KR101818824B1 - System for denitrification using plasma and method for denitrification u sing plasma - Google Patents

System for denitrification using plasma and method for denitrification u sing plasma Download PDF

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KR101818824B1
KR101818824B1 KR1020150185271A KR20150185271A KR101818824B1 KR 101818824 B1 KR101818824 B1 KR 101818824B1 KR 1020150185271 A KR1020150185271 A KR 1020150185271A KR 20150185271 A KR20150185271 A KR 20150185271A KR 101818824 B1 KR101818824 B1 KR 101818824B1
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gas
plasma
discharge tube
supply
supply unit
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KR20170075514A (en
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홍용철
신동훈
최대현
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한국기초과학지원연구원
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    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/32—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by electrical effects other than those provided for in group B01D61/00
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
    • B01D46/0027—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with additional separating or treating functions
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34—Chemical or biological purification of waste gases
    • B01D53/46—Removing components of defined structure
    • B01D53/54—Nitrogen compounds
    • B01D53/56—Nitrogen oxides
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34—Chemical or biological purification of waste gases
    • B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
    • B01D53/86—Catalytic processes
    • B01D53/8621—Removing nitrogen compounds
    • B01D53/8625—Nitrogen oxides
    • B01D53/8628—Processes characterised by a specific catalyst
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04C—APPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
    • B04C5/00—Apparatus in which the axial direction of the vortex is reversed
    • B04C5/14—Construction of the underflow ducting; Apex constructions; Discharge arrangements ; discharge through sidewall provided with a few slits or perforations
    • B04C5/185—Dust collectors
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
    • C01B3/02—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
    • C01B3/22—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by decomposition of gaseous or liquid organic compounds
    • H—ELECTRICITY
    • H05—ELECTRIC TECHNIQUES NOT OTHERWISE PROVIDED FOR
    • H05H—PLASMA TECHNIQUE; PRODUCTION OF ACCELERATED ELECTRICALLY-CHARGED PARTICLES OR OF NEUTRONS; PRODUCTION OR ACCELERATION OF NEUTRAL MOLECULAR OR ATOMIC BEAMS
    • H05H1/00—Generating plasma; Handling plasma
    • H05H1/24—Generating plasma
    • H05H1/46—Generating plasma using applied electromagnetic fields, e.g. high frequency or microwave energy
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2251/00—Reactants
    • B01D2251/20—Reductants
    • B01D2251/206—Ammonium compounds
    • B01D2251/2062—Ammonia
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2251/00—Reactants
    • B01D2251/20—Reductants
    • B01D2251/206—Ammonium compounds
    • B01D2251/2067—Urea
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2259/00—Type of treatment
    • B01D2259/80—Employing electric, magnetic, electromagnetic or wave energy, or particle radiation
    • B01D2259/818—Employing electrical discharges or the generation of a plasma
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/04—Integrated processes for the production of hydrogen or synthesis gas containing a purification step for the hydrogen or the synthesis gas
    • C01B2203/0405—Purification by membrane separation
    • C01B2203/041—In-situ membrane purification during hydrogen production

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Abstract

The present invention relates to a denitrification system using plasma and a denitrification method using the same, and more particularly, to a reducing agent supply unit including a plasma synthesis gas generator; A denitration unit for denitrating the NOx-containing gas with the reducing agent provided from the reducing agent supply unit; And a gas discharge unit for discharging the denitrified gas; A denitration treatment system using plasma, and a denitration treatment method using the same.
INDUSTRIAL APPLICABILITY The present invention has excellent denitrification efficiency for nitrogen oxides and enables denitrification treatment at a low temperature.

Description

TECHNICAL FIELD [0001] The present invention relates to a denitration treatment system using plasma and a denitration treatment method using plasma,

The present invention relates to a denitration treatment system using plasma and a denitration treatment method using plasma.

The emission intensity of nitrogen oxides (NOx) is increasing worldwide, and emission regulations for various emission sources have been established in Korea, and regulations are being strengthened.

Nitrogen oxide (NOx) is, NO, NO 2, N 2 O 3, N 2 O 5 The generation of nitrogen oxides is influenced by the partial pressure of oxygen, the ambient temperature, the content of nitrogen components in fuel, the content of volatile components, and the like. Depending on factors such as thermal nitrogen oxides (thermal NOx), prompt nitrogen Oxide (Prompt NOx), and fuel NOx (fuel NOx). The thermal NOx is generated from the nitrogen molecules of the combustion air supplied in the combustion process and is generated at a temperature of about 1300 DEG C, and the amount of thermal NOx is rapidly increased as the temperature is increased. Prompt nitrogen oxides (Prompt NOx) are produced by the conversion of nitrogen oxides into nitrogen oxides by reacting with hydrocarbons via heavy hydrogen (HCN) in the front of the flame where the initial combustion takes place, to be. Although the fuel NOx is generated by the oxidation of nitrogen contained in the fuel, the exact mechanism is unknown, but since the nitrogen content in the fuel is about 0.5% to 2.0%, the combustion process and method are improved The amount of production can be controlled.

Processes for removing nitrogen oxides are typically selective non-catalytic reduction (SNCR) and selective catalytic reduction (SCR). Selective non-catalytic reduction (SNCR) is a method in which a nitrogen-containing reducing agent such as ammonia (NH 3 ), urea (NH 2 CONH 2 ) or the like is injected at a temperature of about 870 ° C. to 1150 ° C., And then decomposes into N 2 , CO 2 , H 2 O,

Since the reaction efficiency of the selective non-catalytic reduction (SNCR) is determined by the temperature range at which the reducing agent is injected, the temperature at the injection point must be kept constant, and if the temperature is not maintained constant, So that the reaction efficiency is lowered, and the ionized reducing agent can be re-formed into ammonia or nitrogen oxide again. It is necessary to remove nitrogen oxides. Exhaust gas can affect the reaction efficiency depending on the CO content, SO 2, etc. depending on the contents of CO and SO 2 depending on the fuel and the like. That is, when the CO content in the exhaust gas is high, the removal efficiency of nitrogen oxide is decreased. When the content of SO 2 is high and the amount of ammonia slip is large, the reaction temperature rises and ammonia sulfate NH 4) 2 SO 4) or ammonium bisulfate ((NH 4 SO 4) the like are caused clogging of the equipment, and is the cause of corrosion. selective non-catalytic reduction (SNCR), the running cost compared with the selective catalytic reduction (SCR) But the removal rate of nitrogen oxides is low.

