JP5376618B2 - Electrode device for plasma discharge - Google Patents

Description

  The present invention relates to an electrode device for plasma discharge.

  A method using non-equilibrium plasma (low temperature plasma) is known as a method for decomposing various harmful gases such as NOx, SOx, dioxin, etc., or as a method for generating hydrogen by reforming hydrocarbon fuels. Yes. In the method using non-equilibrium plasma, only the energy of electrons (electron temperature) is high, and the energy of ions and molecules is low. Therefore, it is possible to lower the temperature of the process by injecting electrons, radicals, and active species, and to achieve a process comparable to the conventional thermochemical method, and it is possible to reduce the size and weight of the apparatus.

Patent Document 1 discloses that a gas processing apparatus using such non-equilibrium plasma supports both a normal gas processing catalyst and a photocatalyst.
JP-A-2005-144445

Patent Document 2 discloses that a counter electrode is used in a gas processing apparatus using non-equilibrium plasma.
JP 2004-237135 A

Patent Document 3 discloses that a zeolite layer is provided on the surface region of a plasma generating electrode device, and a catalyst is supported on the zeolite layer.
JP 11-347342 A

Patent Documents 4 and 5 disclose that a hydrogen-rich atmosphere is generated by subjecting a hydrocarbon fuel to non-equilibrium plasma treatment.
JP-A-2005-35852 JP-A-2005-170744

  In the structure in which the non-equilibrium plasma and the catalyst are used in combination as described above, the gas purification rate is improved in the case of only the non-equilibrium plasma as compared with the catalyst alone. However, the gas purification rate is not always sufficient for practical use, and further improvement is required for practical use from the viewpoint of energy efficiency.

  An object of the present invention is to further improve gas processing efficiency in a plasma discharge electrode device that generates non-equilibrium plasma and performs gas processing.

The present invention is a plasma discharge electrode device for generating a non-equilibrium plasma and performing gas treatment,
A dielectric powder comprising a dielectric substrate, an electrode embedded in the substrate, a catalyst mixed with the substrate to promote a gas reaction, and a secondary electron emitter powder mixed with the substrate. The catalyst is obtained by mixing a catalyst and a secondary electron emission agent powder in the body, embedding an electrode, and sintering.

  As a result of continuing various studies on gas treatment using a combination of non-equilibrium plasma and a catalyst, the present inventor has carried out gas treatment by further supporting a secondary electron emitting agent in addition to the catalyst on the substrate of the electrode device for plasma discharge. The inventors have found that the efficiency is dramatically improved and have reached the present invention.

Hereinafter, the present invention will be described in more detail with reference to the drawings as appropriate.
FIG. 1 is a diagram schematically showing a gas processing apparatus to which the present invention can be applied. This example relates to a so-called counter electrode type device. Non-equilibrium plasma is generated in the space 3 between the pair of electrode devices 2A and 2B facing each other, and a gas is flowed as shown by an arrow A to perform a predetermined treatment. An electrode 4 is embedded in each electrode device.

  The material constituting the substrate is not particularly limited, but ceramics are preferable, especially alumina, zirconia, silica, mullite, spinel, cordierite, aluminum nitride, silicon nitride, titanium-barium oxide, barium-titanium-zinc oxide. Etc. are preferable. The material of the electrode is not particularly limited, and any material having a predetermined conductivity can be used. For example, tungsten, molybdenum, manganese, titanium, chromium, zirconium, nickel, silver, iron, copper, platinum, palladium, or an alloy thereof is preferable.

  The substrate can be manufactured by a so-called green sheet lamination method. That is, when the dielectric powder such as ceramics is press-molded, a metal plate or a metal foil constituting the embedded electrode can be embedded and then sintered. The electrode can also be formed by applying a paste on a ceramic green sheet. As a coating method in this case, any coating method such as screen printing, calendar roll printing, dipping method, vapor deposition, physical vapor deposition method and the like can be used. When an electrode is formed by a coating method, the above-mentioned various metal or alloy powders are mixed with an organic binder and a solvent (such as terpineol) to prepare a conductor paste, and then this conductor paste is applied onto a ceramic green sheet. Work.

