IV Composition and performance metrics of low-temperature, molten carbonate and solid oxide electrolysis cells for electrochemical conversion of CO.sub.2 into CO, evaluated at a CO-specific current density of 200 ± 30 mA cm.sup.−2 Electric Power Faradaic Voltage ASR Energetic Consumption Cost References Cell Composition Efficiency (V) (Ω .Math. cm.sup.2) Efficiency (kWh/Nm.sup.3) (¢/Nm.sup.3) Ebbesen LSM-YSZ | YSZ | Ni-YSZ 100% 1.0 0.3 92% 2.4 31.656 et al..sup.[14] Kangas LSCF-CGO | CGO | YSZ | Ni-YSZ 100% 1.1 1.1 91% 2.5 32.975 et al..sup.[15] Kaplan Graphite | Li.sub.2O-Li.sub.2CO.sub.3 | Ti >96% 1.1 1.9 74% 2.9 38.251 et al..sup.[13] Verma IrO.sub.2/C-Nafion | KOH | 64% 2.5 4.8 33% 9.4 123.986 et al..sup.[17] Au-MWCNT-PyPBl-Nafion/C Ma IrO.sub.2/C-Nafion | KOH | 101% 2.5 3.6 54% 5.9 77.821 et al..sup.[18] Ag/MWCNT-Nafion Kutz IrO.sub.2/C-PTFE | Suslanion | Ag/C 96% 3.0 8.3 43% 7.4 97.606 et al..sup.[19] Kaczur IrO.sub.2/C | KHCO3 | Sustanion-PTFE | 98% 3.0 13.5 44% 7.2 94.968 et al..sup.[20] Ag/C Dufek IrO.sub.2/Ni | KOH | Nafion | K.sub.2SO.sub.4 | 91% 3.7 11.5 41% 9.8 129.262 et al..sup.[21] Ag/C Endrödi Ir/Ti | KHCO.sub.3 | Sustanion-PTFE | 73% 3.0 3.8 35% 9.8 129.262 et al..sup.[16] Ag/C Haas IrO.sub.2/MMO | K.sub.2SO.sub.4-KHCO.sub.3 | ZrO.sub.2 | 81% 4.4 9.1 27% 12.9 170.151 et al..sup.[22] K.sub.2SO.sub.4-KHCO.sub.3 | Ag Invented NIFe or other transition metal 110% 5.0 0.1 97% 1.51 19.917 PEEC compounds with KeV photons ASR-Area-specific resistance: Ω-cm.sup.2
[0071] Table V illustrates power requirement for dissociation of CO.sub.2 through the PEEC process as compared to just bond dissociation, plasma-chemical, electro-catalysis, and photo-catalysis.
TABLE-US-00005 TABLE V Power requirement for dissociation rate of CO.sub.2 Photo-Enhanced CO.sub.2 Bond-Dissociation Plasma-Chemical Electro-catalysis Photo-catalysis Eleclro-Catalysis Dissociation Rate (5.51 eV/bond) [6] (2.61 eV/bond) [8] (2.13 eV/bond) [13] (1.35 eV/bond) [7] (0.5 eV/bond) 1 g/s 12.069 kW 5.717 kW 4.665 kW 2.957 kW 1.095 kW 10 g/s 120.690 kW 57.168 kW 46.655 kW 29.657 kW 10.952 kW 100 g/s 1206.90 kW 571.686 kW 466.549 kW 295.7 kW 109.518 kW 1000 g/s 12.069 MW 5.717 MW 4.665 MW 3 MW 1.1 MW
The dissociation process by the PEEC process requires substantially low power as compared to others listed. The PEEC process was estimated for power requirement using high energy photons that lower the energy required for breakdown.
EXAMPLE TWO
Dissociation of Water (H.SUB.2.O)
[0072] In chemical reaction processes, catalysts play a crucial role in lowering the kinetic barrier. The dissociation of water molecule into hydrogen and oxygen requires a bipolar catalytic medium as well. The PGMs based on noble metals (Pt, Rh, Pd, Ru, Ir, and Os) have been used as the most efficient HER electrocatalyst in acid medium owing to its moderate hydrogen binding energy and long-life cycle. On the other hand, noble metal oxides, such as RuO.sub.2 and IrO.sub.2, are considered as the state-of-the-art electrocatalysts for OER. However, the high cost and scarcity of noble metals have slowed large-scale applications. And also, there are no rooms to enhance the performance of noble metals as electrocatalysts further, except for modest improvement. It has been a persisting reason to search around for any alternates. On the other hand, alkaline liquid electrolyzer technology has been commercially used because of the overall low cost of various components. Whereas the activity of Pt in alkaline electrolysis condition is about two to three orders of magnitude lower than that in acid. Significant steps have made in early studies to describe the hydrogen evolution reaction (HER) in alkaline media. The fist-step is the water dissociation as H.sub.2O+e.sup.−.fwdarw.H*+OH.sup.−, where H* represents adsorbed H on active site, then followed by either Tafel step (2H*.fwdarw.H.sub.2) or Heyrovsky step (H.sub.2O+H*+e.sup.−.fwdarw.H.sub.2+H.sup.−).