Selective catalytic reduction (SCR), the ammonia in the presence of an oxidizing catalyst (NH 3), urea (NH 2 CONH 2) to nitrogen-containing reducing agent injection react with NOx after the reducing agent is adsorbed to the surface of the oxidation catalyst, such as N 2 , H 2 O, etc., and has a low emission of ammonia and a high removal efficiency of nitrogen oxides. The reaction efficiency of selective catalytic reduction (SCR) is affected by the reaction temperature, and the reaction temperature is determined according to the oxidation catalyst within a temperature range of about 260 ° C to 600 ° C. Selective catalytic reduction (SCR), the need to heat the system in order to provide a reaction temperature, and the use of expensive catalysts, so a high running cost, reliability problems related to toxicity, the storage of the ammonia used, and ammonia by the SO 2 reacts with (NH 4 ) 2 SO 4 ) or ammonia bisulfate ((NH 4 SO 4 )).

In order to solve the above-mentioned problems, the present invention provides a denitrification system using plasma, which has a low processing cost in denitration treatment of nitrogen oxide-containing gas and has excellent nitrogen oxide removal efficiency.

The present invention also provides a denitration treatment method using a denitration treatment system using plasma.

The problems to be solved by the present invention are not limited to the above-mentioned problems, and other matters not mentioned can be clearly understood by those skilled in the art from the following description.

According to one aspect of the present invention, there is provided a plasma processing apparatus comprising: a reducing agent supply unit including a plasma synthesis gas generating apparatus; A denitration unit for denitrating the NOx-containing gas with the reducing agent provided from the reducing agent supply unit; And a gas discharge unit for discharging the denitrified gas; To a denitration treatment system using plasma.

According to an embodiment of the present invention, the reducing agent supply unit supplies hydrogen gas, and the plasma synthesis gas generating apparatus may include at least one plasma hydrogen gas generator.

According to an embodiment of the present invention, the plasma hydrogen gas generator includes: an electromagnetic wave supply unit that oscillates electromagnetic waves of a predetermined frequency; A discharge tube in which a plasma is generated from the electromagnetic wave and a mixed gas of steam and gas supplied from the electromagnetic wave supply unit; A fixing unit fixing the lower end of the discharge tube; A gas supply unit for injecting a mixed gas of steam and gas into the discharge tube in a spiral shape; A hydrocarbon supply unit supplying a liquid, a gas, or both hydrocarbons to the plasma generated inside the discharge tube; An ignition unit for supplying initial electrons for plasma generation to the inside of the discharge tube; And a gas discharge unit for discharging the synthesis gas synthesized from the reaction of the plasma and the hydrocarbon generated in the discharge tube; . ≪ / RTI >

According to an embodiment of the present invention, the fixing portion may be formed to surround the discharge tube at a lower end of the discharge tube.

According to an embodiment of the present invention, the gas supply part includes a supply path formed in the fixed part, and one end of the supply path is connected to the inside of the discharge tube to discharge the mixed gas into the discharge tube Wherein the supply path includes at least one first supply path for supplying steam into the discharge tube; And at least one second supply path for supplying gas into the discharge tube are formed of the same number or a mixture of steam and gas may be supplied to one supply path.

According to an embodiment of the present invention, the gas supply unit may include a supply pipe disposed at an upper end, a lower end, or both of the discharge tubes.

According to an embodiment of the present invention, the gas supply unit may include a supply pipe connected to the discharge tube through the fixing unit.

According to an embodiment of the present invention, the supply pipe may include a supply pipe, one end of which is connected to the inside of the discharge pipe to spray a mixed gas into the discharge pipe, and the supply pipe includes a first supply pipe ; And a second supply pipe for supplying the gas into the discharge tube, or the steam and the gas may be mixed and supplied to one supply pipe.

According to an embodiment of the present invention, the reducing agent supply unit may further include a gas separator for separating impurities and gas from the produced synthesis gas, and a gas storage tank for storing the separated gas.

According to one embodiment of the present invention, the gas separator can separate the carbon powder and the hydrogen gas through the filter or the carbon powder and the hydrogen gas by the cyclone.

According to an embodiment of the present invention, the denitrification treatment unit may further include an oxidation catalyst, and the oxidation catalyst may be at least one selected from the group consisting of vanadium, nickel, cerium, rhodium, platinum, molybdenum, titanium, palladium and tungsten, And the oxidation catalyst may be one which is supported on aluminum oxide, zeolite, or silica carrier.

According to an embodiment of the present invention, the reducing agent supply unit may further include a water-gas shift reaction (WGSR) reactor for concentrating the hydrogen gas generated in the plasma hydrogen gas generator.

According to one embodiment of the present invention, the gas supply unit supplies at least one of air, oxygen, nitrogen, and argon gas, and the gas supply unit and the gas supply pipe can supply water vapor at 100 ° C or higher.

According to an embodiment of the present invention, the reducing agent supply unit further supplies at least one kind of plasma decomposition gas selected from the group consisting of ammonia, urea water, and ammonia water, and the plasma synthesis gas generating apparatus further includes at least one plasma decomposition gas generator can do.

Another aspect of the present invention is a method for producing a reducing agent, comprising: obtaining a reducing agent using plasma; Contacting the reducing agent with a gas containing NOx to denitrify; And discharging the denitrated gas; The present invention also relates to a method for treating a denitration process using plasma.

