以硝酸镍为镍源、酸/碱性硅溶胶为硅源,采用共沉淀法制备了2种Ni/SiO_(2)催化剂。采用固定床反应器,评价Ni/SiO_(2)催化剂对于2-甲基呋喃(2-MF)气相加氢合成2-甲基四氢呋喃(2-MTHF)的反应性能。通过XRD、N_(2)等温吸附-脱附、H_(2)-TPR...以硝酸镍为镍源、酸/碱性硅溶胶为硅源,采用共沉淀法制备了2种Ni/SiO_(2)催化剂。采用固定床反应器,评价Ni/SiO_(2)催化剂对于2-甲基呋喃(2-MF)气相加氢合成2-甲基四氢呋喃(2-MTHF)的反应性能。通过XRD、N_(2)等温吸附-脱附、H_(2)-TPR、NH3-TPD、XPS、FTIR和TEM对催化剂进行了表征。考察了硅溶胶的酸碱性对Ni/SiO_(2)催化剂结构及性能的影响。结果表明,以酸性硅溶胶为硅源制备的Ni/SiO_(2)催化剂以弱酸中心酸量为主且存在中强酸中心,比表面积、平均孔径大,因而该催化剂加氢活性和2-MTHF的选择性较高。Ni/SiO_(2)催化剂稳定性良好,在最优反应条件〔温度90℃、H_(2)压力2 MPa、质量空速4.4 g 2-MF/(g催化剂·h)、H_(2)与2-MF物质的量之比为4∶1〕下进行催化剂稳定性测试(200 h),2-MF的转化率达到99.8%,2-MTHF的选择性均保持在97.5%左右。展开更多
Product selectivity and reaction pathway are highly dependent on surface structure of heterogeneous catalysts.For vapor-phase hydrogenation of dimethyl oxalate(DMO),"EG route"(DMO→methyl glycolate(MG)ethyle...Product selectivity and reaction pathway are highly dependent on surface structure of heterogeneous catalysts.For vapor-phase hydrogenation of dimethyl oxalate(DMO),"EG route"(DMO→methyl glycolate(MG)ethylene glycol(EG)→ethanol(ET))and"MA route"(DMO→MG→methyl acetate(MA))were proposed over traditional Cu based catalysts and Mo-based or Fe-based catalysts,respectively.Herein,tunable yield of ET(93.7%)and MA(72.1%)were obtained through different reaction routes over WO_(x) modified Cu/SiO_(2) catalysts,and the corresponding reaction route was further proved by kinetic study and in-situ DRIFTS technology.Mechanistic studies demonstrated that H_(2) activation ability,acid density and Cu-WO_(x) interaction on the catalysts were tuned by regulating the surface W density,which resulted in the different reaction pathway and product selectivity.What's more,high yield of MA produced from DMO hydrogenation was firstly reported with the H_(2) pressure as low as 0.5 MPa.展开更多
文摘以硝酸镍为镍源、酸/碱性硅溶胶为硅源,采用共沉淀法制备了2种Ni/SiO_(2)催化剂。采用固定床反应器,评价Ni/SiO_(2)催化剂对于2-甲基呋喃(2-MF)气相加氢合成2-甲基四氢呋喃(2-MTHF)的反应性能。通过XRD、N_(2)等温吸附-脱附、H_(2)-TPR、NH3-TPD、XPS、FTIR和TEM对催化剂进行了表征。考察了硅溶胶的酸碱性对Ni/SiO_(2)催化剂结构及性能的影响。结果表明,以酸性硅溶胶为硅源制备的Ni/SiO_(2)催化剂以弱酸中心酸量为主且存在中强酸中心,比表面积、平均孔径大,因而该催化剂加氢活性和2-MTHF的选择性较高。Ni/SiO_(2)催化剂稳定性良好,在最优反应条件〔温度90℃、H_(2)压力2 MPa、质量空速4.4 g 2-MF/(g催化剂·h)、H_(2)与2-MF物质的量之比为4∶1〕下进行催化剂稳定性测试(200 h),2-MF的转化率达到99.8%,2-MTHF的选择性均保持在97.5%左右。
基金supported by National Natural Science Foundation of China (No.22102147 and 22002151)State Key Laboratory of Chemical Engineering (No.SKL-ChE-22A02)+2 种基金Zhejiang Provincial Natural Science Foundation of China under Grant No.LQ21B030009the Strategic Priority Research Program of the Chinese Academy of Sciences (No.XDA29050300)Qinchuang Yuan high-level innovation and entrepreneurship talents implementing project (No.QCYRCXM-2022-177)。
文摘Product selectivity and reaction pathway are highly dependent on surface structure of heterogeneous catalysts.For vapor-phase hydrogenation of dimethyl oxalate(DMO),"EG route"(DMO→methyl glycolate(MG)ethylene glycol(EG)→ethanol(ET))and"MA route"(DMO→MG→methyl acetate(MA))were proposed over traditional Cu based catalysts and Mo-based or Fe-based catalysts,respectively.Herein,tunable yield of ET(93.7%)and MA(72.1%)were obtained through different reaction routes over WO_(x) modified Cu/SiO_(2) catalysts,and the corresponding reaction route was further proved by kinetic study and in-situ DRIFTS technology.Mechanistic studies demonstrated that H_(2) activation ability,acid density and Cu-WO_(x) interaction on the catalysts were tuned by regulating the surface W density,which resulted in the different reaction pathway and product selectivity.What's more,high yield of MA produced from DMO hydrogenation was firstly reported with the H_(2) pressure as low as 0.5 MPa.
