加氢脱氧
脱碳
除氧
催化作用
植物油精炼
柴油
化学
初湿浸渍
金属
有机化学
生物柴油
选择性
作者
Atthapon Srifa,Kajornsak Faungnawakij,Vorranutch Itthibenchapong,Suttichai Assabumrungrat
标识
DOI:10.1016/j.cej.2014.09.106
摘要
Diesel-like alkanes, so-called green diesel, produced from vegetable oil, have emerged as an important biofuel to replace petroleum diesel. In the present work, the deoxygenation of palm oil to green diesel was performed in a trickle-bed reactor over four γ-Al2O3-supported monometallic catalysts (Co, Ni, Pd, and Pt). The catalysts with various metal loadings (2–10 wt.%) were prepared by the incipient wetness impregnation method and were characterized by XRD, TPR, N2 sorption, TEM, and CO pulse chemisorption. The results revealed that metallic sites of the catalysts were formed after pre-reduction in H2 with differences in metal particle size and metal dispersion on γ-Al2O3. The reaction tests revealed that the catalytic activity was in the order of Co > Pd > Pt > Ni, whereas the turnover frequency (TOF) increased with increments of the metal particle size. The decarbonylation reaction was more dominant than the hydrodeoxygenation reaction when the reaction was catalyzed by Ni, Pd, and Pt catalysts. Meanwhile, the contribution of decarbonylation and/or decarboxylation was nearly comparable to that of the hydrodeoxygenation reaction over Co catalyst. By combining the reaction tests with a model compound, oleic acid, a reaction network for the deoxygenation of palm oil was suggested and discussed.
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