According to an embodiment of the present invention,

Obtaining hydrogen gas using a plasma; Contacting the hydrogen gas with a gas containing NOx to denitrify the hydrogen gas; And discharging the denitrated gas; . ≪ / RTI >

According to an embodiment of the present invention, a method of treating a denitration process using plasma includes the steps of: hydrogen gas; And at least one plasma decomposition gas selected from the group consisting of ammonia, urea water, and ammonia water; Respectively; The hydrogen gas; And at least one plasma decomposition gas selected from the group consisting of ammonia, urea water, and ammonia water; Contacting the NOx-containing gas with a gas containing NOx to denitrify the NOx-containing gas; And discharging the denitrated gas; . ≪ / RTI >

According to an embodiment of the present invention, the denitrification treatment method using plasma includes at least one kind of plasma decomposition gas selected from the group consisting of hydrogen gas, ammonia, urea water, and ammonia water using plasma. Respectively; Contacting the hydrogen gas with a gas containing NOx to perform a first denitration process; At least one plasma decomposition gas selected from the group consisting of ammonia, urea water, and ammonia water is added to the mixed gas generated after the first denitrification process; A second denitrification process is performed; And discharging the denitrated gas; . ≪ / RTI >

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According to an embodiment of the present invention, in the denitrification step, the reaction temperature may be from room temperature to 1000 ° C.

According to an embodiment of the present invention, plasma is used to decompose at least one of ammonia, urea water, and ammonia water; ; Contacting the plasma decomposition gas with a gas containing NOx in the presence of an oxidation catalyst to denitrify the plasma decomposition gas; And discharging the denitrated gas; . ≪ / RTI >

The present invention can provide a high purity hydrogen gas using plasma, and can provide a highly efficient denitrification effect at a low temperature by using hydrogen gas produced by plasma as a reducing agent in the denitration treatment.

An object of the present invention is to improve the denitrification effect by using a reducing agent in the denitration treatment of a plasma decomposition gas of a nitrogen compound decomposed using plasma, prolong the lifetime of the catalyst in a selective catalytic reduction (SCR) .

Fig. 1 is an exemplary view showing the structure of a denitration treatment system 1 according to an embodiment of the present invention.
FIG. 2 is an exemplary view showing a configuration of a denitration processing system 2 using plasma, according to another embodiment of the present invention.
FIG. 3 illustrates an exemplary configuration of a plasma hydrogen gas generator according to an embodiment of the present invention.
4 is a vertical cross-sectional view illustrating a connected portion of the waveguide 125 and the discharge tube 130 of the plasma hydrogen gas generator 110 according to an embodiment of the present invention.
5 is a horizontal cross-sectional view illustrating a detailed configuration of the gas supply unit 140 of the plasma hydrogen generator 110 according to an embodiment of the present invention.
6 is a horizontal cross-sectional view illustrating a detailed configuration of a hydrocarbon supply unit 150 of the plasma hydrogen generator 110 according to an embodiment of the present invention.
7 is a horizontal cross-sectional view illustrating a detailed configuration of the plasma hydrogen gas generator 110 according to an embodiment of the present invention.
8 is a horizontal cross-sectional view illustrating a detailed configuration of the gas supply pipe 145 of the plasma hydrogen gas generator 110 according to an embodiment of the present invention.
Fig. 9 exemplarily shows a configuration diagram of a denitration treatment system 3 according to another embodiment of the present invention.
10 to 14 illustrate a flow chart of a denitrification process using plasma, according to an embodiment of the present invention.
15 is a conceptual diagram illustrating a denitrification process using the denitration process according to the present invention in an LNG power generation system according to an embodiment of the present invention.

Hereinafter, embodiments of the present invention will be described in detail with reference to the accompanying drawings. In the following description of the present invention, detailed description of known functions and configurations incorporated herein will be omitted when it may make the subject matter of the present invention rather unclear. Also, terminologies used herein are terms used to properly represent preferred embodiments of the present invention, which may vary depending on the user, intent of the operator, or custom in the field to which the present invention belongs. Therefore, the definitions of these terms should be based on the contents throughout this specification. Like reference symbols in the drawings denote like elements.

The present invention relates to a denitrification system using plasma, and the denitrification system may include a reducing agent supply unit, a denitrification unit, and a gas discharge unit. The denitration treatment system will be described with reference to Figs. 1 to 9. Fig.

1, the denitrification unit 1 includes a reducing agent supply unit 100, a denitrification unit 100, a denitrification unit 100, (200) and a gas discharge unit (300). The reducing agent supply unit 100 generates a reducing agent for denitration treatment of the gas containing NOx, and supplies the reducing agent to the denitration processing unit 200. The reducing agent supply unit 100 produces a synthesis gas by using a plasma synthesis gas generator, and includes, for example, hydrogen gas; One or more plasma decomposition gases of ammonia, urea water, and ammonia water; Or both of them, and supplies them to the denitration treatment unit 200. For example, the plasma syngas generator may include one or more plasma hydrogen gas generators, one or more plasma decomposition gas generators, or both, or may generate hydrogen and plasma decomposition gases in one apparatus. Also, the plasma syngas generator may be a gasification or reforming (dry or wet) system.

The denitrification unit 200 performs a denitration process for the gas containing NOx with the reducing agent supplied from the reducing agent supply unit 100. The denitrification unit 200 generates a gas containing NOx in the denitrification unit 200, A gas containing NOx can be supplied from the outside. For example, the denitrification unit 200 may be a combustion tube of a boiler, an engine intake, an SNCR, an SCR processing unit, or the like, and may be supplied with a gas containing NOx such as a combustion gas, an exhaust gas and the like. The denitration treatment unit 200 further includes an oxidation catalyst (or a catalyst for reducing nitrogen oxides), wherein the oxidation catalyst is at least one selected from the group consisting of vanadium, nickel, cerium, rhodium, platinum, molybdenum, titanium, palladium and tungsten, Oxide, and the like. Preferably, the oxidation catalyst may be supported on an aluminum oxide, zeolite, or silica carrier, and may be vanadium / titanium oxide, platinum / palladium oxide, and the like.

