PdMoP/γ-Al2O3催化剂上大豆油甲酯加氢脱氧制备烷烃类生物柴油

Hydrodeoxygenation of soybean oil methyl esters to alkane biodiesel over the PdMoP/γ-Al2O3 catalyst

  • 摘要: 采用等体积浸渍法将Pd、Mo和P元素负载在γ-Al2O3上制得PdMoP/γ-Al2O3催化剂,通过XRD、NH3-TPD、XPS、Py-FTIR、氮吸附和STEM-EDS等手段对催化剂进行了表征,以大豆油甲酯为原料考察了催化剂的催化加氢脱氧性能,并进行了加氢脱氧工艺条件的优化。结果表明,Pd、Mo、P三种元素相结合能够有效地调节催化剂的酸性;Mo元素可降低催化剂的强酸酸性;P元素可增强催化剂的弱酸酸性,使得催化剂弱酸的B/L值减小、强酸的B/L值略有增大。经优化后的加氢工艺条件为:315 ℃、1.5 MPa、WHSV为0.5 h-1、H2/esters体积比为1100,大豆油甲酯的转化率达到98.4%,C15-18烷烃收率达到91.5%。

     

    Abstract: The PdMoP/γ-Al2O3 catalyst was prepraed through loading the Pd, Mo, and P elements on the γ-Al2O3 support by incipient impregnation method and characterized by XRD, NH3-TPD, XPS, Py-FTIR, nitrogen physisorption and STEM-EDS. The catalytic performance of PdMoP/γ-Al2O3 in the hydrodeoxygenation of soybean oil methyl ester to alkane biodiesel was invetigqated and the operation conditions were optimized. The results show that a combination of Pd, Mo and P elements can effectively adjust the catalyst acidity; Mo can reduce strong acidity, whereads P can enhance weak acidity, leading to a decrease in the B/L ratio of weak acid sites and a slight increase in the B/L ratio of strong acid sites. The optimized hydrodeoxygenation conditions are 315 ℃, 1.5 MPa, WHSV=0.5 h-1, and V(hydrogen)/V(esters)=1100; under such conditions, the conversion of soybean oil methyl esters reaches 98.4% and the C15-18 alkane yield is 91.5%.

     

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