| Nitrogen oxides(NOx),a major component of atmospheric pollutants,can cause a series of environmental problems such as haze,acid rain,and photochemical smog.Nowadays,with the improvement of our life,the number of motor vehicles has increased significantly.NOxemitted from diesel exhaust is the main pollutant source,which is urgent to be controlled immediately.The selective catalytic reduction of NOx with NH3(NH3-SCR)is an effective approach to remove NOx contaminants,and highly effective catalyst is the key to carry out NH3-SCR reaction.Currently,V2O5-WO3(MoO3)/TiO2catalysts are commercially available in NH3-SCR technology.However,the narrow active window,the toxicity and volatility of vanadium limit its application in diesel vehicles.Cu-CHA microporous zeolites have been developed and applied by researchers because of their large specific surface area,wide active window,and high hydrothermal stability.Among them,the representatives of Cu-CHA zeolites are Cu-SAPO-34 and Cu-SSZ-13,which have achieved extensive application in the NH3-SCR technology.Especially the latter one is the best choice to response the national VI NOx emission standards.In this thesis,Cu-SAPO-34 zeolite was prepared by one-pot method,and then the catalyst was treated at low/high-temperature hydrothermal environment.X-ray powder diffraction(XRD),scanning electron microscope(SEM),and H2 temperature programmed reduction(H2-TPR)and NH3-SCR were used to character physicochemical properties and activity.It was found that its structure was not significantly destoryed after different hydrothermal treatment.Moreover,the relative content of Cu2+increased after high temperature treatment,raising the NH3-SCR activity of Cu-SAPO-34.The results confirm that the synthesized Cu-SAPO-34 has strong resistance to low/high-temperature hydrothermal aging.Secondly,Si/Al≈9 SSZ-13 zeolote was synthesized by the crystal transformation method in a 500 m L quick-opened autoclave.USY zeolite was used by the parent zeolite.Its high crystallinity,good morphology and large specific surface area were confirmed by XRD,SEM,BET.At the same time,different ion-exchange methods(straight or traditional ion-exchange)are used to prepare Cu-SSZ-13,and its temperature was optimized.The sam ple obtained by the straight ion-exchange method has the same NH3-SCR activity and hydrothermal aging resistance as the traditional ion-exchange method.And two ion-exchanged methods negligibly affects the crystallinity and specific surface area of the zeolite.In addition,the optimal ion-exchange temperature for both methods is 80 oC.Beyond that,a 5 L quick-opened autoclave was used to synthesize SSZ-13 for expangding product.And the product also has high crystallinity and specific surface area.Moreover,the NH3-SCR activity of Cu-SSZ-13synthesized by different ion-exchange methods was equivalent.Finally,Cu-SSZ-13 zeolite and silica sol were selected as the catalyst powder and the binder,respectively.Ball milling was used to obtain the stable slurry firstly,and its best time was 9 h.Then,the cordierite ceramic honeycomb was used as the catalyst carrier.Cu-SSZ-13monolithic catalyst was prepared by pull-up coating method.Its shedding rate was tested to find out the optimal ratio of each component,confirming its good binding foece.Finally,the optimal catalyst was tested by NH3-SCR,confirming its good NH3-SCR performance. |