The gas discharging unit 300 may further include a gas separator (not shown) for discharging the gas generated in the denitrification processing unit 200 and separating a desired gas to reuse the gas in various fields.

2 is a schematic diagram illustrating a denitration processing system 2 using a plasma according to another embodiment of the present invention. The denitration processing system 2 includes a plasma hydrogen A gas generator 110, a denitration unit 200, and a gas exhaust unit 300. The denitration processing unit 200 and the gas exhaust unit 300 are as described above. The plasma hydrogen gas generator 110 generates hydrogen gas from the reaction between the plasma and the hydrocarbon. The hydrogen gas is supplied to the denitration processing unit 200, and when used for the denitration treatment, the denitration reaction can be performed at a low temperature without a catalyst , And the denitrification performance can be improved.

3 illustrates a schematic diagram of a plasma hydrogen gas generator according to an embodiment of the present invention. Referring to FIG. 3, a plasma hydrogen gas generator 110 generates plasma using a plasma, The gas discharge unit 140, the hydrocarbon supply unit 150, the ignition unit 160, the gas discharge unit 170, and the gas discharge unit 170. [ And may include a fixing portion 180 (not shown).

The electromagnetic wave supply unit 120 generates electromagnetic waves and supplies them to the discharge tube 130 and includes a power source unit 121, an electromagnetic wave oscillator 122, a circulator 123, a tuner 124, and a waveguide 125.

The power supply unit 121 supplies power required for driving the plasma hydrogen gas generator 110.

The electromagnetic wave oscillator 122 is connected to the power supply unit 121 and receives power from the power supply unit 121 to oscillate the electromagnetic wave. For example, it is possible to use an electromagnetic wave oscillator that oscillates electromagnetic waves having a frequency range of 902 to 928 MHz or 886 to 896 MHz, and preferably oscillates an electromagnetic wave having a frequency of 915 MHz or 896 MHz by using the electromagnetic wave oscillator 122 .

The circulator 123 is connected to the electromagnetic wave oscillator 122 and outputs the electromagnetic wave oscillated by the electromagnetic wave oscillator 122 and also protects the electromagnetic wave oscillator 122 by destroying the electromagnetic wave energy reflected by the impedance mismatch.

The tuner 124 adjusts the intensity of the incident wave and the reflected wave of the electromagnetic wave output from the circulator 123 to induce impedance matching so that the electric field induced by the electromagnetic wave is maximized within the discharge tube 130.

The waveguide 125 transmits the electromagnetic wave input from the tuner 124 to the discharge tube 130. For example, the size of the waveguide 125 is related to the frequency of the electromagnetic wave oscillated by the electromagnetic wave oscillator 122, and as the frequency of the electromagnetic wave oscillated by the electromagnetic wave oscillator 122 becomes smaller, the wavelength becomes longer, When electromagnetic waves having different frequencies are introduced, electromagnetic waves having frequencies lower than the cutoff frequency inherent to the waveguide are not introduced into the waveguide. That is, the waveguide acts as a kind of high pass filter, so that the size of the waveguide is determined according to the frequency used.

When the discharge tube 130 is inserted at a position that is 1/4 of the wavelength λg from the end of the waveguide 125, the wavelength at the position where the discharge tube is inserted is about 11 cm (≈43.5 ÷ 4).

The discharge tube 130 generates a plasma from the electromagnetic wave supplied from the electromagnetic wave supply unit 120 and a mixed gas of steam and gas supplied from the gas supply unit 140 to gasify the hydrocarbon to generate syngas. The synthesis gas mainly consists of carbon monoxide (CO) and hydrogen (H2), and may further include impurities such as carbon powder and the like. The mixed gas of steam and gas injected into the discharge tube 130 stabilizes the generated plasma and forms a swirl in the discharge tube 130 to protect the inner wall of the discharge tube 130 from the high temperature plasma flame. Generally, it is very difficult to generate plasma by using only pure steam at atmospheric pressure. Even if it occurs, there is a problem that plasma is easily turned off. However, by using a mixed gas of steam and gas, Can be generated. In addition, it is possible to control the ratio of the hydrogen gas in the syngas produced by controlling the mixing ratio of the mixture of the steam (H2O) and the gas.

The gas supply unit 140 injects a mixed gas of steam and gas into the discharge tube 130 in a spiral shape. The gas supplies at least one of air, oxygen, nitrogen, and argon, preferably oxygen. The gas supply unit 140 can inject water vapor of 100 DEG C or higher, preferably 100 DEG C to 145 DEG C, more preferably 100 DEG C to 140 DEG C in a spiral form.

The hydrocarbon supply unit 150 supplies liquid, gas, or both hydrocarbons to the plasma generated inside the discharge tube 130.

The ignition unit 160 includes a pair of electrodes disposed inside the discharge tube 130 and supplies initial electrons for generating plasma through the electrodes.

The gas discharge part 170 is provided at the upper end of the discharge tube 130 and discharges the syngas produced by the plasma to the outside. For example, the gas discharging unit 170 supplies a syngas, that is, hydrogen gas to the denitrification unit 300 as a reducing agent for the denitration treatment.

4 is a vertical cross-sectional view illustrating a portion where a waveguide 125 and a discharge tube 130 of a plasma hydrogen gas generator 110 are connected to each other according to an embodiment of the present invention. 4 (a), the discharge tube 130 is connected to the waveguide 125 to provide a space in which plasma is generated by an electromagnetic wave input through the waveguide 125. The discharge tube 130 is formed in a cylindrical shape and is perpendicular to the waveguide 125 at a point corresponding to 1/8 to 1/2, preferably 1/4 of the wavelength of the waveguide 125 from the end of the waveguide 125 And may be made of quartz, alumina, or ceramics for easy transmission of electromagnetic waves. The discharge tube holder 131 formed below the waveguide 125 supports the discharge tube 130 so that the discharge tube 130 is stably inserted into the waveguide 125 and fixed. The fixing portion 180 is formed to surround the lower end of the discharge tube 130 and is made of a suitable material for supporting the discharge tube 130, and is preferably made of a carbon block. The gas supply section 140 includes a supply passage formed in the fixed section 180. The hydrocarbon supply unit 150 is formed to surround the plasma generation part at the upper end of the gas supply part 140, that is, the discharge tube 130.

