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Catalytic Properties of CoMo/Al_2O_3 Sulfide Catalysts in the Hydrorefining of Straight-Run Diesel Fraction Mixed with Rapeseed Oil

机译:CoMo / Al_2O_3硫化物催化剂在菜籽油直馏柴油馏分加氢精制中的催化性能

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CoMo/Al_2O_3 sulfide catalysts varying in preparation method and Co/Mo ratio have been tested in the hydrorefining of a mixture of straight-run diesel fraction and rapeseed oil in a flow reactor at a temperature of 340–360°C, a hydrogen pressure of 4.0–7.0 MPa, and a liquid hourly space velocity of 1–2 h~(–1). A comparison between catalysts prepared using citric acid (CoMo/Al_2O_3-1.5) and both citric and orthophosphoric acids (CoMoP/Al_2O_3-1.5) as promoters, with Co/Mo = 0.3 and 0.5, has demonstrated that the most active catalyst in hydrodesulfurization and hydrodenitrogenation is the phosphorus-containing Co/Mo ≈ 0.5 sample. The addition of rapeseed oil to straight-run diesel fraction lowers the hydrodesulfurization and hydrodenitrogenation activities of the CoMo sulfide catalysts, irrespective of the method by which they were prepared. The fatty acid triglyceride conversion selectivity of these catalysts depends on the Co/Mo ratio and on reaction conditions: decreasing the Co/Mo ratio from 0.46 to 0.26, lowering the reaction temperature, and raising the hydrogen pressure and hydrogen-to-feedstock ratio increase the C_(18)/C_(17) hydrocarbon ratio in the hydrogenated product. The addition of rapeseed oil improves the quality of the product; however, for attaining the preset residual sulfur level in this case, the process needs to be conducted at a higher temperature than the hydrorefining of straight-run diesel fraction containing no admixture.
机译:制备方法和Co / Mo比不同的CoMo / Al_2O_3硫化物催化剂已在流式反应器中在340–360°C,氢气压力为4.0–7.0 MPa,液时空速为1-2 h〜(–1)。使用柠檬酸(CoMo / Al_2O_3-1.5)和柠檬酸和正磷酸(CoMoP / Al_2O_3-1.5)作为助催化剂制备的催化剂(Co / Mo = 0.3和0.5)之间的比较表明,加氢脱硫和加氢脱氮是含磷的Co / Mo≈0.5样品。将菜籽油添加到直馏柴油馏分中会降低CoMo硫化物催化剂的加氢脱硫和加氢脱氮活性,而与制备方法无关。这些催化剂的脂肪酸甘油三酸酯转化选择性取决于Co / Mo比和反应条件:将Co / Mo比从0.46降低到0.26,降低反应温度,并提高氢气压力和氢气/原料比增加氢化产物中的C_(18)/ C_(17)烃比。添加菜籽油可提高产品质量;然而,在这种情况下,为了达到预设的残留硫含量,该方法需要在比不包含混合物的直馏柴油馏分的加氢精制更高的温度下进行。

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