| In order to achieve efficient desulfurization and denitrification of industrial flue gas,this paper adopts an ozone oxidation-alkali absorption process,and uses chemical simulation software Aspen Plus to simulate and analyze the process.Firstly,it has been known from previous studies that the ozone oxidation process is suitable for lower temperature.The conclusion is verified by the chemical reaction equilibrium theory in this paper.The results show that the ozone oxidation process is suitable for lower temperatures below 150℃.Secondly,for the O3 oxidation-Na OH absorption process,the effects of factors such as flue gas temperature,residence time,O3/NO molar ratio,and initial concentration of NO on the oxidation process were studied,by using the plug flow reactor and the exponential function as the oxidation model.It is found that O3 has a high selectivity for NO.The temperature has little effect on oxidation rate of NO.The residence time and the initial concentration of NO have certain effects,and the O3/NO molar ratio has the biggest impact.Meanwhile,the effect of factors such as the temperature,the NO concentration,the NO2/NO molar ratio of flue gas at the inlet of the absorption tower and the amount of absorption liquid on the absorption rate of SO2 and NOx were studied.The results show that SOx can be fully absorbed and the above factors have little effect on the absorption rate of SO2,and the flue gas temperature has certain effect on the NOx absorption rate,but the NO concentration,NO2/NO molar ratio and the amount of absorption liquid has a significant effect on the NOx absorption rate.Thirdly,for the Na OH-Na2S2O3 absorption process,the effects of Na2S2O3concentration,SO2 concentration and p H on SO2 and NOx absorption rates were discussed.It was found that the increase of the above three factors can promote the absorption of NOx,because in an alkaline solution,S2O32-can exist stably and have reducibility,so that it can jointly reduce NO2 combined with the reducibility of SO32-.Under the conditions of Na2S2O3 mass fraction of 10%,SO2 concentration of 300 mg/m3 and p H of 10,the NOxabsorption rate can reach 83.32%.Finally,three different sulfate additives were added to the Ca SO3 desulfurization process respectively.The promoting effects of different additives on NO2 absorption at different concentrations were compared.The mechanism of the additive action was discussed,and the specific path of the SO42-action was analyzed.Reducing additives such as Fe SO4 are not suitable for removing NOx,because its ferrous iron will consume NO3-,which will lead to disproportionation reaction of NO2 and produce more NO.When the additive concentration is 0.35 mol/L,the NOx absorption rate of Ca SO3 desulfurization process with(NH4)2SO4,Mg SO4 and Fe SO4 as additives can reach 68.38%,70.35%and65.98%.It can be seen that the ozone oxidation-alkali solution absorption process can realize high-efficiency oxidation of NO,and can achieve the removal of NOx while efficiently removing SOx. |