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作 者:包建国[1] 龚建议[1] 杨运泉[1,2] 陈卓[1] 蒋新民
机构地区:[1]湘潭大学化工学院,湖南湘潭411105 [2]湘潭大学绿色催化与反应工程湖南省普通高校重点实验室,湖南湘潭411105
出 处:《石油化工》2010年第1期42-46,共5页Petrochemical Technology
基 金:国家自然科学基金项目(20576110);湖南省高校创新团队支持计划资助项目(06FJ4106);湖南省教育厅重点项目(05A003)
摘 要:采用共沸蒸馏-均匀沉淀法辅以超声波分散技术制备了纳米γ-Al2O3(γ-Al2O3(Ⅰ)),并以γ-Al2O3(Ⅰ)与商品γ-Al2O3(γ-Al2O3(Ⅱ))为载体,采用等体积浸渍法制得了Co与Mo负载量(分别以CoO与MoO3的质量分数计)分别为6%和16%的CoMo/γ-Al2O3(Ⅰ)与CoMo/γ-A12O3(Ⅱ)催化剂,采用间歇搅拌釜考察了催化剂的苯酚加氢脱氧性能。BET,SEM,XRD,H2-TPR,NH3-TPD表征结果表明,γ-Al2O3(Ⅰ)载体呈纤维介孔状,具有较大的比表面积、孔体积及适宜的孔分布。相对于CoMo/γ-A12O3(Ⅱ)催化剂,CoMo/γ-Al2O3(Ⅰ)催化剂的活性组分高度分散于γ-Al2O3(Ⅰ)载体表面,还原性能较高,酸中心较多。苯酚加氢脱氧反应结果表明,CoMo/γ-A12O3(Ⅰ)催化剂具有较高的加氢脱氧活性,苯酚转化率为79.2%,苯选择性为89.3%。γ-AlzO3 ( I ), which could was used as catalyst support in hydrodeoxygenation, was synthesized from Al2 ( SO4 ) 3 and NHaHCO3 through azeotropic distillation-homogeneous precipitation and ultrasonic dispersion. Both CoMo/γ-A1203 ( I ) and CoMo/γ-A12O3 ( Ⅱ ) catalysts with 6% cobalt and 16% molybdenum loadings (based on mass fractions of CoO and MoO3, respectively) were prepared through impregnation, in which γ-Al2O3 ( Ⅱ ) was a commercial support. Hydrodeoxygenations of phenol to benzene over the two CoMo/γ-A1203 catalysts were carried out in a batch stirred reactor separately. BET, SEM, XRD, Hz-TPR and NH3-TPD characterization results showed that γ-Al2O3 ( I ) support with fiber mesopore had larger surface area and pore volume as well as appropriate pore distribution. Compared with CoMo/y-A1zO3 ( Ⅱ ) catalyst, active component of CoMo/γ-Al2O3 ( I ) catalyst highly dispersed on surface of γ-A1203 ( I ). And CoMo/γ-Al2O3 ( I ) was better in reduction behavior and more in acidic sites than CoMo/γ-A1203 ( II ). Phenol conversion and benzene selectivity were 79.2% and 89.3% respectively in hydrodeoxygenation of phenol over CoMo/y-AlzO3 ( I ) catalyst.
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