  When manufacturing the substrate, the method for forming the ceramic green sheet is not particularly limited, and any method such as a doctor blade method, a calendar method, a printing method, a roll coater, or a plating method can be used. In addition, as the raw material powder of the green sheet, the above-described various ceramic powders and powders such as glass can be used. At this time, examples of the sintering aid include silicon oxide, calcia, titania, magnesia, and zirconia. It is preferable to add 3 to 10 parts by weight of the sintering aid with respect to 100 parts by weight of the ceramic powder. Known dispersing agents, plasticizers, and organic solvents can be added to the ceramic slurry.

A substrate can also be made by powder press molding, and when a mesh metal or metal foil is used for the electrode to be embedded, a sintered body in which the electrode is embedded can be obtained by a hot press method.
By appropriately selecting a molding aid, a molded body of the substrate can be produced even by extrusion molding. By appropriately selecting a solvent on the surface of the extruded product, a metal paste serving as a conductive film component can be formed as an electrode by printing or the like.

  The catalyst is mixed in the material constituting the substrate.

In the present invention, the secondary electron emitter powder is mixed and contained in the base material. In this case, for example, the secondary electron emission agent particles can be mixed in the green sheet dough described above and fired.

  The particle diameter of the secondary electron emitter particles is preferably 100 μm or less, more preferably 50 μm or less. Further, the particles of the secondary electron emitting agent may be crystalline or amorphous.

The secondary electron emitting agent is preferably one kind of metal oxide selected from the group consisting of Be, Mg, Ca, Sr, Sc and Y, or a mixture of two or more kinds of metal oxides.
In a preferred embodiment, magnesia (MgO) and yttria (Y ₂ O ₃ ) are particularly preferable. Two or more secondary electron emitting agents can be used in combination.

  In addition, when the total weight of the secondary electron emitting agent and the catalyst (and the carrier if necessary) is 100% by weight, from the viewpoint of the effect of the present invention, the amount of the secondary electron emitting agent is 0.1% by weight or more. Preferably, it is more preferably 1% by weight or more. Further, from the viewpoint of the stability of the gas treatment efficiency, the amount of secondary electron emitting agent is preferably 50% by weight or less, and more preferably 30% by weight or less.

  FIG. 2 is a diagram schematically showing an electrode device for plasma discharge. In order to avoid complications, cross-sectional hatching is not shown.

In the plasma discharge electrode device 16 of FIG. 2, the electrode 4 is embedded in the substrate 11. A surface layer 9 </ b> A is formed on the electrode 4, and a back surface layer 10 is formed under the electrode 4. In this example, the substrate 11 is formed by a green sheet molding method, and the front surface layer and the back surface layer are each divided into a plurality of layers. The back surface layer 10 is divided into layers 10a, 10b, 10c, and 10d from the electrode 4 to the bottom surface, and the surface layer 9A is divided into layers 9a, 9b, 9c, 9d, and 9e from the electrode 4 to the surface. ing. In the substrate 11, secondary electron emitting agent particles and catalyst particles are mixed as described above.

  In the present invention, the planar pattern of each electrode is not particularly limited, and can be designed according to the type of catalyst and the type of reaction. For example, the planar pattern of the electrodes can be comb-like or mesh-like.

  In the case where the electrode has a net shape or a comb shape, it is preferable that the through holes are formed in a net shape or regularly formed in the gaps between the comb teeth. In this embodiment, the shape of the mesh is not particularly limited, and may be a circle, an ellipse, a racetrack shape, a quadrangle, a polygon such as a triangle, or the like. The shape of the comb-teeth of the comb-like electrode is not particularly limited, but is preferably a rectangle or a parallelogram.

