| Nitrogen oxide(NOx)is one of the main air pollutants.The control of NOx emission is imperative.Compared with the thermal power industry,the non-power industry is more and more polluting.Most of the flue gas emitted by non-electric industries is low temperature.It is difficult to meet the requirement of low-temperature activity if traditional vanadium titanium based catalysts are used.Therefore,it is very necessary to develop a SCR catalyst with high denitration activity and high anti-poisoning performance at low temperature.In this paper,Cu-Fe/CA low-temperature denitration catalysts were prepared by a citric acid(CA)sol-gel method.The physicochemical properties of the catalysts were studied by many advanced characterization methods.In addition,the change of denitration activity of Cu-Fe/CA catalysts and the mechanism of anti-poisoning were further discussed by a density functional theory of quantum chemistry.The main research results are as follows:(1)Compared with Fe/CA catalysts with different doping amounts of Cu,when the mass ratio of Cu to Fe is 3 to 24(Cu3Fe24/CA),the catalyst has a good low-temperature denitration activity.The denitration efficiencies are 89%and 87%at 140℃and 280℃,respectively.When the temperature is at 160-260℃,the denitration efficiencies are always maintained at more than 99%,N2 selectivity is higher than 95%,and NH3escape rate is always maintained at about 5%in the whole test temperature range.This indicated that the catalyst causes less secondary contamination after SCR reaction.The results of calculating the adsorption behavior of gas molecules on the Cu-Fe/CA catalyst surface shows that the Cu site on the catalyst surface not only has a good adsorption effect on gas molecules,but also can enhance the adsorption of gas molecules on the nearby Fe site,thus improving the denitration performance of Cu-Fe/CA catalyst.The reaction kinetics of Cu3Fe24/CA and Fe/CA denitration catalysts show that the apparent activation energy of Cu3Fe24/CA catalyst is 26.83 k J/mol,which is 6.69 k J/mol lower than that of the Fe/CA catalyst.(2)The denitration activity of Cu3Fe24/CA catalyst decreases due to alkali metal K poisoning.When the K loading is 2%,the denitration activity of the catalyst decreases significantly,and the denitration efficiency is only 31%at 120℃.The main reason is that K inhibits the adsorption capacity of NH3 molecule on the catalyst surface,and the adsorption energies of NH3 molecule on Cu site and Fe site decreased from-1.54 e V and-1.06 e V to 0.47 e V and-0.52 e V,respectively.Zr modification can effectively improve the anti-K metal performance of Cu3Fe24/CA catalyst.When the mass ratio of Zr:Cu:Fe is 3:3:24,the anti-K poisoning performance of the catalyst increases significantly.The denitration efficiency of K0.48Zr3Cu3Fe24/CA catalyst increases from 31%to 55%at 120℃,and the denitration efficiency rises to more than 90%at160-260℃.(3)Cu doping can significantly improve the SO2 poisoning resistance of Fe/CA catalyst.At 180℃,when 100 ppm SO2 is entered,the denitration efficiency of Fe/CA catalyst is decreased sharply,which is only 12%after500 min.However,the denitration efficiency of Cu3Fe24/CA catalyst gradually stabilized at about 54%after continuous addition of SO2 for 500min because Cu doping reduces the production of sulfuric acid or ammonium sulfate by inhibiting the oxidation of SO2 to SO3.However,after further modification with Mn,it was found that Mn2Cu3Fe24/CA catalyst delays the time of SO2 poisoning.When SO2 is entered for 420min,the denitration efficiency would still be decreased rapidly in the same trend as the poisoning of Cu3Fe24/CA catalyst.(4)The modification of Mn can greatly enhance the low-temperature denitrification efficiency of Cu3Fe24/CA catalyst.When the mass ratio of Mn:Cu:Fe is 2:3:24,the active temperature window of Mn2Cu3Fe24/CA catalyst moves forward from the original low temperature of 160-260℃to120-240℃and remains above 90%.Especially at 120℃,its denitration efficiency increases from 59%to 93.6%.However,the doping of Mn will lead to the formation of NO2 and N2O in the medium temperature region and reduce the N2 selectivity of the catalyst.In addition,the number of Mn2Cu3Fe24/CA acid sites increased from 2.57 to 2.63,and the number of Lewis acid sites increased from 1.03 to 2.36.The H2-TPR characterization,shows that the low-temperature active site of Mn2Cu3Fe24/CA catalyst are about 3 times higher than those of the Cu3Fe24/CA catalyst,while the high temperature active sites are reduced,which is the reason that the active temperature window of Mn2Cu3Fe24/CA catalyst moves forward to low temperature. |