Method of reducing nitrogen oxide content in gas

Abstract: A method of reducing a nitrogen oxide content in gas is disclosed. In this method, subject gas containing nitrogen oxide is supplied to a gas passage (2) of a surface discharger (1) to decompose the nitrogen oxide content in the gas into nitrogen gas.

Description: The present invention relates to a method of reducing nitrogen oxide content present in a gas such as a combustion exhaust gas from an engine, a boiler, an incinerator or the like, and more particularly to a method of decomposing the nitrogen oxide into nitrogen gas by means of an electric discharge into the gas containing the nitrogen oxide. As a method of reducing nitrogen oxide content by means of an electric discharge, it is known to use a corona discharger for decomposing the nitrogen oxide into nitrogen gas (e.g. the Japanese laid-open patent gazette No. Hei 2-191525). A further known method is illustrated in Fig. 7. In this method, subject gas is supplied to a gas passage 2 of a glow discharger 1' including a pair of electrodes 6, 7 opposing to each other across the gas passage 2 and a dielectric layer 4' formed on an opposing surface of at least either of the pair of electrodes 6, 7, so as to decompose the nitrogen oxide into nitrogen gas. With either of the above-described conventional methods, decomposition of the nitrogen oxide content is to be effected by means of electric discharge into the atmosphere across the gas passage. For this reason, these conventional methods suffer problems to be described next. In the case of a combustion exhaust gas from an engine, a typical nitrogen-oxide containing gas, the content of nitrogen oxide varies in accordance with variation in engine load. Similarly, in the case of a combustion exhaust gas from an incinerator, the content varies in accordance with the kind of objects incinerated in the incinerator. As a result, the condition between the electrodes, i.e. the insulation condition within the gas passage changes at every moment with continuous supply of the gas. Therefore, with the atmospheric discharge traversing the combustion exhaust gas flow, the discharge condition also varies in accordance with the variation in the insulation condition. Therefore, it is impossible to provide a constant amount of energy for effective decomposition of the nitrogen oxide. Consequently, decomposing performance deteriorates. Moreover, if an excessive amount of energy is supplied, the excess energy may even oxide NO (which makes up the largest portion of the nitrogen oxide present in the gas) into NO 2 . Further, the atmospheric discharge is effected at a great number of electrodes distributed throughout the gas passage from its entrance to exit, the gas introduced through the entrance experiences the discharging operations for a plurality of times to receive an additional amount of energy with each discharging operation. Accordingly, in the case of the combustion exhaust air which has oxygen content, the above-described oxidation reaction (NO + O) of NO into NO 2 is very likely to occur. As described above, the conventional methods can not provide good efficiency in the reduction of nitrogen oxide content by decomposing the oxide into nitrogen gas. Also, because of the problem of oxidation of NO into NO 2 , a post treatment was necessary for treating this NO 2 . As a result, the conventional methods suffer high initial and running costs. The WO-A-92/19361 (published 12.11.92) describes a method to oxidize pollulants containing NOx compounts and to prevent the formation of new NOx pollulants with an electric glow dicharger (silent discharger). A primary object of the present invention is to provide an improved method of reducing nitrogen oxide content in gas which method can eliminate the necessity of post treatment of NO 2 thereby to provide a cost advantage. A method for accomplishing the above-noted object is characterized in claim 1. According to the method of the present invention, the decomposing process, i.e. N-radical reaction: N + NO → 1/2O 2 is effected by applying energy to the subject gas through a surface discharging operation. The discharging operation takes place in a constant and stable manner without being affected by change in the inter-electrode insulation condition due to variation in the composition of the subject gas. Moreover, since the discharging operation of the method of the invention is a surface discharging operation, it is possible to provide the gas passage with an electrical continuity throughout from its entrance to exit without any discontinuities between adjacent electrodes. With this, the occurrence of oxidation reaction, i.e. (NO + O → NO 2 ), can be minimized. According to a preferred