Hydrodeoxygenation of palm oil to hydrocarbon fuels over Ni/SAPO-11 catalysts

Catalytic upgrading of vegetable oils into jet fuels range hydrocarbons using heterogeneous catalysts: A review

“…A similar trend could be observed by increasing the loading of Ni particles. When the loading was increased from 2 to 7 and 9 wt.%, the selectivity to alkanes increased from 60 to 67 and 68%, respectively [80]. Table 2 here.…”

“…A summary of some recent studies on the behaviors of the transition metals-based catalysts during the hydroprocessing of some vegetable oils under variable conditions has also been presented in Table 2 [77], [78], [79], [80], [81], [82], [83], [84]. In all the cases, the reactions proceed via the HDO/HDC mechanism, with the side reactions being mainly of methanation and watergas types.…”

Development of nickel based catalysts for the transformation of natural triglycerides and related compounds into green diesel: a critical review

“…In the context of the same effort a SAPO-11 support with small particles and large surface area and mesoporosity was also synthesized hydrothermally [116] (Table 2, entry 6). Using this support Ni/SAPO-11 catalysts with different Ni loadings (2, 7 and 9%) were prepared by wet impregnation.…”

Study on palm oil hydrogenation for clean fuel over Ni–Mo–W/γ-Al 2 O 3 –ZSM-5 catalyst

“…The conversion decreased in the following order under the investigated reaction condition: Ni-Mo-W N Ni-Mo N Ni. In comparison, Ni/SAPO-11 catalysts in previous research gave a liquid alkane yield of 70 wt.% in the same process [31]. Thus, Mo and W acted as activity promoters of Ni catalysts in the deoxygenation of palm oil.…”