The discharge tube 130 and the waveguide 125 are connected in the same manner as in FIG. 4B except that the discharge tube 130 is easily fixed and the discharge tube 130 protrudes outward at the lower end of the discharge tube 130 And a hooking jaw 131-1 is provided. The engaging protrusion 131-1 is interposed between the first carbon block 181 and the second carbon block 182 of the fixing portion 180 so that the first carbon block 181 and the second carbon block 182 And a case 183 is formed outside the first and second carbon blocks 181 and 182 so that the discharge tube 130 can be fixed. In this embodiment, the gas supply unit 140 includes a gas supply unit 140 including a supply path formed in the second carbon block 182, which supplies gas to the lower end of the discharge tube 130.

5 illustrates a horizontal cross-sectional view illustrating a detailed configuration of a gas supply unit 140 of a plasma hydrogen generator 110 according to an embodiment of the present invention. Referring to FIG. 5, The gas supply unit 140 of the plasma hydrogen gas generator 110 according to the embodiment includes at least one first supply path 141 and at least one second supply path 142. [ The first supply path 141 and the second supply path 142 are connected to one end of the discharge tube 130 to supply steam and gas into the discharge tube 130, respectively. The steam and the gas supplied to the first supply path 141 and the second supply path 142 are mixed in the discharge tube 130 to form a mixed gas of steam and gas. Alternatively, steam and gas may be mixed and supplied in one supply path.

The first supply path 141 and the second supply path 142 may be formed in an appropriate number in the gas supply part 140 as necessary. 5 (a) shows an embodiment in which the first supply path 141 and the second supply path 142 are formed one by one, FIGS. 5 (b) and 5 Two supply passages 142 are provided in each of two or three feed passages 142, respectively. As shown in the figure, the first supply path 141 and the second supply path 142 may be formed in the same number of the fixing portions 180 (i.e., the second carbon block 182), respectively. That is, when two first supply paths 141 are formed, two second supply paths 142 may be formed. The first supply path 141 and the second supply path 142 may be disposed at equal intervals around the discharge tube 130 in the fixed portion 180 (i.e., the second carbon block 182) The first supply passage 141 and the second supply passage 142 are alternately arranged in the gas supply section 140 (i.e., the first supply passage 141, the second supply passage 142, the first supply passage 141, ), The second supply path 142, and so on).

The first supply path 141 and the second supply path 142 are supplied to the discharge tube 130 so that the mixed gas of the supplied steam and gas is rotated in the form of a spiral along the inner peripheral surface of the discharge tube 130. The first supply path 141 and the second supply path 142 are formed in such a manner that steam and oxygen discharged into the discharge tube 130 flow along the inner circumferential surface of the discharge tube 130 The discharge tube 130 is connected to the inside of the discharge tube 130 so as to be discharged. The first supply path 141 and the second supply path 142 are disposed in the vicinity of one end where the first supply path 141 and the second supply path 142 are connected to the discharge tube 130, 130). In this case, the supplied steam and gas are mixed with each other inside the discharge tube 130 and rotate in one direction to form a vortex shape. The rotating direction of the steam and the gas supplied from the first supply path 141 and the second supply path 142 may be the same.

The hydrocarbon supply unit 150 of the plasma hydrogen generator 110 includes at least one hydrocarbon supply pipe 151 and is connected to the plasma formed in the discharge pipe 130 through the hydrocarbon supply pipe 151 as a gas, The two will be supplied. The hydrocarbon feed pipe 151 and the hydrocarbon feed pipe 151 may be formed in a suitable number in the hydrocarbon feed pipe 150 as required. Like the first feed pipe 141 and the second feed pipe 142, May be arranged at equal intervals around the discharge tube (130) within the discharge tube (150). For example, the hydrocarbon feed pipe 151 may be fed to the discharge pipe 130 so that the supplied hydrocarbon is rotated in the form of a spiral along the inner circumferential surface of the discharge pipe 130. 6 (a), the hydrocarbon feed pipe 151 is connected to the discharge pipe 130 so that the hydrocarbon discharged into the discharge pipe 130 is discharged along the inner circumferential surface of the discharge pipe 130 (that is, parallel to the inner circumferential surface) 130). The hydrocarbon feed pipe 151 and the discharge pipe 130 are connected to each other so that the proceeding direction of the hydrocarbon feed pipe 151 is connected to the end of the discharge pipe 130 It shall be constructed parallel to the inner circumferential surface. In this configuration, the supplied hydrocarbon rotates in one direction within the discharge tube 130 to form a swirling shape. At this time, it is preferable that the rotating direction of the vortex coincides with the rotating direction of the mixed gas of steam and gas.

As another example, as shown in FIG. 6 (b), the hydrocarbon supply pipe 151 may be formed so as to face the center portion of the plasma formed inside the discharge tube 130. In this case, the hydrocarbon injected through the hydrocarbon feed line 151 is injected directly toward the center of the high-temperature plasma, so that the partial combustion and gasification of the hydrocarbon can be more easily performed.

As a carrier gas for supplying hydrocarbon into the discharge tube 130, carbon dioxide (CO 2 ) or a mixed gas of oxygen and gas may be used in the same manner as the gas supply unit 140, and pure steam or oxygen It can also be used as a carrier gas. The syngas generated in the plasma hydrogen gas generator 110 contains a considerable amount of carbon dioxide in addition to hydrogen (H 2 ) and carbon monoxide. Therefore, when the carbon dioxide is separated from the syngas and recycled as a carrier gas for transferring the hydrocarbon fuel, the hydrocarbon can be effectively transferred to the plasma in the discharge tube 130 and also the environmental pollution due to the discharge of carbon dioxide into the air can be prevented It is effective.