embodiment of the present invention, in addition to the subject gas, a reducing gas for the nitrogen oxide is supplied to the gas passage of the surface discharger. This feature has the advantage of further improving the decomposing efficiency. Specifically, in case ammonium gas is employed as the reducing gas, there occurs the reaction of: (NO + NH 2 → N 2 + H 2 O). In case hydrocarbon gas is employed as the reducing gas, there occurs the reaction of: (4CH + 6NO → 4CO + 3N 2 + 2H 2 O). In case hydrogen gas is employed as the reducing gas, there occurs the reaction of: (3H + 2NO → N 2 + OH + H 2 O). As described above, according to the method of the present invention, it is possible to improve the efficiency in reducing nitrogen oxide in gas by decomposing the nitrogen oxide into nitrogen gas and also to minimize the oxidation reaction of (NO + O → NO 2 ) to eliminate any post treatment for NO 2 and consequently to achieve significant cost reduction in the decreasing operation of nitrogen oxide. According to a further embodiment of the present invention, radicals of the reducing gas for the nitrogen oxide are produced and then these radicals are introduced into the subject gas containing the nitrogen oxide so as to decompose the nitrogen oxide into nitrogen gas. For producing the radicals, the reducing gas is supplied to the gas passage of the surface discharger. In this case, it is possible to use air or nitrogen gas, in addition to the ammonia gas, the hydrogen carbon, the hydrogen gas. And, the N-radicals produced through the discharge cause the reaction of: (N + NO → N 2 + 1/2O 2 ). With the above method, the radicals are produced by providing energy to the reducing gas through the discharging operation. Accordingly, this method has the advantage that the application of the energy to the reducing gas can be completed instantaneously whereby the gas passage can be of a very short length to restrict surface reaction. Further, since the application of the energy is effected not by the atmospheric discharging operation but by the surface glow discharging operation which can take place in a very stable manner on the discharging portion formed on the dielectric layer without being influenced by the gas, the production of the radicals can be effected very stably. As described above, according to the above of the present invention, radicals of the reducing gas can be produced in an efficient manner and by causing the radicals to react with nitrogen oxide the reduction of the nitrogen oxide into nitrogen gas can be effected at lower costs and at a higher efficiency. The invention will become more apparent from the following more detailed description of the embodiments of the invention with reference to the accompanying drawings. BRIEF DESCRIPTION OF THE DRAWINGS Fig. 1 is a block diagram, Fig. 2 is a vertical section showing major portions of a surface discharger, Fig. 3 is a section showing the major portions of the surface discharger, Fig. 4 is a graph illustrating a relationship between NO and a discharge voltage, Fig. 5 is a block diagram illustrating a further embodiment, Fig. 6 is a block diagram, and Fig. 7 is a principle diagram of a conventional discharger. As illustrated in Fig. 1, according to a method of the invention, subject gas G containing nitrogen oxide is supplied to a gas passage 2 (see Figs. 2 and 3) of a surface discharger 1 to cause a reaction of: (2NO + e → N 2 + O 2 ). That is, the method decomposes (reduces) the nitrogen oxide into nitrogen gas. The surface discharger 1, as shown in Figs. 2 and 3, includes a cylindrical inner dielectric member 3 formed of glass and a cylindrical outer dielectric member 4 formed of ceramic. The inner and outer dielectric members 3, 4 are disposed between a pair of holders 5A, 5B to form the gas passage 2 between the inner and outer dielectric members 3, 4. On an inner peripheral surface of the outer dielectric member 4, there are provided a plurality of line-like discharge electrodes 6 extending along a longitudinal axis of the discharger, with the electrodes 6 being spaced apart from each other in a peripheral direction of the cylindrical member 4. On an outer peripheral surface of this outer dielectric member 4, there is provided a cylindrical dielectric electrode 7 to cover this outer peripheral surface. Further, an outer peripheral surface of the dielectric electrode 7 is covered with a cylindrical dielectric member 8 formed of ceramics. One holder 5A forms a gas entrance 2a of the gas passage 2 and the other holder 5B forms a gas exit 2b. The diameter of the gas exit 2b can vary conveniently. It should be noted, however, that the radicals of the reducing gas can become inactive if the exit diameter is too