  In the present invention, the gas processing method is not particularly limited. For example, harmful gas can be detoxified using non-equilibrium plasma. Alternatively, hydrocarbon gas can be processed to generate hydrogen, and hydrocarbons with lower carbon numbers (lower hydrocarbons) can be generated.

  Such harmful gases are not limited, but examples include exhaust gases such as NOx and SOx, and exhaust gases containing harmful chemical substances such as dioxins. The catalyst used for such a reaction is not particularly limited. Specifically, one or more selected from Pt, Rh, Pd, Ni, Ag, V, Au, Ce, Co, Cr, Cu, Fe, Li, Ni, Mn, Mo, W and Zn Catalysts containing elements are preferred.

In addition, a reaction from a hydrocarbon fuel to a hydrogen rich gas can be performed. In this case, a fuel reforming catalyst that promotes this reaction is used. In order to accelerate the reaction, a hydrocarbon-based fuel is mixed with air, oxygen, water or the like. Examples of the reaction mode for generating a hydrogen rich gas include partial oxidation using oxygen, steam reforming using water, autothermal reaction using oxygen and water, and the like.

  The fuel reforming catalyst is not limited, but noble metal elements such as copper, palladium, zinc, rhodium, platinum, ruthenium, aluminum, nickel, zirconium, titanium, cerium, cobalt, manganese, silver, gold, barium, iron, etc. are used. sell. More preferably, rhodium, ruthenium, platinum, nickel or the like is used.

  The hydrocarbon fuel is not particularly limited as long as it can generate hydrogen by low-temperature plasma. For example, hydrocarbons such as methane, ethane and propane, alcohols such as methanol and ethanol, ethers such as dimethyl ether and diethyl ether, naphtha, gasoline and light oil are exemplified. Here, when priority is given to the ease of reforming, methane or methanol is preferably used. On the other hand, when the energy density is prioritized, such as being mounted on an automobile, liquid fuel such as gasoline or light oil is preferably used. In addition, the hydrocarbon fuel at the time of reforming may be in a liquid or gas state.

  As the carrier of the fuel reforming catalyst, for example, zinc oxide, cerium oxide, aluminum oxide, zirconium oxide, titanium oxide, and composite oxides thereof can be used. Among these, aluminum oxide is preferable.

(Experiment 1)
A plasma discharge electrode device 16 as shown in FIG. 2 was produced. Specifically, fine aqueous alumina (specific surface area 100 m ² / g) is impregnated with a dinitrodiamine Pt aqueous solution, dried at 120 ° C., and then fired at 550 ° C. for 3 hours, so that Pt containing 10 wt% Pt with respect to alumina. / Alumina powder was obtained. Alumina sol and water were added thereto to obtain a slurry. A mesh-shaped electrode 4 was immersed in the slurry, and a plasma reactor electrode device 16 was produced through drying and firing processes. After that, as shown in FIG. 1, a power source was connected between the four electrode devices, and a plasma reactor was manufactured with a distance between the electrodes of 1 mm. However, in the present invention example, BeO, MgO, CaO, Sc ₂ O ₃ , Y ₂ O ₃ , Li ₂ O, Nb ₂ O ₅ , and WO ₃ powder were added to the slurry. The amount of BeO, MgO, CaO, Sc ₂ O ₃ , Y ₂ O ₃ , Li ₂ O, Nb ₂ O ₅ , and WO ₃ powder is 1 to 50% by weight based on the total solid content of the slurry. _However, 0 to 0.9 wt% in the slurry for Y 2 _{O 3,} was added 51 wt%. For the added BeO, MgO, CaO, Sc ₂ O ₃ , Y ₂ O ₃ , LiO, Nb ₂ O ₅ and WO ₃ , an average particle size of 50 μm was used.

A model gas composed of NO _X : 200 ppm, CO _X : 1000 ppm, and the balance N ₂ was used. The model gas heated to 200 ° C. was introduced into the plasma reactor at a space velocity of 95,000 h ⁻¹ , the amount of NO in the exhausted gas was analyzed, and the NOx purification rate was measured (Equation 1). The conditions of the pulse power source for generating plasma were a repetition period of 3 kHz, a peak voltage of 8 kV, and a peak current of 12A. Table 1 shows the results.