According to another embodiment of the present invention, the plasma hydrogen gas generator 110 includes an electromagnetic wave supply unit 120, a discharge tube 130, a gas supply unit 140, an ignition unit 160, a hydrocarbon supply unit 150, 170 and a fixing portion 180. [ The electromagnetic wave supply unit 120, the discharge tube 130, the hydrocarbon supply unit 150, the ignition unit 160, and the gas discharge unit 170 are as described above. The gas supply unit 140 injects a mixed gas of steam and gas into the discharge tube 130 in a spiral shape and includes a supply pipe 145. The gas supplies at least one of air, oxygen, nitrogen, and argon, preferably oxygen. The gas supply unit 140 injects steam at a temperature of 100 占 폚 or higher, preferably 100 占 폚 to 150 占 폚, preferably 100 占 폚 to 145 占 폚, more preferably 100 占 폚 to 140 占 폚 in a spiral form.

The supply pipe 145 is disposed at the upper end, the lower end, or both of the discharge tube 130 so as to supply the mixed gas toward the discharge tube 130, and one end of the supply pipe 145 is connected to the inside And the mixed gas is injected into the inside of the discharge tube. For example, the supply pipe 145 includes a supply pipe 145 passing through the fixing portion 180 and connected to the discharge pipe 130, that is, a supply pipe 145 passing through the second carbon block 182 Or the supply pipe 145 includes a supply pipe 145 'which is connected to the discharge pipe 130 through the hydrocarbon supply part 150. [

7A and 7B illustrate a horizontal sectional view showing a detailed configuration of a plasma hydrogen gas generator 110 according to an embodiment of the present invention. The gas supply pipe 145 is disposed at the upper end of the discharge tube 130 and the gas supply pipe 145 is disposed at the upper end of the discharge tube 130. FIG. As shown in FIG.

The supply pipe 145 is disposed on the discharge tube 130 so as to incline toward the horizontal line L of the discharge tube 130 and one end of the one or more supply pipes 145 is connected to the inside of the discharge tube 130 Since the mixed gas is injected into the discharge tube 130, the gasification efficiency of the hydrocarbon can be increased. 7 (d) shows an embodiment in which the gas supply pipe 145 is arranged to be inclined upward toward the horizontal line L. FIG. 7 (e) shows an embodiment in which the gas supply pipe 145 is arranged at the lower end of the discharge tube 130, And the supply pipe 145 is disposed horizontally at the upper end of the discharge tube 130. Figure 7F shows an embodiment in which the supply pipe 145 is arranged horizontally at the lower end and the upper end of the discharge tube 130, ) Are arranged to be inclined upward and downward toward the horizontal line (L).

8 is a horizontal cross-sectional view illustrating a detailed configuration of a gas supply pipe 145 of a plasma hydrogen gas generator 110 according to an embodiment of the present invention. In FIG. 8, The supply pipe 145 of the plasma hydrogen generator 110 according to an embodiment of the present invention includes at least one first supply pipe 146 for supplying steam and at least one second supply pipe 147 for supplying gas. One end of each of the first supply pipe 146 and the second supply pipe 147 is connected to the inside of the discharge tube 130 to supply steam and gas into the discharge tube. The steam and the gas supplied to each of the first supply pipe 146 and the second supply pipe 147 can be mixed and supplied to the inside of the discharge tube 130 And mixed to form a mixed gas of steam and gas. The first supply pipe 146 and the second supply pipe 147 may be formed in an appropriate number as necessary. 8 (a) shows an embodiment in which the first supply pipe 146 and the second supply pipe 147 are formed one by one, and FIG. 8 (b) shows an example in which the first supply pipe 146 and the second supply pipe 147 are two Respectively. As shown, the first supply pipe 146 and the second supply pipe 147 may be formed in the same number, respectively. That is, when two first supply pipes 146 are formed, two second supply pipes 147 may also be formed. The first supply pipe 146 and the second supply pipe 147 may be arranged at equal intervals and the first supply pipe 146 and the second supply pipe 147 alternately (that is, the first supply pipe 146 ), A second supply pipe 147, a first supply pipe 146, a second supply pipe 147, and so on). The first supply pipe 146 and the second supply pipe 147 may be disposed at the same interval or at different intervals at the upper end and the lower end of the discharge tube 130. Further, the supply pipes disposed at the upper end and the lower end can be disposed apart from each other. 8 (c) shows an embodiment in which the supply tube 145 disposed at the lower end of the discharge tube 130 and the supply tube 145 'disposed at the upper end are provided at equal intervals, FIG. 8 (d) And the supply pipe 145 'disposed at the upper end are spaced apart from each other.

The first supply pipe 146 and the second supply pipe 147 are supplied to the discharge tube 130 so that the mixed gas of the supplied steam and gas rotates in the form of a spiral along the inner peripheral surface of the discharge tube 130. The first supply pipe 146 and the second supply pipe 147 are arranged in such a manner that steam and oxygen discharged into the discharge tube 130 are discharged along the inner circumferential surface of the discharge tube 130 And is connected to the inside of the discharge tube 130. The first supply pipe 146 and the second supply pipe 147 are moved in the direction of the inner peripheral surface of the discharge tube 130 in the vicinity of one end where the first supply pipe 146 and the second supply pipe 147 are connected to the discharge pipe 130, As shown in FIG. In such a case, the supplied steam and gas are mixed with each other in the discharge tube 130 to rotate in one direction to form a vortex shape. The rotation direction of the steam and the gas supplied from the steam supply pipe 146 and the gas supply pipe 147 may all be the same.