small. Therefore, the diameter should be large enough not to cause this inconvenience. The position of forming the gas exit 2b is not limited to that shown in Fig. 2. For instance, the exit can alternately be formed to be opened towards a right side end of the discharger. The introduction of the gas G is effected along a tangential direction of the gas passage 2 so as to cause the introduced gas G to flow with a spiral movement within the gas passage 2. A reference mark 6a denotes a high-voltage terminal for the discharge electrodes 6. A mark 7a denotes a ground terminal for the dielectric electrode 7 and this terminal extends through the thickness of the cylindrical dielectric member 8. A reference numeral 11 denotes a glaze film (protection film). Incidentally, the plurality of discharge electrodes 6 are connected with each other at longitudinal ends thereof through an unillustrated line extending in the peripheral direction. That is, these electrodes 6 are parallel connected. In operation of the surface discharger 1, through application of an alternating voltage by the discharging electrodes 6 and the dielectric electrode 7, a glow discharging portion is formed along the inner peripheral surface of the cylindrical outer dielectric member 4 so as to cause the reaction of: (2NO + e → N 2 + O 2 ). The cylindrical outer dielectric member 4 has an inner diameter D1 of 6 mm and a thickness t1 of 0.5 mm. The length of the cylindrical inner dielectric member 3, i.e. the length L of the gas passage 2 in which the surface discharging portion is formed by the discharging electrodes 6 and the dielectric electrode 7, is 300 mm. The gas passage 2 has a thickness t2 of 3mm, and the cylindrical dielectric member 8 has a thickness t3 of 1.5 mm. In order to confirm the effects of the method of the above-described embodiments, the present inventor conducted experiments. In these experiments, the employed surface discharger 1 has the dimensional characteristics described above. Experiment 1 Combustion exhaust gas containing 560 ppm of NOx, 1.0 % of O 2 and the rest of N 2 was supplied as the subject gas G to the discharger. A discharging voltage of 6.7 kV was applied to the discharge electrodes 6 and the dielectric electrode 7. And, the NOx concentration was measured at the gas passage exit. The measurement showed 140 ppm NOx concentration. Experiment 2 Gas containing NO and O 2 was supplied to the discharger. And, a relationship between the discharging voltage and the amount of reduction from NO to N 2 was observed. The result is illustrated in Fig. 4. The result shows that the reduction takes place in the range of discharging voltage between 4.5 and 9 kV. A further embodiment of the present invention will be described next. In this further embodiment, as illustrated in Fig. 5, together with the subject gas G, a reducing gas Ga for the nitrogen oxide is supplied to the surface discharger 1. In this embodiment, in addition to the aforementioned reaction of: (2NO + e → N 2 + O 2 ), in case ammonium gas is employed as the reducing gas, there occurs the reaction of: (NO + NH 2 → N 2 + H 2 ). In case hydrocarbon gas is employed as the reducing gas, there occurs the reaction of: (4CH + 6NO → 3N 2 + 4CO + 2H 2 O). In case hydrogen gas is employed as the reducing gas, there occurs the reaction of: (3H + 2NO → N 2 + OH + H 2 O). For confirming the effects of the method of this further embodiment, the inventor conducted experiments to be described next. Experiment 3 Combustion exhaust gas from a diesel engine containing 1040 ppm of NOx, 11.9 % of O 2 and 6.9 % of CO 2 was supplied as the subject gas G to the discharger. As the reducing gas, ammonium gas was supplied. A discharging voltage of 5 kV was applied to the discharge electrodes 6 and the dielectric electrode 7. And, the NOx concentration was measured at the gas passage exit. The measurement showed 480 ppm NOx concentration. In this embodiment, the same surface discharger 1 as the foregoing embodiment was used. A still further embodiment will be described next. In a method of this embodiment, as illustrated in Fig. 6, reducing gas Ga for nitrogen oxide is supplied to the gas passage 2 of the surface discharger 1 to produce radicals R of the reducing gas Ga. And, these radicals R are guided to a mixing reactor 12 to be introduced into the subject gas G to decompose the nitrogen oxide into nitrogen gas. The reducing gas Ga can comprise e.g. ammonia gas, hydrogen gas, nitrogen gas, air or the like. In case, ammonia gas is employed as the reducing gas Ga, there occurs the reaction of: (NO + NH 2 → N 2 + H 2 O) at the mixing reactor 12. In case nitrogen gas is employed as the reducing gas Ga, there occurs the reaction of: (2NO + 2N → 2N 2 + O 2 ) at the