[0073] In efforts to reduce the cost by improving HER electroactivity, platinum alloys with transition metals were used and discovered that Pt alloys with transition metal can have similar synergistic effect of Pt for HER electroactivity. Thus, the development of highly efficient and stable electrocatalysts that bring down water dissociation barrier as low as possible and keep appropriate hydrogen adsorption/desorption strength is highly essential in industrial applications.
[0074]
[0075] For electrochemical water splitting reaction, the thermodynamic potential is 1.23 V at 25° C. and 1 atm. However, due to the kinetic barrier for the reaction, water electrolysis requires a higher potential than thermodynamic potential (1.23 V) to overcome the kinetic barrier. The excess potential is also known as overpotential (η) which mainly comes from the intrinsic activation barriers present on both anode and cathode. Overpotential is a very important descriptor to evaluate the activity of the electrocatalysts. Usually, the overpotential value corresponding to the current density of 10 mA/cm.sup.2 is used to compare the activities among different catalysts. This current density corresponds to a 12.3% solar-to-hydrogen efficiency.
[0076] The Tafel slope and exchange current are two other parameters to assess the activity from the overpotential vs. kinetic current relationship, which is expressed by the equation: η=a+b log j, where η is the overpotential, and j is the current density. In the Tafel plot, the linear correlation yields two important kinetic parameters. One is the Tafel slope b, and the other is the exchange current density jo which can be obtained by extracting the current at zero overpotential. The Tafel slope b is related to the catalytic reaction mechanism in terms of electron-transfer kinetics. For example, a smaller Tafel slope means that there is a significant current density increment as a function of the overpotential change, or in other words, faster electrocatalytic reaction kinetics. The exchange current density describes the intrinsic charge transfer under equilibrium conditions. A higher exchange current density means a greater charge transfer rate and a lower reaction barrier. A lower Tafel slope and a higher exchange current density are expected for a better electrocatalyst.
[0077] Most effective catalytic materials, no matter whether they can work on catalytic process directly or electro-assisted or photo-assisted way, are in demand for many applications. A new approach called PEEC provides better catalytic effect to answer to various demands. There are several unique features of PEEC that set its performance superior to the conventional electrocatalytic media. Either the photon source for PEEC listed in Table II is imbedded inside nano-structured ECM or the photon sources are placed outside the nano-structured ECM to illuminate the ECM, the photon energy is extremely high (10 eV˜1.33 MeV) that it has a series of coupling interaction with the atoms of nano-structured ECM to liberate a large number of the intra-band electrons of atom. These many numbers of liberated free electrons still carry high energy aftermath of interactions. These electrons have a significant role to diminish or suppress the overpotentials at both HER and OER by electron-transfer kinetics, resulting in faster electrocatalytic reaction kinetics. Energetic photon-interaction induces and results in many free electrons that will increase charge potential at the surface of ECM for greater dissociation rate. The increased charge potential at the surface of ECM exceeds not only kinetic barrier (5.15 V), but also thermodynamic potential (1.23 V) by the charge potential attribution of accumulated number of free electrons at surface layer of ECM over several factor or order of magnitude to split a water molecule. Those free electrons still carrying high kinetic energy with great mobility in ECM domain play substantial role for dramatic increase in not only the charge potential to induce enhanced catalytic reaction mechanism under electron-transfer kinetics, but also exchange current density which lowers reaction barrier. High exchange current density enhances charge transfer rate by even over the required charge density to nearly diminish and nullify the overpotential issues at HER and/or OER.
[0078] In
[0079] Another aspect of energetic photons is direct coupling with water molecules that can eventually break down water molecules into hydrogen and oxygen but not by catalytic effect. Since higher the photon energy is, longer the mean free path is, thick ECM for anode and cathode can be used. Since thick ECM increases its volume and reaction surface area, an increased production rate of hydrogen and oxygen is anticipated.
