The adsorption competitive adsorption and conversion behaviors of thiophene and 1?hexene on Hβ molecular sieve have been studied by using the method of in?situ infrared spectroscopyThe roles of different acidic sites in the alkylation reaction of thiophene and olefin molecule were systematically discussed. The results show that 1?hexene is preferentially adsorbed on the B acid sites, and it s easy to dimerize through protonation activation. Thus,there is a significant competitive relationship between the adsorption of thiophene molecules and the protonation reaction process. Moreover, it can be confirmed that the adsorbed thiophene molecule on non?framework aluminum on zeolite are more likely to its alkylation with a protonation 1?hexene molecule near the center of the B acidThis results can provide basic theoretical guidance for the development of zeolite catalysts for alkylation desulfurization processes.

In this paper, the method of combining Grand Canonical Monte Carlo simulation and Ideal Adsorption Solution Theory was used to study the adsorption performance of CO₂ and CH₄ on NaX zeolite. By comparing the fitting results of simulation data under different adsorption theoretical models and calculating the adsorption heat, a description of the adsorption and separation process of CO₂ and CH₄ gas was obtained. The results show that the adsorption strength of CH₄ molecules is weaker than that of CO₂ molecules, and its adsorption is closer to the ideal adsorption. The adsorption selectivity of CO₂ molecules is decreases with the increase of its content in the air, and decreases with the increase of temperature under low pressure conditions. Therefore, low temperature and low pressure are more conducive to the separation of CO₂ molecules.

This paper carried out the screening of WO _x /SiO₂ catalyst carrier and the investigation of WO _x loading capacity, and successfully screened a domestic SiO₂ carrier with excellent performance. The structure and properties of the catalyst were characterized by nitrogen physical adsorption, XRD, Raman spectroscopy and TEM/EDS. The dispersion of WO _x species on the carrier was mainly investigated, the catalytic reaction performance of disproportionation of ethylene and butene to propylene was investigated, and the performance was compared with that of a foreign commercial catalyst. The research results show that the WO _x loading threshold of the domestic carrier S?SiO₂ is 8%. At this time, the catalyst shows the best catalytic activity and selectivity. Compared with the catalytic performance of the comparative commercial catalyst, the catalyst activity is nearly 10% higher, and the stability and selectivity are equivalent, and the correlation structure characterization results can confirm that the dispersion characteristics of WO _x species on the support are the key factors that affect the catalytic performance, while the SiO₂ support and loading are both the key to the dispersion state of WO _x species. This study can provide a basis for the localization of WO _x /SiO₂ catalysts for high?efficiency olefin disproportionation reactions, especially the selection of domestic SiO₂ carriers.