mixing reactor 12. The employed surface discharger 1 is the one shown in Figs. 2 and 3. For confirming the effects of the method of this embodiment, the inventor conducted further experiments to be described next. The surface discharger 1 employed in these experiments was the one having the above-described dimensional characteristics. Experiment 4 Gas containing 400 ppm of NOx and 5 % of O 2 was supplied as the subject gas G to the mixing reactor 12. Ammonia gas was supplied as the reducing gas Ga to the surface glow discharger 1. The, measurement was made of NOx concentration of the exhaust gas from the mixing reactor 12. The measurement showed a concentration of 180 ppm. Experiment 5 Gas containing 400 ppm of NOx and not containing any O 2 was supplied as the subject gas G to the mixing reactor 12, and ammonia gas was supplied as the reducing gas Ga to the surface discharger 1. Then, the NOx concentration was measured on the exhaust gas from the mixing reactor 12. The measurement showed a concentration value of 10 ppm. Incidentally, in the surface discharger 1 employed in all the foregoing embodiments, the charger includes the plurality of discharge electrodes 6 disposed in parallel with each other. Alternately, these discharge electrodes 6 can be disposed in a spiral format along the inner peripheral surface of the cylindrical outer dielectric member 4. Experiment 6 Air: O.8 Nm 3 /h was passed through silica gel to be rendered into dry air. And, this dry air was passed through the surface discharger to experience a discharging treatment (75 V, 0.4 A) and then was mixed with 10 Nm 3 /h of exhaust gas which contained 300 ppm of NO, 10 % of O 2 and 5 % of water vapor. It was observed that the resultant exhaust gas after the mixing contained 100 ppm of NO 2 , 15 ppm of NO (NO 2 + NO = 115 ppm). Thus, the process achieved the elimination ratio of 61.7 %. In the above, the air after the discharging operation contained 4000 ppm of O 3 which is substantially equal in mol to the NO content in the exhaust gas. Experiment 7 With the same surface discharger employed in the above-described experiment 3, its discharging amount (140 V, 0.7 A) was increased to substantially double the amount of ozone to be produced to 8,000 ppm. And, the resultant ozone was mixed into the exhaust gas described in the experiment 3. The measurements on this exhaust gas were 50 ppm of NO 2 , 10 ppm of NO (NO 2 + NO = 60 ppm), i.e. an elimination ratio of 80 %.

Claims: Method of reducing nitrogen oxide content in a subject gas by means of an electric glow discharger where the subject gas is supplied to a gas passage of the discharger to decompose the nitrogen oxide content in the gas into nitrogen gas characterized in that the employed glow discharger is a surface discharger having a plurality of linelike spaced electrodes extending along the longitudinal axis, or in a spiral format along one peripheral surface of the surface discharger. A method according to claim 1, characterized by the step of: supplying reducing gas (Ga) for the nitrogen oxide to said gas passage (2) of the surface discharger (1) together with said subject gas (G). A method according to claim 2, characterized in that said reducing gas (Ga) comprises at least one selected from the group consisting of ammonia gas, hydrocarbon gas, and hydrogen gas. A method of reducing a nitrogen oxide content in gas by means of all electric glow discharger, the method having the steps of: producing radicals (R) of a reducing gas (Ga) for nitrogen oxide content, and then supplying said radicals (R) to subject gas (G) contained in a separate reactor and containing the nitrogen oxide to decompose said nitrogen oxide content into nitrogen gas; characterized in that the method further has the step of supplying said reducing gas (Ga) to a gas passage (2) of a surface discharger (1) to produce said radicals (R), and that the employed glow discharger is a surface discharger having a plurality of linelike spaced electrodes extending along the longitudinal axis, or in a spiral format along one peripheral surface of the surface discharger. A method according to claim 4, characterized in that said reducing gas (Ga) comprises at least one selected from the group consisting of ammonia gas, hydrocarbon gas, hydrogen gas, nitrogen gas and air.

Inventors: KITOH SHIGEHIRO, MASUDA SENICHI, SAIKI SHIGEO, SAKAKIBARA KAICHI, KITOH, SHIGEHIRO, MASUDA, SENICHI, SAIKI, SHIGEO, SAKAKIBARA, KAICHI
Applicants: JAPAN MARINE MACH DEV ASS, MASUDA RESEARCH INC, TAKUMA KK, JAPAN MARINE MACHINERY DEVELOPMENT ASSOCIATION, MASUDA RESEARCH, INC., TAKUMA CO., LTD.
Application year: 1992
Main classification: B01D53
IPC codes: C07C205, B01D53, C07B63, C07C37, C07C201, B01J19, C07C39, B01D9