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OXIDATION METHOD FOR SINTERING FLUE GAS DENITRIFICATION AND SYSTEM

机译:烟气脱硝的氧化方法及系统

摘要

An oxidation method for sintering flue gas denitrification. The method comprises: using an ozone plasma generator to discharge electricity into an oxygen source and generate plasma free radicals; and the plasma free radicals transforming NO in a flue gas into a nitrogen oxide with a higher valence state. The volume of the plasma free radicals produced is controlled according to the concentration of the flue gas. In a mixture of the oxygen source and a NOx-containing flue gas, the mass ratio of NO to NO3 is 0.8-1.5:1. The plasma free radical production volume of the ozone plasma generator is 6-12 kg/h for 30,000-50,000 Nm3/h of the NOx-containing flue gas, realizing rapid oxidation and high denitrification efficiency. Using the ozone plasma for denitrification can achieve a higher NOx denitrification rate and up to 98% NOx removal rate. Further provided is a sintering flue gas denitrification system. The denitrification system comprises: a detection device, a flue gas intake device, an ozone plasma generator, a controller, a denitrification device, a spraying device, a desulfurization tower, and a flue gas discharging device. The controller is connected to the detection device, the flue gas intake device, and the ozone plasma generator. The denitrification device is connected to the ozone plasma generator and the flue gas intake device. The desulfurization tower is internally provided with the spraying device. The denitrification device is connected to the desulfurization tower. The flue gas discharging device is provided at a top end of the desulfurization tower.
机译:烧结烟气脱氮的氧化方法。该方法包括:使用臭氧等离子体发生器将电排放到氧气源中并产生等离子体自由基;等离子体自由基将烟道气中的NO转化为价态较高的氮氧化物。根据烟道气的浓度控制所产生的血浆自由基的体积。在氧气源和含NO x 的烟气的混合物中,NO与NO 3 的质量比为0.8-1.5:1。对于30,000-50,000 Nm 3 / h的含NO x 的烟气,臭氧等离子体发生器的等离子体自由基产生量为6-12 kg / h,实现了快速氧化和高反硝化效率。使用臭氧等离子体进行反硝化可以实现更高的NO x 反硝化率和高达98%的NO x 去除率。还提供了一种烧结烟气脱氮系统。该反硝化系统包括:检测装置,烟道气进气装置,臭氧等离子体发生器,控制器,反硝化装置,喷雾装置,脱硫塔和烟道气排放装置。控制器连接到检测装置,烟道气进气装置和臭氧等离子体发生器。反硝化装置连接到臭氧等离子体发生器和烟道气进气装置。脱硫塔内部设有喷雾装置。脱硝装置连接至脱硫塔。烟气排放装置设置在脱硫塔的顶端。

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