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108results about How to "Improved air distribution" patented technology

Blast furnace chute polycyclic distributing method

The invention discloses a blast furnace chute multi-ring burden distribution, which comprises firstly calculating the distance from the center of furnace burden from the center of a blast furnace after furnace burden fell into an xy plane, secondly deciding largest and smallest burden distribution angles in theory, thirdly deciding the actual burden distribution angles of outer ring and inner ring of ores and coke, fourthly deciding the burden distribution ring number of ores and coke, determining the burden distribution angle of middle ring of ores and coke and the angel difference of adjacent rings, and sixthly determining the burden distribution rings of each ring in ores and coke. The process largely enriches the regulating method on the upper portion of the blast furnace, changes coal gas distribution, effectively increases the coal gas usage of the blast furnace, reduces coke ratio, realizes the stable and long term operation of the blast furnace, has strong loading material capacity, can eliminate furnace burden gravity segregation and the existing of pile top, much reasonably distributes furnace burden, is beneficial for strengthening smelting, and improves the press amount relationship and further increases the air quantity of the blast furnace.
Owner:CHONGQING IRON & STEEL (GRP) CO LTD

Flue gas recirculation-based wide load-wide coal deep denitrification system for CFB (circulating fluidized bed) boiler

The invention provides a flue gas recirculation-based wide load-wide coal deep denitrification system for a CFB (circulating fluidized bed) boiler. The system comprises the boiler, an SNCR (selective non-catalytic reduction) system, a primary air blower, a secondary air blower, an induced draft fan, a recirculation flue, a primary air recirculation adjusting valve, a secondary air recirculation adjusting valve and the like. One end of the recirculation flue is connected with an outlet of the induced draft fan, the other end is connected with an inlet of the primary air blower and an inlet of the secondary air blower by the aid of the primary air recirculation adjusting valve and the secondary air recirculation adjusting valve, low-temperature flue gas is led out of the outlet of the induced draft fan, the low-temperature flue gas with the proper flow is sent to different positions of a combustion chamber by the blowers through control by the adjusting valves, distribution of temperature fields in the boiler is optimized by fine controlling content of oxygen of primary air and content of oxygen of secondary air on the basis of SNCR, pollutant emission is reduced, and the CFB boiler can realize low emission of NOx under wide load-wide coal conditions.
Owner:SICHUAN CHUANGUO BOILER

Pulse backflush deashing device for filter

ActiveCN102908840AOvercome airflow eccentricityOvercome defects such as vibrationDispersed particle filtrationJet flowDiffusion loss
The invention discloses a pulse backflush deashing device for a filter. Filtering units are arranged on a pipe plate of the filter, and the pipe plate divides the filter into a clean gas cavity and a dusty gas cavity in a sealing manner. The pulse backflush deashing device comprises ejectors arranged at the upper parts of the filtering units, and backflush pipelines matched with the ejectors, wherein one end of each backflush pipeline is communicated with a backflush gas storage tank through a pulse backflush valve, and a direction-adjusting multi-hole jet nozzle according to the top part of each ejector is arranged at the other end of each backflush pipeline. As the pulse backflush deashing device adopts the direction-adjusting multi-hole jet nozzles with the jet directions being adjustable, the jet direction of backflush gas can be adjusted, the jet length can be extended, and a primary jet flow and a secondary jet flow are mixed uniformly by multiple high speed jet flows, so that the distribution statuses of backflush gas flows entering the ejectors can be improved, the diffusion loss is reduced, the energy transmission efficiency can be improved, and the deficiencies, such as non-uniformity of pulse backflush, as well as gas flow eccentricity and filter pipe vibration that are brought by the existing jet nozzles, are overcome.
Owner:CHINA UNIV OF PETROLEUM (BEIJING)

Porous partition spray equipped desulfurization tower

The invention discloses a porous partition spray equipped desulfurization tower. The lower part in the tower body is a first order absorption zone, the upper part in the tower body is a second order absorption zone, and a porous air flow distribution plate is disposed between the first order absorption zone and the second order absorption zone. The porous air flow distribution plate includes a plate body, the plate body is provided with liquid leakage holes, the plate body is also provided with upward ventilation columns, each ventilation column is equipped with an air cap, the tower body is externally provided with a tower outside slurry pool of the second order absorption zone, and the tower outside slurry pool is connected to the liquid leakage holes through a seal pipeline. According to the porous partition spray equipped desulfurization tower provided by the invention, the first order spray operates at a low Ph value, the second order spray operates at a high Ph value, the energy consumption of a circulating pump is greatly reduced, the porous air flow distribution plate is used for separating the two order absorption systems, the rising flue gas and falling slurry can pass separately, thus ensuring smooth flue gas rising and uniform flue gas distribution. The desulfurization tower is especially suitable for high sulfur coal flue gas desulfurization, can lower the investment and operation cost, and is applicable to current ultra-clean emission reconstruction of power plants.
Owner:浙江菲达环保科技股份有限公司

Skewed gas flow electric bag composite dust remover

The invention discloses a skewed gas flow electric bag composite dust remover, which comprises a gas flow distribution region, an electric dust removing region and a bag dust removing region from left to right, wherein the lower parts of the electric dust removing region and the bag dust removing region are provided with dust collecting regions; a clean gas region is positioned on the upper part of the bag dust removing region; the gas flow distribution region comprises two gas flow distribution plates which are arranged vertically, and a skewed gas flow distribution plate; the electric dust removing region comprises a cathode line, an anode plate and a high-pressure electric device; the joint between the electric dust removing region and the bag dust removing region is provided with an electric bag bonding plate; the bag dust removing region comprises a gas flow diversion plate, a bag, a framework and a tube nest; the framework and the bag construct a whole body which is arranged on the tube nest; each dust collecting region consists of an ash hopper and an ash hopper baffle plate; and the clean gas region mainly comprises clapboards. Optimal gas flow distribution in the electric bag composite dust remover is realized, the generation of eddy current in the electric dust removing region is reduced, the running resistance of the bag dust removing region is reduced, re-entrainment is reduced, and low-resistance efficient running of the electric bag composite dust remover is ensured.
Owner:SOUTH CHINA UNIV OF TECH

Three-cycle desulphurization method for wet type ammonia-process desulphurization and flue gas desulfurization tower or system

The invention relates to the field of environmental protection and discloses a three-cycle desulphurization method for wet type ammonia-process desulphurization. The desulphurization method is implemented with a first slurry circulating loop, a second slurry circulating loop and a third slurry circulating loop, wherein in the first slurry circulating loop, slurry having mass concentration of 10%-20% and a pH value of 4.0-5.0 is used for carrying out cycle spraying treatment on flue gas, and the temperature of the flue gas treated by the slurry is 50-60 DEG C; in the second slurry circulating loop, slurry having mass concentration of 10%-15% and a pH value of 5.0-6.0 is used for carrying out cycle spraying treatment on the flue gas; and in the third slurry circulating loop, slurry having mass concentration of 3%-10% is used for carrying out cycle spraying treatment on the flue gas. The invention also discloses a flue gas desulfurization tower or system using the three-cycle desulphurization method. According to the three-cycle desulphurization method, the three independent circulating loops are divided according to the concentration of the slurry, the circulating loops separately control the slurry having different concentrations and pH values for treatment of the flue gas, and the contradiction of high desulphurization efficiency and high oxygenation efficiency of by-products is solved.
Owner:SICHUAN JUNHE ENVIRONMENTAL PROTECTION
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