| Emissions of nitrogen oxides(NOx)cause serious harm to human health and the global climate.Diesel vehicles are a major contributor to mobile source NOx,and ammonia selective catalytic reduction(NH3-SCR)is considered to be one of the most effective aftertreatment technologies available for NOx removal,and its core is the NH3-SCR catalyst.The commercialization of Cu-CHA small-pore zeolites catalysts(Cu-SSZ-13 and Cu-SAPO-34)is a milestone event in environmental catalysis.However,with increasingly stringent global emission regulations,such as the California Air Resources Board’s requirement to reduce NOx from the current 0.27 g/k W-hr to an ultra-low limit of 0.027g/k W-hr by 2027,this means that the catalytic efficiency of NH3-SCR must exceed 99%.However,Cu-CHA catalysts still face many serious challenges under actual service conditions,such as poor NOx catalytic performance during cold start,sulfur/phosphorus/alkali metal poisoning deactivation,and high-and low-temperature hydrothermal deactivation.In order to meet the future regulatory requirements for ultra-low NOx emissions,this dissertation designs and constructs Cu-CHA catalysts at the atomic level to develop catalytic materials with better performance.The main contents are as follows.(1)Cu-SAPO-34 catalysts with similar copper content were precisely synthesized by the"one-pot"method using different structure directing agents(diethylamine,triethylamine,propylamine,and tetraethylammonium hydroxide),and after low-temperature hydrothermal treatment,Cu-SAPO-34 catalysts with more Si-O(H)-Al density and ZCu(OH)sites(Z represents one framework negative charge),the Cu-SAPO-34 catalysts were more prone to low-temperature hydrothermal deactivation leading to the degradation of NH3-SCR catalytic performance,where the Cu-SAPO-34synthesized using tetraethylammonium hydroxide exhibited the strongest water resistance and good denitrification activity.(2)The low-temperature hydrothermal stability of Cu-SAPO-34 was improved by protection strategies such as rare earth metal(Ce,La and Sm)doping,alkali metal(Na,K and Cs)exchange and NH3 pre-sorption,but different strategies exhibited different protection effects in the low-and high-temperature regions.On the basis of revealing the mechanistic differences of these protection strategies,a combination strategy of Ce doping,Na exchange and NH3 pre-sorption was simultaneously employed to further prevent the low-temperature hydrolytic deactivation of Si-O(H)-Al and ZCu(OH)sites,and stronger water-resistant Cu-SAPO-34 denitrification catalysts were developed.(3)The Cu-exchanged SAPO-18,SAPO-34 and SAPO-18/34 intergrowth zeolites were carefully designed by modulating the ratio of structure directing agents(N,N-diisopropylethylamine,triethylamine or their mixtures).The results show that the Cu-SAPO-18/34 intergrowth zeolite has more Si(n Al)(n=1~4)structures compared to the pure crystalline phase Cu-SAPO-18 and Cu-SAPO-34,which leads to more and stronger acidic sites,facilitates the generation of more Cu active centers during aqueous ion exchange(AIE)and inhibits the formation of Cu Ox,thus leads to higher NH3-SCR catalytic activity,better high-and low-temperature hydrothermal stability and resistance to SO2 poisoning.(4)Copper exchanged SSZ-13,SAPO-34 and SAPO-18 catalysts were successfully prepared by the solid-state ion exchange(SSIE)method.Compared with the conventional AIE route,this SSIE technology can improve the ion-exchange level of copper,avoid the accumulation of Cu Ox,and improve the NH3-SCR catalytic activity and high-temperature hydrothermal stability.In addition,the use of NH4+-type zeolite carriers improves the dispersion of Cu2+better than H+-type zeolite carriers in the SSIE process,i.e.,in NH4+-type zeolite carriers,at 150~250°C,Cu2+is solventized by NH3 to produce Cu(NH3)x2+intermediates(x=2 or 4),which are then dissociated and decomposed in an oxygen atmosphere at 250~400°C.The formed Cu(NH3)x2+intermediate promotes Cu2+mobility and lowers the reaction energy barrier to facilitate Cu2+occupation of ion-exchange sites,while H+-type zeolite carriers are unable to produce this intermediate species. |