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Burner for generating reductive atmosphere of exhaust gas in engine cogeneration plant having denitrification processBurner for generating reductive atmosphere of exhaust gas in engine cogeneration plant having denitrification process description/claimsThe Patent Description & Claims data below is from USPTO Patent Application 20090120080, Burner for generating reductive atmosphere of exhaust gas in engine cogeneration plant having denitrification process. Brief Patent Description - Full Patent Description - Patent Application Claims Applicant claims foreign priority under Paris Convention and 35 U.S.C. §119 to Korean Patent Application No. 10-2007-0114984, filed Nov. 12, 2007 with the Korean Intellectual Property Office, where the entire contents are incorporated herein by reference. 1. Field of the Invention The present invention relates to a burner for generating a reductive atmosphere of exhaust gas in an engine cogeneration plant having a denitrification process, which is to produce a catalyst activation condition to remove nitrogen oxides from the engine exhaust gas in the engine cogeneration plant using a lean burn engine. More specifically, the present invention relates to a burner for stable combustion, in which one or more auxiliary burners are installed in a post-combustion burner installed in a boiler of an engine cogeneration plant. 2. Background of the Related Art In general, an internal combustion engine is described by a motive power where fuel is supplied into a cylinder and then the fuel is burned and exploded to generate a gas, of which expansion force is utilized to move a piston. A boiler is described by an apparatus that produces high-pressure steam or hot water by heating water, and is mainly used in a heating facility, a bathhouse, and as an industrial heat source for turbine driving, and the like. In the above cogeneration plant, fuel and oxygen are supplied to an internal combustion engine 1 to generate electricity, and the heat of exhaustion gas is used to produce steam. Here, the combustion exhaust gas stream is recovered from the internal combustion engine 1 at about 500 to 1000° F. and contains about 6 to 15% of oxygen. The stream having sufficient fuel is supplied a thermal reaction means required to react the fuel, nitrogen oxides and available oxygen, thereby generating a reduced oxygen stream. The reduced oxygen stream is cooled inside a heat exchanger. Depending on reduction condition, conversion oxygen is supplied to the cooled stream before being supplied to the catalyst bed. The oxygen may be provided directly with air. More preferably, the oxygen may be supplied after being discharged from the internal combustion engine 1 and passing through the exhaust stream channel. The conversion oxygen stoichiometrically exceeds the amount of nitrogen oxygen, but is less than the amount of combustible materials. According to the result, the nitrogen oxides inside the stream are treated into nitrogen dioxide at the final end portion before the catalyst bed. Thereafter, the nitrogen dioxide is reduced at the remaining portion of the catalyst bed 6 due to excessive combustible materials. The stream, where the amount of nitrogen oxide is considerably reduced, is discharged. The exhaust gas discharged from the internal combustion engine 1 is transferred to a thermal reactor such as the post-burner 3 and burned at 1800 to 3200° F., preferably 2000 to 2400° F. Gaseous harmful substances have 1800 to 3200° and contains about 750 ppmv of nitrogen oxides. The above stream passes through a heat exchanger. The harmful substance is cooled to about 600 to 1050° F., preferable 750 to 900° F. The values corresponding to the exhaust stream are obtained at the boiler 4, and steam is produced accordingly. The exhaust gas discharged from the boiler, which contains sufficient fuel and cooled, is mixed with a desired amount of conversion oxygen before passing through the catalyst bed 5 and added to the duct 9 at 14. As described above, the oxygen is added directly to the air supplier 14, but may be added through a desired channel of the engine exhaust unit from the duct 11 via a line 13. Due to this construction, the amount of oxygen injected to the post-burner 3 can be reduced. Therefore, the amount of fuel required to the post-burner can be reduced. The important purpose of conversion oxygen is accomplished, depending on the mixture injected into the catalyst bed 5. In particular, the amount of conversion oxygen added to the cooled steam from the boiler 4 exceeds that of nitrogen oxides within the stream, but is less than the combustible substances within the stream. In general, the added oxygen is about 20.2 to 0.9%. The nitrogen oxides in the line 9 are in the form of nitrogen monoxide. The mixture is injected through the front end portion of the catalyst bed 5, where the oxygen is reacted with nitrogen monoxide to be converted in the form of nitrogen dioxide. The amount of oxygen within the duct 16, which is placed under the catalyst bed 6, is 1.5 to 3%. The value of the nitrogen oxides within the duct 16 is 15 ppmv and the carbon monoxide