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焙烧及还原条件对Ni2P/TiO2-Al2O3催化剂加氢脱硫性能的影响
引用本文:苑丹丹,张永江,李锋,宋华.焙烧及还原条件对Ni2P/TiO2-Al2O3催化剂加氢脱硫性能的影响[J].化工进展,2015,34(6):1656.
作者姓名:苑丹丹  张永江  李锋  宋华
作者单位:1.东北石油大学化学化工学院, 黑龙江 大庆 163318;2.东北石油大学石油与天然气化工省重点实验室, 黑龙江 大庆 163318
基金项目:国家自然科学基金,黑龙江省自然基金,黑龙江省教育厅项目(12541080)。
摘    要:采用溶胶-凝胶法制备了TiO2-Al2O3复合载体, 以柠檬酸(CA)为络合剂采用浸渍法制备了Ni2P负载的TiO2-Al2O3复合载体催化剂, 并用 X 射线衍射(XRD)、N2吸附比表面积(BET)测定技术对催化剂的结构和性质进行了表征, 考察了载体焙烧温度、催化剂焙烧温度、还原温度、还原压力对其进行的二苯并噻吩(DBT)加氢脱硫(HDS)性能的影响。结果表明, 升高载体焙烧温度有利于催化剂表面上活性物种的分散, 但焙烧温度过高会导致催化剂烧结, 适宜的载体焙烧温度为550℃。当还原温度为500~550℃时, 磷化镍主要以Ni12P5相形式存在, 且随着还原温度的升高, Ni12P5的衍射峰强度逐渐增强, 还原温度为700℃时, 可得到单一的Ni2P物相。载体焙烧温度为550℃, 催化剂焙烧温度为500℃, 还原温度为700℃, 常压还原制备的Ni2P/TiO2-Al2O3催化剂具有最好的活性。在360℃、3.0MPa、氢油体积比500、液时体积空速2.0h-1的条件下, 反应4h时, DBT转化率为99.5 %。

关 键 词:磷化二镍  催化剂  加氢脱硫  柠檬酸  制备  
收稿时间:2014-10-13

Effect of calcination and reduction conditions on hydrodesulfurization performance of the Ni2P/TiO2-Al2O3 catalyst
YUAN Dandan,ZHANG Yongjiang,LI Feng,SONG Hua.Effect of calcination and reduction conditions on hydrodesulfurization performance of the Ni2P/TiO2-Al2O3 catalyst[J].Chemical Industry and Engineering Progress,2015,34(6):1656.
Authors:YUAN Dandan  ZHANG Yongjiang  LI Feng  SONG Hua
Affiliation:1 College of Chemistry & Chemical Engineering, Northeast Petroleum University, Daqing 163318, Heilongjiang, China;2 Provincial Key Laboratory of Oil & Gas Chemical Technology, Northeast Petroleum University, Daqing 163318, Heilongjiang, China
Abstract:The TiO2-Al2O3 complex support was prepared by sol-gel method. A nickel phosphide catalyst, Ni2P/TiO2-Al2O3 with citric acid (CA) as chelating agent, was prepared by the impregnation method. The catalysts were characterized by X-ray diffraction (XRD) and N2-adsorption specific surface area measurements (BET). The effects of calcination temperature of support, calcination temperature of catalyst, reduction temperature, reduction pressure and calcination time of catalyst on catalyst activity for dibenzothiophene (DBT) hydrodesulfurization (HDS) were studied. The result showed that increasing the calcination temperature of support favored dispersion of active species on catalyst surface. The optimal calcination temperature of support was 550℃ because of catalyst sintered by excessive temperature. When reduction temperature was in the reange of 500—550℃, the active phase was mixed phases of Ni12P5 and Ni2P. The peak intensities of Ni12P5 increased with the reduction temperature increasing. At reduction temperature of 700℃, the single Ni2P phase was observed. The Ni2P/TiO2-Al2O3 catalyst prepared under a support calcination temperature of 550℃, a catalyst calcination temperature of 500℃, a reduction temperature of 700℃ under atmospheric pressure was found to be optimal. At reaction temperature of 360℃, pressure of 3.0MPa, hydrogen/oil ratio of 500 (V/V), and liquid hourly space velocity of 2.0h-1, the conversion of dibenzothiophene HDS was 99.5% in 4h.
Keywords:nickel phosphide  catalyst  hydrodesulfurization  citric acid  preparation
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