As can be seen from Table 1, in Examples 1 to 10 and Comparative Examples 1 to 4, it can be seen that the NOx purification rate is higher when the secondary electron emitting agent is contained. Looking at the example 1 to 5, _MgO, is particularly high NOx purification rate when containing Y 2 _{O 3} can be seen. Further, looking at the relationship between the content of Y ₂ O ₃ and the NOx purification rate, it can be seen that the NOx purification rate is high when the content is 1 to 50% by weight, more preferably 1 to 30% by weight. It can be seen that even when a plasma discharge electrode device having a similar design is used, a high NOx purification rate can be obtained by using a secondary electron emission agent in combination with a purification catalyst.

(Experiment 2)
A plasma discharge electrode device and a plasma reactor device similar to those in Experiment 1 were prepared, and hydrogen gas generation experiments were performed.
A model gas composed of 2000 ppm of C ₃ H ₈ , 3000 ppm of O ₂ and the balance N ₂ was used. The model gas heated to 200 ° C. is introduced into a plasma reactor heated to 200 ° C. at a space velocity of 95,000 h ⁻¹ , and the amount of H ₂ in the exhausted gas is converted into a TCD (thermal conductivity detector). Analysis was carried out with the gas chromatography provided, and the H ₂ yield was measured (Equation 2). The conditions of the pulse power source for generating plasma were a repetition period of 3 kHz, a peak voltage of 8 kV, and a peak current of 12A.

The results are shown in Table 2. As can be seen from Table 2, in Examples 1 to 10 and Comparative Examples 1 to 4, it can be seen that the H ₂ yield is higher when the secondary electron emitting agent is contained. Looking at the example 1 to 5, _MgO, it is particularly high H ₂ yield when the content of the Y 2 _{O 3} can be seen. Further, when the relationship between the content of Y ₂ O _{3 and} the yield of H ₂ is seen, the H ₂ yield is high when the content is 1 to 50% by weight, more preferably 1 to 30% by weight. I understand. Even when a plasma discharge electrode device having a similar design is used, it can be seen that a high H ₂ yield can be obtained by using the secondary electron emission agent in combination with the purification catalyst.

(Experiment 3)
In the sample of Example 5 of Experiments 1 and 2, the average particle diameter of the secondary electron emitter particles was changed as shown in Table 3. As can be seen from Table 3, the average particle diameter of the secondary electron emitter is preferably 100 μm or less, more preferably 50 μm or less. This is considered to be due to the difficulty in emitting secondary electrons from the inside of the particle as the particle size increases.

It is a figure which shows a plasma reactor apparatus typically. It is the schematic which shows the electrode apparatus 16 for plasma discharge.

Claims (6)

An electrode device for plasma discharge that generates non-equilibrium plasma and performs gas treatment,
A dielectric substrate, an electrode embedded in the substrate, a catalyst mixed with the substrate to promote the reaction of the gas, and a secondary electron emitter powder mixed with the substrate; It said catalyst and said molded body of powder embedded the electrode with mixing secondary electron emission material powder, characterized in that obtained by sintering, plasma generating electrode apparatus.   The apparatus according to claim 1, wherein hydrogen is generated by treatment of the gas.   The apparatus according to claim 1, wherein the gas is a toxic gas, and a process for detoxifying the toxic gas is performed.   The secondary electron emission agent powder is composed of one kind of metal oxide selected from Be, Mg, Ca, Sr, Sc and Y or a mixture of two or more kinds of metal oxides. 4. An apparatus according to any one of claims 3.   The apparatus according to claim 4, wherein the secondary electron emission agent powder comprises at least one of scandia and yttria. 6. The apparatus of claim 5, wherein the secondary electron emitter powder comprises yttria.

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