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首页> 外文期刊>Fuel Processing Technology >Hydrorefining of oil from rapeseed cake pyrolysis over NiMo/Al2O3 catalyst
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Hydrorefining of oil from rapeseed cake pyrolysis over NiMo/Al2O3 catalyst

机译:NiMo / Al2O3催化剂对菜籽饼热解油的加氢精制

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摘要

Bio-oil from rapeseed cake pyrolysis, bio-oil fraction boiling over 120 °C and bio-oil blended with light gas oil fraction were submitted to the hydrorefining studies. The usability of NiMo/Al2O3 catalyst for pyrolytic oil hydrorefining was tested at the following parameters: temperature (290-350 °C), LHSV (0.5-2.0 h~(-1)) and 3 MPa hydrogen pressure. The influence of hydrorefining parameters on the physicochemical properties and chemical composition of the obtained products was evaluated. Hydrorefining of raw bio-oil at the temperature of 350 °C 2.0 h~(-1) and 3 MPa of H2 resulted in unsatisfactory level of refining. Removal of low boiling fraction and LHSV until the value of 0.5 h~(-1) was reached allowed to deepen the degree of hydrorefining up to the levels of 71.4% of HDS, 29.0% of HDN and 78.8% of HDO. These hydrorefining products cannot be used as internal combustion engine liquid fuels or as their components. Blending of the bio-oil (20% v/v) with petroleum-derived oil fraction and subjecting it to a hydrorefining process made it possible to obtain a fuel component of relatively good quality.
机译:来自菜籽饼热解的生物油,沸点超过120°C的生物油馏分以及与轻质瓦斯油馏分混合的生物油已提交加氢精制研究。在以下参数下测试了NiMo / Al2O3催化剂在热解油加氢精制中的可用性:温度(290-350°C),LHSV(0.5-2.0 h〜(-1))和3 MPa氢气压力。评估了加氢精制参数对所得产物的理化性质和化学组成的影响。原始生物油在350°C 2.0 h〜(-1)和3 MPa H2的条件下进行加氢精制导致精制水平不理想。除去低沸点馏分和LHSV直至达到0.5 h〜(-1)值,可使加氢精制程度加深至HDS 71.4%,HDN 29.0%和HDO 78.8%。这些加氢精制产品不能用作内燃机液体燃料或用作其组分。将生物油(20%v / v)与石油衍生的油馏分混合并对其进行加氢精制过程,可以得到质量相对较高的燃料成分。

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