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97results about How to "Reduce nitrogen oxide content" patented technology

Two-stage thermal oxidation of dryer offgas

A method and apparatus are provided for reducing the VOC, CO, and, alternatively, the NOx content of dryer offgas that is discharged into the atmosphere from a moist organic product drying process using thermal oxidizing apparatus that includes a burner, furnace, mixing chamber, thermal oxidizer, tempering chamber, and an indirect gas-to-gas heat exchanger. The dryer offgas is separated into two portions, with a larger portion being preheated by indirect heat exchange with the hot gaseous output from the thermal oxidizer. The non-preheated portion is directed to the burner in the function of flue gas recycle for NOx control. The preheated portion is separated into two portions, with one portion being directed to the furnace/mixing chamber of the thermal oxidizing apparatus. The other portion of the preheated offgas is recycled to the hot gas inlet of the dryer and serves the function of dryer heat transfer media. Ultimately, all the dryer offgas enters the thermal oxidizer, and comprises a smaller non-preheated portion directed to the burner and a larger preheated portion directed to the furnace/mixing chamber. By preheating a large proportion of the offgas directed to the thermal oxidizing apparatus, simultaneous achievement of an adequate thermal oxidizer temperature, 1600° F., and an adequate oxygen concentration of 5% by volume is achieved for optimized thermal oxidation of carbon monoxide and volatile organic compounds.
Owner:AEROGLIDE

Integrated method for simultaneously realizing denitrification, desulfurization and heavy metal removal from flue gas, and special equipment suitable for the method

The invention relates to an integrated method for simultaneously realizing denitrification, desulfurization and heavy metal removal from flue gas, and special equipment suitable for the method. The integrated method is characterized in that an acidic gas capture agent adopted by the invention captures SO2 and/or highly charged nitrogen oxides NOx in raw flue gas and thus ammonium sulfate as a by-product and/or ammonium nitrate as a by-product is obtained finally, and the acidic gas capture agent adsorbs heavy metals in the raw flue gas simultaneously, wherein the above processes are carried out in a same absorbing device. The special equipment suitable for the method of the invention comprises an absorbing tower, a raw flue gas input pipeline having an external connection with the absorbing tower body, a purified flue gas output pipeline having an external connection with the absorbing tower body, a system for supplying the acidic gas capture agent and absorbents, a demisting water input pipeline, an absorption liquid cycling system, a slurry discharge system, and a separation and treatment system, wherein the raw flue gas input pipeline is provided with a supercharging system anda forced oxidation system. Through the method of the invention, the integrated purification processes of denitrification, desulfurization and heavy metal removal from flue gas can be completed in a same device and by-products from the integrated purification processes are ammonium sulfate and ammonium nitrate, wherein ammonium sulfate and ammonium nitrate can be utilized as components of fertilizers. Through the method, waste water and waste residue are not produced in the integrated purification processes and the integrated purification processes have the advantages of simple system, low cost, high recovery rate, etc.
Owner:BEIJING SPC ENVIRONMENT PROTECTION TECH

Two-stage thermal oxidation of dryer offgas

ActiveUS7654011B2Reducing VOC and CO contentLimit production of NOxDrying solid materials with heatDrying gas arrangementsAtmospheric airOxygen
A method and apparatus are provided for reducing the VOC, CO, and, alternatively, the NOx content of dryer offgas that is discharged into the atmosphere from a moist organic product drying process using thermal oxidizing apparatus that includes a burner, furnace, mixing chamber, thermal oxidizer, tempering chamber, and an indirect gas-to-gas heat exchanger. The dryer offgas is separated into two portions, with a larger portion being preheated by indirect heat exchange with the hot gaseous output from the thermal oxidizer. The non-preheated portion is directed to the burner in the function of flue gas recycle for NOx control. The preheated portion is separated into two portions, with one portion being directed to the furnace / mixing chamber of the thermal oxidizing apparatus. The other portion of the preheated offgas is recycled to the hot gas inlet of the dryer and serves the function of dryer heat transfer media. Ultimately, all the dryer offgas enters the thermal oxidizer, and comprises a smaller non-preheated portion directed to the burner and a larger preheated portion directed to the furnace / mixing chamber. By preheating a large proportion of the offgas directed to the thermal oxidizing apparatus, simultaneous achievement of an adequate thermal oxidizer temperature, 1600° F., and an adequate oxygen concentration of 5% by volume is achieved for optimized thermal oxidation of carbon monoxide and volatile organic compounds.
Owner:AEROGLIDE

Built-in biomass gasification combustion hot water boiler

The invention discloses a built-in biomass gasification combustion hot water boiler which comprises a water heater, a biomass gasification device and a combustion chamber. The water heater comprises a water tank and a plurality of smoke pipes. The biomass gasification device is used for generating biomass gas. The combustion chamber is arranged between the water heater and the biomass gasification device and used for combusting the biomass gas and conveying smoke generated after combustion into the water heater so as to heat water in the water tank. The biomass gasification device comprises a device body, a fire grate, a fire barrier, an air sleeve and a first water jacket, wherein the interior of the device body is divided by the fire grate into a gasification reaction chamber in the middle and an air chamber on the lower portion, and the interior of the device body is divided by the fire barrier into a gas storage chamber on the upper portion and the gasification reaction chamber in the middle. Generated water vapor is supplied to the gasification reaction chamber through the first water jacket to serve as a gasification agent, cold air is preheated in the air sleeve into hot air through the air sleeve, then the hot air is supplied to the combustion chamber for combustion supporting, and the biomass gas is supplied to the combustion chamber to be combusted through the gas storage chamber.
Owner:GUANGZHOU QIYADIAN BOILER CO LTD