TABLE-US-00006 TABLE VI Power requirement for dissociation rate of H.sub.2O Photo-Enhanced Thermodynamic Goethite, Electro-Catalysis H.sub.2O Bond-Dissociation Electro-catalysis Potential Fe + 3O(OH) (PEEC) Dissociation Rate (5.15 eV/bond) [6] (2.2 eV/bond) [28] (1.23 eV/bond) [27] (1.1 eV/bond) [2] (0.4 eV/bond) 1 g/s 30 kW 12.815 kW 7.165 kW 5.717 kW 2.330 kW 10 g/s 300 kW 128.155 kW 71.650 kW 57.168 kW 23.3 kW 100 g/s 3 MW 1.281 MW 716.500 kW 571.686 kW 233 kW 1000 g/s 30 MW 12.815 MW 7.165 MW 5.717 MW 2.33 MW 2H.sub.2O + 15 hv .fwdarw. 2H.sub.2 + O.sub.2 E = −15 hv = −5.15 eV = −496.924 kJ/mol Breakdown rate of H.sub.2O into 2H + O; 1 eV = 96.49 kJ/mol 1 kg of H.sub.2O = 55.5 moles E = −5.15 eV = −496.924 kJ/mol = −27,579 kJ/kg Power required: P.sub.H2O =27,579 kJ/s ≈ 30 MW for breaking down 1 kg/s of H.sub.2O
Materials for PEEC Cathode and Anode
[0080] There are virtually no limits on the selection of materials for the cathode and anode of PEEC since abundant energetic electrons liberated from the intraband of atom in ECM by the energetic photon source imbedded into the cathode and/or anode can surpass the thermodynamic potential (1.23 V) and intrinsic kinetic barrier potential (5.15 V) for accelerating electrocatalytic reaction kinetics and increase the exchange current density which lowers reaction barrier. It is generally known that a good catalyst would facilitate the adsorption of reactants on the surface of catalyst, their reaction, and desorption of the products to regenerate the active sites for the cyclic process of adsorption-reaction-desorption with new reactant molecules. In terms of common understanding on catalytic process and materials, the characteristics of PEEC clearly show extraordinary approach that is advantageous and supersedes the performances of conventional processes and renders a broad option for the selections of materials for cathode and anode. As long as the selected materials for PEEC are chemically most resistant against corrosion and oxidation, they will satisfy the material requirements of PEEC.
Summary of PEEC Process Benefits
[0081] The PEEC process enhances ECM processes with the addition of VUV, X-rays, and/or gamma rays to offer multiple benefits: [0082] 1) The PEEC based nano-structured ECM can flexibly use inexpensive transition metals. [0083] 2) The rate of dissociation with any inexpensive transition metals can exceed the level of dissociation rate so far known with the PGM. [0084] 3) The ECM with high energy photon sources, such as VUV, soft X-rays, X-rays, and gamma rays, can be applicable to most of chemical synthesis and dissociation processes. [0085] 4) The interaction of ECM with energetic photons drastically increases the population density of liberated free electrons (or charge potential) at the surface of nano-structure ECM that alleviates or diminishes the overpotential issue that may happen in conventional electrocatalytic processes. [0086] 5) Artificially enhance charge potential due to the high population density of liberated free electrons through interaction of ECM with energetic photons suppresses thermodynamic potential (1.23 V) and intrinsic kinetic barrier potential (5.15 V) for faster electrocatalytic reaction kinetics by AV as demonstrated in
[0092] The PEEC process is a combination of ECM with energetic photon sources, such as VUV, soft X-rays, X-rays, and gamma rays, that can increase the dissociation rate with a reasonable energy consumption. The PEEC system can utilize a choice of inexpensive transition metals as electro-catalytic media since energetic photons induce high population density of liberated free electrons beyond the conventional concepts that rely on noble metals and noble metal oxides. The PEEC exceeds the conventional catalytic processes by overcoming the thermodynamic potential and intrinsic kinetic barrier potential for faster electrocatalytic reaction. The integrated dissociation or synthetic process of aqueous and gaseous molecules that will offer the production of oxygen, hydrogen, water, methane or many more chemicals as the end-products is unique.
[0093] The PEEC process can reduce the environmentally unwanted gas, carbon dioxides, and at the same time it can produce useful chemicals, oxygen, hydrogen, water, methane, and even further polymers in a single integrated system.
[0094] With the VUV, and soft X-rays, X-rays, gamma rays, an ECM can flexibly use of any inexpensive transition metals. And the rate of dissociation with any inexpensive transition metals can exceed any level of Faradaic efficiency. The ECM with VUV, and soft X-rays, X-rays, gamma rays can be applicable to most of chemical synthesis and dissociation processes.
[0095] The PEEC process has governmental applications including, but not limited to, the following: [0096] Mars exploration requires onsite propellant production. The PEEC process will greatly help the production of oxygen, hydrogen, methane, and polymers in a single integrated system approach. [0097] Production of oxygen and hydrogen from ice water harvested from permanently shadowed region of the Moon.
[0098] The PEEC process also has prospective industry applications: [0099] Reduction of environmentally polluting and global warming gas, CO.sub.2. [0100] Enhanced scrubber technology to get rid of CO.sub.2 at flue stacks of factories. [0101] Enhanced chemical processes of dissociation and synthesis in an inexpensive way. [0102] Enhanced hydrogen production.
[0103] Other embodiments of the present invention will be apparent to those skilled in the art from consideration of the specification. It is intended that the specification and Figures be considered as exemplary only, with a true scope and spirit of the invention being indicated by the following claims.