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Preparation,Characterization Of Highly Dispersed Anti-Sintered Ni/SiO2 Catalysts And Their DRM Reaction Catalytic Performance

Posted on:2019-02-13Degree:MasterType:Thesis
Country:ChinaCandidate:J C WanFull Text:PDF
GTID:2381330572456220Subject:Applied Chemistry
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Dry reforming of methane?DRM?reaction attracts people's attention since its conducive to the rational use of natural resources,advantages of reducing carbon waste and greenhouse e:ffect.The main reasons stand in the way of industrial application of DRM is the difficult to find a highly efficient and stable catalyst.There are two main problems for the current load type Ni/SiO2 catalyst,one is the sintering of Ni particles,the other one is carbon deposition.The first part of this dissertation we study the dispersion and catalytic activity of the load type Ni/SiO2 catalysts prepared by different prescursors;We focus on the study of preparation mechanism about nano Ni/SiO2 catalyst prepared by Ni?acac?2 prescursor;The second part of this article we preliminarily explored the effect and modification mechanism of ammonia modified loading Ni/SiO2 catalyst.The main results are summarized as follows:A series of Ni/SiO2 catalysts were prepared by different precursors?Ni?acac?2,Ni3?C6H5O7?2,Ni?CH3C00?2·4H2O,Ni?NO3?2·6H2O,NiCl2·6H2O?.Catalyst prepared by Ni?acac?2 has better catalytic performance in DRM.We characterized the structure and particle size of the catalysts by XRD,characterized particle size by TEM,explored the combination between SiO2 and Ni by H2-TPR,characterized carbon deposition by TG and TPO.It indicates that Ni/SiO2 catalyst prepared by Ni?acac?2 has better dispersion,more closely relationship with SiO2,less carbon deposition after DRM reaction,better anti-sinter resistance.The catalyst prepared by Ni?acac?2 showed good catalytic performance and stability for DRM reaction within 280 h,the CH4 conversion was kept at?83%,the CO2 conversion was maintained at?90%,the yield of CO and H2 were kept at?87%and-86%,the carbon balance maintained at?100%.On this basis a series of Ni/SiO2 catalysts with different Niwt%were prepared by Ni?acac?2.The BET test show that Ni/SiO2 catalysts have smaller specific surface area and pore volume than supporter SiO2;5wt%Ni/SiO2 catalyst prepared by Ni?acac?2 was high resistant to aggregate of Ni particles.The size and dispersion of Ni particles were still maintain well?<5 nn?even after calcined at 900 ? for 2 h or calcined at 800 ? for 20 h;Analogy our groups previous conclusion 9wt%Pd/SiO2 is the biggest monolayer coverage of Pd?acac?2 on SiO2 we caculate the biggest monolayer coverage of Ni?acac?2 on SiO2 is 7wt%.In-situ IR characterization of catalysts prepared by Ni?acac?2 with different Ni loading show the sharp band?3737 cm-1?belongs to free silanol group decreases significantly in intensity with the increase of Ni?acac?2 loading,whereas those of the hydrogen bonded OH species?3000-3800 cm-1?increase in intensity.This result indicates that the organic group of Ni?acac?2 interacts with free silanol group of SiO2 surface through hydrogen bond.As long as the loading of Ni?acac?2 lower than the limitation of monolayer?7wt%Ni/SiO2?the Ni particles will uniformly disperse on the surface of SiO2.TEM and H2-TPR characterization of catalysts prepared by Ni?acac?2 with different Ni loading show the paticle size of Ni maintain small and the relationship with supported SiO2 were more closely when Ni loading was below 7wt%.NH3·H2O can increase the anti-sinter resistance,dispersion of Ni particles,catalytic performance of DRM for catalysts prepared by Ni?NO3?2·6H2O.The results of TG and in situ IR show that Ni?NO3?2·6H2O and ammonia form coordination complex when co-impregnation which can promote the dispersion of nickel on supporter;Characterization of BET,in situ IR and conventional IR show that ammonia affects the surface Si-OH skeleton;The results of H2-TPR,TEM and XPS show that Ni?NO3?2·6H2O,ammonia and SiO2 form nickel silicate after co-impregnation for 12 h and calcination at 800 ? for 2 h.Nickel silicate has a strong interaction with the silica supporter,good dispersion and excellent catalytic performance after the reduction;The higher concentration of ammonia and stronger alkaline environment has a positive effect on the dispersion of Ni particles.
Keywords/Search Tags:Dry reforming of methane, Ni/SiO2 catalysts, Sintering, Carbon deposition, Precursors, Ni?acac?2, Formation mechanism, Ni?NO3?2·6H2O, NH3·H2O modification
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