is reduced to below 50 ppmv. The oxidized gaseous harmful substances discharged from the catalyst bed 6 are transferred to the fuel saving unit 7 or the low pressure waste heat boiler from the duct 16. The cooled gas having about 300 to 400° F. is input to the chimney 8 via the discharge duct 17 and discharged to the atmosphere. The nitrogen oxides being discharged are below 15 ppmv and the carbon monoxide is below 50 ppmv. According to a technique disclosed in Korean Patent Publication No. 10-0667223, fuel is supplied to a combustion chamber 21 while being mixed again and combusted therein. Flame generated in the combustion chamber 21 is re-circulated inside the combustion chamber 21 and incompletely combusted fuel is burned by a choke 23, thereby saving energy and improving heat efficiency of the boiler. In addition, as the prior art related to the present invention, Korean Patent Publication No. 10-0253991 discloses a method of reducing nitrogen oxides in a boiler, which is a low pollution type burner. According to this technique, the fuel nozzle of a low nitrogen oxide burner, which is disposed in the upper end row of the burner unit, is replaced to increase the amount of fuel being sprayed, or the size of the nitrogen oxide burner is reduced to decrease the amount of combustion air being sprayed. However, in the conventional techniques, the exhaust gas from an internal combustion engine is mixed with oxygen and supplied to a burner. Thus, the concentration of oxygen is low so that the combustion is unstable and thus flame cannot be properly formed. Accordingly, in order to meet a stable combustion condition, the concentration of oxygen is required to increase and a larger amount of fuel is to be consumed as much as the amount of air being additionally supplied. Accordingly, the present invention has been made in view of the above-mentioned problems occurring in the prior art, and it is a primary object of the present invention to provide a burner for generating a reductive atmosphere of exhaust gas in an engine cogeneration plant having a denitrification process, in which in order to produce a catalyst activation condition to remove nitrogen oxides from the engine exhaust gas in the boiler of the engine cogeneration plant, a mixture of the engine exhaust gas and fuel is injected into an engine exhaust gas injection port and a stable combustion can be maintained by means of an auxiliary burner. To accomplish the above object of the present invention, according to the present invention, there is provided a burner for generating a reductive atmosphere of exhaust gas in a boiler system of an engine cogeneration plant having a denitrification process. The burner comprises: a post-combustion burner for combusting an internal combustion engine exhaust gas, the internal combustion exhaust gas being supplied from an internal combustion engine exhaust gas injection port; and an auxiliary burner installed in an outer side of the post-combustion burner, wherein the auxiliary burner is combined with a fuel injection port through which fuel is supplied, and an air channel through which air inflows; and combustion heat generated by combusting the supplied fuel and air is provided to a combustion chamber of the post-combustion burner through a flame channel. A combustible mixture gas is injected to the post-combustion burner through the internal combustion engine exhaust gas injection port. The combustible mixture gas contains fuel more than to the extent to remove oxygen contained in the internal combustion engine exhaust gas. In addition, new air through a blower and fuel are injected at the same time to the auxiliary burner and combusted therein. The new air is injected to an air injection port and recovers heat transferred from a combustion flame inside the combustion chamber while passing through the air channel, thereby enabling to prevent heat loss and safety accidents. The burner further comprises a damper capable of adjusting the amount of a combustible mixture gas to be supplied to the front and rear sides of the flame of the auxiliary burner after being injected to the internal combustion engine exhaust gas injection port, thereby enabling to adjust combustion conditions. The combustible mixture gas is a mixture of internal combustion engine exhaust gas and fuel. The present invention generates a stable reductive atmosphere required for denitrification catalyst to remove nitrogen oxides, which is produced in engine exhaust gas of an engine cogeneration plant using a lean burn engine. According to the present invention, fuel is injected into the engine exhaust gas in advance, and thus a combustible mixture gas of the engine exhaust gas and fuel is injected through an injection port. A new air and fuel are supplied to an auxiliary burner respectively and combusted therein, thereby enabling to achieve, in a stable way, a reductive atmosphere having oxygen of no more than 1% and carbon monoxide of about 1000 ppmv. Continue reading about Burner for generating reductive atmosphere of exhaust gas in engine cogeneration plant having denitrification process... 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