This paper using a method of catalytic adsorption combined with dielectric barrier discharge plasma which added to hydrocarbon gases. The different background gases, different dielectric properties and different pore sizes of the hydrolysis coke on the denitrification performance was studied. The effect of the coaction of plasma and the different properties of the removal of NO in flue gas was investigated, and the catalytic mechanism of the synergistic effect of plasma and hydrocarbon gas was discussed. The results shown that: The denitrification rate was significantly affected by plasma power and the initial concentration of NO; the reaction was restrained by the presence of oxygen and greatly promoted by the hydrocarbon gases. The permittivity of the catalyst has a great influence on the activity and the porous structure of the catalyst can obviously promote the reaction when the low temperature plasma combined with hydrocarbon gases.

Manganese-based bimetallic catalysts were prepared with self-made pyrolysis coke as carrier and its denitration performance of low-temperature SCR (selective catalyst reduction) was studied. The effects of different metal species, calcination temperature, calcination time and the metal load quantity on the denitration performance of the catalyst were studied by orthogonal test. The denitration mechanism of the catalyst was analyzed by XRD (X-ray diffraction), SEM (scanning electron microscope), BET test and transient test. The experiments show that: ① The denitration efficiency of Mn-based bimetallic catalysts mainly relates to the metal type, the metal load quantity and the catalyst adjuvant type. ② The optimal catalyst preparation conditions are as follows: the load quantity of monometallic MnO2 is 10%, calcined at 300°C for 4h, and then loaded with 8% CeO2, calcined at 350°Cfor 3h. ③ The denitration mechanism of manganese-based bimetallic oxide catalysts is stated as: NH3 is firstly adsorbed by B acid center Mn-OH which nears Mn4+==O to form NH4+, NH4+ was then attacked by the gas phase NO to form N2, H2O and Mn3+-OH. Finally, Mn3+-OH was oxidized by O2 to regenerate Mn4+.

Fly ash and bentonite were mixed in a certain proportion as raw materials to prepare a denitration catalyst. In previous studies, it has been concluded that fly ash-type catalysts can provide significant catalytic activity for denitrification after being modified with oxygen. In this study, the effect of plasma conditions on the denitration performance of the catalyst was investigated from the aspects of plasma modification power, modification time, and the flow rate of the gas. Boehm titration and infrared analysis systems were used to characterize the performance of the catalyst. The experimental results show that the optimal modification power is 60 W, the optimal modification time is 20 min, and the optimal gas flow rate is 40 mL/min.

There are three different fly ashes mixed with bentonite respectively as raw material to preparation of denitration catalyst. Then the catalyst combined with the low temperature plasma for denitration. The different mixing ratio, drying temperature and drying time of catalyst preparation were studied. The denitration mechanism of fly ash catalyst modified with different gases (O2, N2, Ar, and hydrocarbon gas) by low-temperature plasma technology was studied. The compositions of fly ash were detected by element analysis, ICP analysis, Boehm analysis, and Infrared spectral analysis which affected the denitration performance of fly ash catalyst. And we discussed the effect of denitration performance with different types of fly ash and plasma power. The results shown that: fly ash mixed with bentonite for 2:1, drying temperature is 100°C and drying time is 30 min are the optimal preparation conditions; The denitration performance is best of the catalyst which produced by circulating fluidized bed when the plasma power is 30 W. And Oxygen can be used as the modification gas for preparing the fly-ash catalyst. There are more basic functional groups on the surface of fly ash catalyst modified with oxygen atmosphere and the N=O plays a main role.

This paper used an equal volume impregnation method to produce egg yolk-egg white bimetallic-supported catalyst. Phase structure and crystal morphologies were characterized by X-ray diffraction, scanning electron microscopy, temperature programmed reduction (TPR), and inductive coupling plasma methods, and the paper discussed the effect of different metal loading, calcination temperature, and calcination time on the desulfurization activity. The experimental results showed that desulfurization performance increased first and then gradually decreased as metal loading, calcination temperature, and calcination time increased. The optimum preparation conditions of bimetallic catalyst were 8% NiO and 5% MnO2, the most suitable calcination temperature was 400°C, and the most suitable calcination time was 4 h. Finally, the eggshell, the egg white, and the egg yolk catalysts had its own different characteristics in the desulfurization processing: the eggshell catalyst showed a rapid reaction rate but lasted for a short time, the egg yolk catalyst showed a slow reaction rate but lasted for a long time, and the reaction rate and lasting time of the egg white were between the eggshell and the egg yolk.