According to another embodiment of the present invention, FIG. 9 shows a denitration treatment system 3 according to another embodiment of the present invention. The denitration treatment system 3 includes a reducing agent supply unit 100, a denitrification unit 200, And a gas discharge unit 300. The reducing agent supply unit 100 may include a plasma hydrogen gas generator 110 and a plasma decomposition gas generator 111. [ The plasma hydrogen gas generator 110, the denitrification unit 200, and the gas discharge unit 300 are as described above. The plasma decomposition gas generator 111 has the same configuration as the plasma hydrogen gas generator 110 and supplies at least one of ammonia, urea water, and ammonia water to the discharge tube 130 in order to obtain a plasma decomposition gas, . The denitrification system 3 further includes a gas separator 113, a gas storage tank 114, and a WGSR 115. The gas separator 113 separates the mixed gas generated in the plasma gas generator 110. The gas separator 113 preferably separates impurities such as carbon powder and the hydrogen gas from the mixed gas generated in the plasma hydrogen gas generator 110 into a filter or a cyclone Separate.

The gas storage tank 114 may store the gas separated by the gas separator 113 and adjust the supply amount appropriately when supplied to the denitration processing unit 200, if necessary.

The WGSR (Water-Gas Shift Reaction) reactor 115 concentrates the hydrogen gas generated in the plasma hydrogen gas generator 110. The concentrated hydrogen gas in the reducing agent supply unit 100 may be supplied to the denitration processing unit 200 or may be stored in the gas storage tank 114 via the gas separator 113.

The present invention relates to a denitration treatment method using plasma. The above method uses a denitrification system using plasma according to the present invention. According to one embodiment of the present invention, FIGS. 10 to 14 illustrate a flow chart of a denitrification method using plasma according to an embodiment of the present invention, including: obtaining a reducing agent (S100); Denitrification treatment (S200); And discharging gas (S300); . ≪ / RTI >

The step of obtaining a reducing agent (S100) is a step of obtaining a reducing agent by using a plasma, and the present invention is a step of obtaining a reducing agent by using a plasma synthesis gas generator in a reducing agent supply unit (100) , Hydrogen gas; At least one plasma decomposition gas selected from the group consisting of ammonia, urea water, and ammonia water; Or both.

In the denitrification process (S200), the reducing agent is contacted with a gas containing NOx to denitrify.

The step of discharging the gas (S300) is a step of discharging the generated mixed gas after the denitration processing (S200).

In an embodiment of the present invention, the denitration treatment method using plasma in FIG. 11 includes: obtaining hydrogen gas using plasma (S100a); (S200a) denitrating the hydrogen gas by contacting the gas containing NOx; And discharging the denitrified gas (S300a). The denitrification process (S200a) is a process for denitrating the NOx-containing gas without using a catalyst using hydrogen gas. In other words, hydrogen gas acts as SNCR, and denitrification is possible at low temperature.

In an embodiment of the present invention, a denitration treatment method using plasma in FIG. And at least one plasma decomposition gas selected from the group consisting of ammonia, urea water, and ammonia water; (100b), respectively; The hydrogen gas; And at least one plasma decomposition gas selected from the group consisting of ammonia, urea water, and ammonia water; (200b) denitrifying the NOx-containing gas in contact with the NOx-containing gas; And discharging the denitrated gas (300b); . ≪ / RTI > The step 200b of performing denitrification by contacting with a gas is a step of denitrifying the NOx-containing gas without using a catalyst using hydrogen gas. The plasma decomposition gas is applied as a carrier gas for carrying the hydrogen gas, The efficiency of the treatment can be further improved. The denitrification process 200b may further include an oxidation catalyst, and the amount of the expensive oxidation catalyst may be smaller than that of the prior art, so that the cost of denitrification is lowered, The efficiency can be increased.

In an exemplary embodiment of the present invention, a denitration process using plasma in FIG. And at least one plasma decomposition gas selected from the group consisting of ammonia, urea water and ammonia water; (100c), respectively; (200c) of contacting the hydrogen gas with a gas containing NOx to perform a first denitration process; At least one plasma decomposition gas selected from the group consisting of ammonia, urea water, and ammonia water is added to the mixed gas generated after the first denitrification process; (300c) a second denitrification process by contacting the first denitration process; And discharging the denitrated gas (400c); . ≪ / RTI > In the first denitrification process 200c, since the hydrogen gas acts as the SNCR, the denitration process without the catalyst and the second denitration process 300c are performed by moving the gas to the catalyst layer after the first denitration process, Denitrification treatment is performed. The first denitration treatment step 200c and the second denitration treatment step 300c are performed at a reaction temperature of from room temperature to 1000 ° C and preferably the first denitration treatment step 200c is performed at a reaction temperature of room temperature to 100 ° C And the second denitrification process 300c may be performed at a reaction temperature of 100 ° C to 500 ° C.

In one embodiment of the present invention, a denitration treatment method using plasma in FIG. 14 is a method of treating a plasma using a plasma, wherein at least one plasma decomposition gas among ammonia, urea water, and ammonia water; Gt; 100d < / RTI > (200d) denitrifying the plasma decomposition gas in the presence of an oxidation catalyst by contacting it with a gas containing NOx; And discharging the denitrated gas (300d); . ≪ / RTI > The oxidation catalyst is as mentioned above. When applied to the denitration treatment of the plasma decomposition gas, the lifetime of the oxidation catalyst, that is, the SCR can be extended and the efficiency can be increased.

delete

In the denitrification step of the present invention, the reaction temperature may be from room temperature to 1000 ° C, preferably from room temperature to 200 ° C when hydrogen gas is applied; Room temperature to 150 캜; Room temperature to 100 캜; Lt; 0 > C to 80 < 0 > C.

According to an embodiment of the present invention, the method of treating a denitration using plasma according to an embodiment of the present invention can be applied to denitrification of nitrogen oxides generated by a combustion reaction, oxidation of nitrogen, and the like. For example, An internal combustion engine for power generation of solid fuel or gaseous fuel, an incinerator, an incinerator boiler, and the like. 15 is a conceptual diagram illustrating a denitrification process using the denitration process according to the present invention in an LNG generation system according to an embodiment of the present invention. The LNG of the power generation system is reformed in a plasma hydrogen gas generator to generate hydrogen gas to denitrify the mixed gas and to introduce the plasma decomposition gas into the catalyst layer of the SCR to perform the second denitrification process. The introduced plasma decomposition gas can extend the lifetime of the catalyst layer of the SCR and improve the reaction efficiency.