Inside-mixing type reducing agent atomizing spray gun for SNCR (Selective Non-Catalytic Reduction) denitration process

The invention discloses an inside-mixing type reducing agent atomizing spray gun for an SNCR (Selective Non-Catalytic Reduction) denitration process, belonging to the technical field of boiler denitration devices. The inside-mixing type reducing agent atomizing spray gun comprises a spray gun sleeve, an electric propulsion plant and a spray gun and is characterized in that the spray gun sleeve is installed on the external wall of a boiler and communicated with a boiler hearth; the spray gun sleeve is inclined downward and has an included angle of 5-15 degrees with the horizontal plane; and the electric propulsion plant is fixedly connected with the spray gun and fixedly connected with the spray gun sleeve. When the system is put into operation, a motor is rotated forward and drives a screw rod to rotate through a coupler, a screw nut is moved forward in the rotation action of the screw rod and drives the spray gun to move forward and enter the hearth to spray; and when the system is shut down, the motor is rotated reversely and the screw nut moves backward to drive the spray gun to exit the hearth. The inside-mixing type reducing agent atomizing spray gun disclosed by the invention has the advantages of good atomizing effect, high degree of automation, low rate of gas consumption and prevention of corrosion to a water-cooled wall and is applicable to boilers such as a medium-small coal-powder boiler and a circulating fluidized bed the like; and the atomizing medium can be compressed air or steam.
Owner:SHANDONG SHANDA WIT ENVIRONMENTAL ENGINEERING CO LTD

Ultralow-emission nitrogen oxide biomass chain boiler

The invention provides an ultralow-emission nitrogen oxide biomass chain boiler. The ultralow-emission nitrogen oxide biomass chain boiler comprises a boiler body, a chain grate and a spiral feeder, wherein an upper header, a lower header, an upper boiler barrel and a lower boiler barrel are arranged in the boiler body; a hearth, a flue gas radiation chamber, a flue gas convection box and a smoke exhaust box are arranged in the boiler body; an air preheater is arranged in the smoke exhaust box; the chain grate is arranged at the bottom of the hearth; primary air is supplied from the air chamber of the chain grate; in particular, hearth front and back air jet pipes are arranged on front and back arch throats respectively, and are connected with front and back air jet pipe fans; secondary air is supplied in two segments from front and back arches. Furthermore, the primary air can be supplied in two segments from the air chamber of the chain grate; the air source of the primary air and/or the secondary air can be hot air output by the air preheater; 1-3 afterburning ports are formed beside a feeding hole in the front arch throat; a denitrification combustion device is correspondingly arranged on each afterburning port. By adopting the ultralow-emission nitrogen oxide biomass chain boiler, zero emission of carbon dioxide is basically realized, and the effect of low emission of dust, nitrogen oxide and sulfur dioxide is achieved.
Owner:迪森(常州)能源装备有限公司 +1

Control method and device for reducing nitrogen oxide content in heating furnace combusting waste gas

The invention relates to the technical field of heating furnaces, in particular to a control method and device for reducing the nitrogen oxide content in the heating furnace combusting waste gas. Themethod comprises the steps that the current furnace temperature of a first furnace temperature control area in a heating furnace is acquired; it is judged whether the difference value of the current furnace temperature and the set target furnace temperature is greater than a first numerical value or not; if the different value is not greater than the first numerical value, the furnace temperatureof the first furnace temperature control area is adjusted to first set target temperature; and if the different value is greater than the first numerical value, the process target furnace temperatureis acquired, and after temperature adjustment of first set time is conducted on the first furnace temperature control area with the process target furnace temperature as the aim, the current furnace temperature is acquired again, wherein the process target furnace temperature is between the current furnace temperature and the set target furnace temperature. According to the control method for thereducing the nitrogen oxide content in the heating furnace combusting waste gas, when the current furnace temperature and the first set target furnace temperature differ much, the lower process targetfurnace temperature is used to conduct in-furnace multi-stage temperature adjustment so that the furnace temperature in the furnace temperature control area is stably adjusted to the set target furnace temperature, and the nitrogen oxide content generated when combustion is conducted in the heating furnace is reduced.
Owner:SHOUGANG JINGTANG IRON & STEEL CO LTD

Efficient and energy-saving gas thermal desorption equipment

The invention provides efficient and energy-saving gas thermal desorption equipment. A heating well is provided with an outer radiation pipe and an inner pipe which are mutually sleeved and form a backflow gap, and a heat exchanger is arranged above the inner pipe; a burner is arranged above the heating well, sprayed high-temperature flue gas can reach the bottom of the heating well through the inner pipe, the burner has a gas inlet, a combustion-supporting air inlet and a smoke exhaust port, wherein the gas inlet is connected with a gas station, the outer side of the combustion-supporting airinlet is communicated with a combustion-supporting fan, the inner side of the combustion-supporting air inlet is communicated with a combustion chamber of the burner through the heat exchanger, the smoke exhaust port is connected with a smoke exhaust fan and is used for discharging flue gas at the top of the heating well. A gap is left between the heat exchanger and the top of the inner pipe to form a flue gas return channel. According to the invention, the flue gas backflow channel is adopted, so that the combustion can be more complete, the nitrogen oxide content in the flue gas can be reduced, and the overall temperature of the heating well can be more uniform.
Owner:ZHONGKE DINGSHI ENVIRONMENTAL ENG CO LTD
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