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Producing clean diesel fuel by co-hydrogenation of vegetable oil with gas oil

机译:通过植物油和瓦斯油的加氢生产清洁柴油

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The goal of our investigation was the production of partially bio-derived fuels in the gas oil boiling point range. Our aim was the production of diesel fuel blending components by co-hydrogenation of mixtures of high-sulphur gas oil (about 1.0%) and vegetable oil raw materials with different vegetable oil contents (0, 5, 15, 25 and 100%). The experiments were carried out on a NiMo/ Al_2O_3 catalyst with a targeted composition (T = 300-380℃, P = 60-80 bar, LHSV = 1.0/h and H2/HC = 600 Nm~3/m~3). We obtained that both the vegetable oil conversion reactions and the gas oil quality improvement reactions took place. Under the favourable operational conditions (360-380℃, P = 80 bar, LHSV = 1.0/h and H_2/HC = 600 Nm~3/m~3 and up to 15% vegetable oil content of the feed), the main properties of the high-yield (>90%) products except for the Cold Filter Plugging Point (CFPP) value satisfied the requirements of the standard of diesel fuels (EN 590:2009). The amount of vegetable oil higher than 15% reduced the desulphurization efficiency, because of the intake of large quantities of oxygen with the triglyceride molecules of the vegetable oil. The products— depending on the vegetable oil content of the feedstocks— have an increased n- and i-paraffin content, so their combustion properties are very favourable, and the emission of particles is lower.
机译:我们研究的目标是生产在汽油沸点范围内的部分生物来源的燃料。我们的目标是通过将高硫瓦斯油(约1.0%)和具有不同植物油含量(0、5、15、25和100%)的植物油原料的混合物进行加氢生产柴油混合组分。实验是在具有目标组成(T = 300-380℃,P = 60-80 bar,LHSV = 1.0 / h和H2 / HC = 600 Nm〜3 / m〜3)的NiMo / Al_2O_3催化剂上进行的。我们获得了植物油转化反应和瓦斯油质量改善反应均发生的结果。在良好的操作条件下(360-380℃,P = 80 bar,LHSV = 1.0 / h和H_2 / HC = 600 Nm〜3 / m〜3且进料中植物油含量最高为15%),主要性能除冷滤塞点(CFPP)值外,其余高收率产品(> 90%)均满足柴油标准(EN 590:2009)的要求。高于15%的植物油含量会降低脱硫效率,因为植物油的甘油三酸酯分子会吸收大量的氧气。根据原料的植物油含量,产品的正链烷烃和异链烷烃含量会增加,因此它们的燃烧性能非常好,并且颗粒排放量更低。

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