Claims (21)

A reducing agent supply unit including a plasma synthesis gas generator;
A denitration unit for denitrating the NOx-containing gas with the reducing agent provided from the reducing agent supply unit; And
A gas discharge unit for discharging the denitration treated gas;
Lt; / RTI >
The reducing agent supply unit supplies hydrogen gas,
Wherein the plasma synthesis gas generator comprises at least one plasma hydrogen gas generator,
Wherein the plasma hydrogen gas generator comprises:
An electromagnetic wave supply unit for generating electromagnetic waves of a predetermined frequency;
A discharge tube in which a plasma is generated from the electromagnetic wave and a mixed gas of steam and gas supplied from the electromagnetic wave supply unit;
A fixing unit fixing the lower end of the discharge tube;
A gas supply unit for injecting a mixed gas of steam and gas into the discharge tube in a spiral shape;
A hydrocarbon supply unit supplying a liquid, a gas, or both hydrocarbons to the plasma generated inside the discharge tube;
An ignition unit for supplying initial electrons for plasma generation to the inside of the discharge tube; And
A gas discharge unit for discharging the synthesis gas synthesized from the reaction between the plasma generated by the discharge tube and the hydrocarbon; Lt; / RTI >
Wherein the reducing agent supply unit further comprises a WGSR reactor (Water-gas shift reaction) for concentrating the hydrogen gas generated in the plasma hydrogen gas generator.
delete delete The method according to claim 1,
Wherein the fixing portion is formed to surround the discharge tube at a lower end of the discharge tube.
The method according to claim 1,
Wherein the gas supply portion includes a supply passage formed in the fixed portion,
Wherein one end of the supply path is connected to the inside of the discharge tube to spray the mixed gas into the discharge tube,
Wherein the supply path includes at least one first supply path for supplying steam into the discharge tube; And at least one second supply path for supplying gas into the discharge tube are formed in the same number or a mixture of steam and gas is supplied to one supply path.
The method according to claim 1,
Wherein the gas supply unit includes a supply pipe disposed at an upper end, a lower end, or both of the discharge tubes.
The method according to claim 1,
Wherein the gas supply unit includes a supply pipe connected to the discharge tube through the fixing unit.
8. The method according to claim 6 or 7,
Wherein the supply pipe has one end of the supply pipe connected to the inside of the discharge pipe to inject a mixed gas into the discharge pipe,
Wherein the supply pipe includes: a first supply pipe for supplying steam into the discharge pipe; And a second supply pipe for supplying gas to the inside of the discharge tube are constituted by the same number or a mixture of steam and gas is supplied to one supply pipe.
The method according to claim 1,
Wherein the gas supply unit supplies at least one gas of air, oxygen, nitrogen, and argon gas,
Wherein the gas supply unit supplies steam at 100 DEG C or higher.
The method according to claim 1,
Wherein the reducing agent supply unit further comprises a gas separator for separating impurities and gas from the produced syngas, and a gas storage tank for storing the separated gas.
11. The method of claim 10,
Wherein the gas separator separates carbon powder and hydrogen gas through a filter or separates carbon powder and hydrogen gas by a cyclone.
The method according to claim 1,
Wherein the denitrification treatment unit further comprises an oxidation catalyst,
Wherein the oxidation catalyst comprises at least one of vanadium, nickel, cerium, rhodium, platinum, molybdenum, titanium, palladium and tungsten, and oxides thereof,
Wherein the oxidation catalyst is supported on an aluminum oxide, zeolite, or silica carrier.
delete The method according to claim 1,
Wherein the reducing agent supply unit further supplies at least one kind of plasma decomposition gas selected from ammonia, urea water, and ammonia water,
Wherein the plasma synthesis gas generator further comprises at least one plasma decomposition gas generator.
Obtaining a reducing agent using plasma;
Contacting the reducing agent with a gas containing NOx to denitrify; And
Discharging the denitrated gas; Lt; / RTI >
In the denitrification step, the reaction temperature is from room temperature to 400 ° C,
A denitration treatment system using the plasma of claim 1 is used.
A method of denitrification treatment using plasma.
16. The method of claim 15,
The denitration treatment method using the plasma includes:
Obtaining hydrogen gas using a plasma;
Contacting the hydrogen gas with a gas containing NOx to denitrify the hydrogen gas; And
Discharging the denitrated gas; Wherein the denitration treatment is performed using a plasma.
16. The method of claim 15,
The denitration treatment method using the plasma includes:
Hydrogen gas using plasma; And at least one plasma decomposition gas selected from the group consisting of ammonia, urea water, and ammonia water; Respectively;
The hydrogen gas; And at least one plasma decomposition gas selected from the group consisting of ammonia, urea water, and ammonia water; Contacting the NOx-containing gas with a gas containing NOx to denitrify the NOx-containing gas; And
And a step of discharging the denitration-treated gas.
16. The method of claim 15,
The denitration treatment method using the plasma includes:
A plasma decomposition gas of at least one of hydrogen gas, ammonia, urea water, and ammonia water using plasma; Respectively;
Contacting the hydrogen gas with a gas containing NOx to perform a first denitration process;
Contacting the mixed gas produced after the first denitrification process with at least one plasma decomposition gas selected from the group consisting of ammonia, urea water, and ammonia water to perform a second denitrification process; And
Discharging the denitrated gas; Wherein the denitration treatment is performed using a plasma.
delete 16. The method of claim 15,
The denitration treatment method using the plasma includes:
At least one plasma decomposition gas of ammonia, urea water, and ammonia water using plasma; ;
Contacting the plasma decomposition gas with a gas containing NOx in the presence of an oxidation catalyst to denitrify the plasma decomposition gas; And
Discharging the denitrated gas; Wherein the denitration treatment is performed using a plasma.
delete
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