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Direct Synthesis Of Hydrogen Peroxide From H2/O2 And Integration Thereof Into Oxidative Reactions Over Au/TS-1

Posted on:2009-08-16Degree:DoctorType:Dissertation
Country:ChinaCandidate:S Q MaFull Text:PDF
GTID:1101360272970220Subject:Industrial Catalysis
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Hydrogen peroxide is an important green oxidizing agent.It is used in many industrial areas,such as textile industry,papermaking,chemical industry and environmental protection. The current industrial production of H2O2 involves a circular reaction pathway by the sequential hydrogenation and oxidation of alkyl-anthraquinone.However,this process has several obvious drawbacks,including complex operation steps,high cost and safety issue in transportation and storage.Consequently,alternative routes for H2O2 synthesis are highly desirable.The direct synthesis of H2O2 from O2 and H2 over a precious metal catalyst is an attractive alternative,which has been investigated for almost one century.Recently,supported gold nanoparticles proved to be a potential catalyst for direct H2O2 formation from H2 and O2. Familiar supports for gold catalyst are TiO2,Al2O3,SiO2,Fe2O3,active carbon,et al.Since titanium silicalite TS-1 was successfully prepared in 1983,it has exhibited the unique catalytic performance in many selective oxidation reactions involving H2O2 as the oxidant.Several reactions exhibit the potential for an industrial process,including propene epoxidation,ammoxidation of cyclohexanone and hydroxylation of phenol et al.However,the high cost and the problem of transportation and storage of commercial H2O2 have limited the industrial application of TS-1.In this paper,a bifunctional catalyst Au/TS-1 is prepared and employed in the direct synthesis of H2O2 from O2 and H2.The conditions of catalyst preparation and reaction are systematically studied.On the basis of the direct synthesis of H2O2 from O2 and H2,oxidative desulfurization and 1-butylene epoxidation are attempted over Au/TS-1 in the presence of O2 and H2.The following results have been obtained:1.Several supported gold catalysts are prepared by the method of deposition-precipitation with urea(DP urea) and used in the direct syntheis of H2O2 using deionized water as reaction medium at room temperature.TiO2 supported gold catalyst exhibits the highest activity,followed by Au/TS-1,Au/Al2O3,Au/Fe2O3,and SiO2. Preparation methods of the Au/TS-1 catalyst influence the catalytic activity in the direct synthesis of hydrogen peroxide.The catalyst,which contains smaller gold particles,.exhibits a higher catalystic activity.2.Effects of the preparation condition of Au/TS-1 catalysts and reaction conditions on the direct synthesis of H2O2 are systemically investigated.Results show that Au3+ and Au+ are mainly gold species on the Au/TS-1 catalysts dried at 40 and 100℃.These samples can not catalytze the formation of hydrogen peroxide.With increasing of calcination temperature from 200~400℃,the Au3+ and Au+ species are gradually reduced to metallic Au0,and the catalytic activity increases.Metallic gold species Au0 is proposed as the active species in the direct synthesis of hydrogen peroxide.With the amount of urea increasing during the preparation process of the Au/TS-1 catalyst,the final pH value of solvent increases,and samller gold nanoparticles are formed.The catalytical activity and the stability of the Au/TS-1 catalyst are also improved.The increase of Ti content in Au/TS-1 can result in the increase of catalytical activity.Instead of deionized water as reaction solvent,methanol is a rather suitable medium for H2O2 synthesis.However,a higher catalytic activity can be obtained using a water-methanol mixture as the solvent,and the optimal water/methanol volume ratio is 3:2.3.Oxidative desulfurization is investigated over bifunctional Au/TS-1 catalyst in the presence of H2 and O2.Results show that methyl sulfide(DMS) can be very seaily oxidized by H2O2 generated in situ.For the effect of steric hindrance,the oxidation rate of 2-methyl thiophene is lower than DMS and thiophene.With increasing reaction time,the removal of sulfide can be improved continuously.The temperatrue has a singnificant effect on the removal of thiophene.With increasing reaction temperature,the removal is higher than that at room temperature,and the optimum temperature is 40℃.The mechanism of oxidative desulfurization by in situ generated H2O2 over Au/TS-1 is similar with that in the system TS-1/H2O2.The sufides are oxidized to sub-sulfone,sulfone,sulfur dioxide and sulfuric acid.4.Using bifunctional Au/TS-1 as catalyst,epoxidation of 1-butylene is investigated in the presence of H2 and O2.The result shows that high temparature is disadvantageous to the synthesis of hydrogen peroxide,but favor the 1-butylene epoxidation.A highest formation rate of 1,2-butylene oxide(BO) is obtained at 40℃.With increasing reaction time,the amount of BO increases and the fomation rate keep at about 0.54~0.6 g/(gAu h).Increasing the Ti content of Au/TS-1 can also improve the formation of BO.The selectivity of BO is 100% when the integration is performed at room temperature.
Keywords/Search Tags:Titanium silicalite, Gold catalysis, Hydrogen peroxide, Direct synthesis, 1-Butylene, Epoxidation, Oxidative desulphurization
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