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Optimization of Bio-Hydrogenated Kerosene from Refined Palm Oil by Catalytic Hydrocracking

机译:催化加氢裂化法优化精制棕榈油中的生物加氢煤油

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In this work, hydro-processing was used as an alternative route for producing bio-hydrogenated kerosene (BHK) from refined bleached deodorized palm oil (RPO) in the presence of a 0.5 wt% Pd/Al 2 O 3 catalyst. The Box-Behnken Design was used to determine the effects of reaction temperature, H 2 pressure, and reaction time in terms of liquid hourly space velocity (LHSV) on BHK production. The kerosene selectivity was used as the response for staticial interpretation. The results show that both temperature and LHSV produced significant effects, whereas H 2 pressure did not. The optimal conditions were found to be 483 °C, 5.0 MPa, and 1.4 h ?1 LHSV; these conditions provided approximately 57.30% kerosene selectivity and a 47.46% yield. The BHK product had a good heating value and flash point. However, the mass percentage of carbon and hydrogen was 99.1%, which is just below the minimum standard (99.5%), according to the carbon loss by the reaction pathway to form as CO and CO 2 . Water can be produced from the reaction induced by oxygen removal, which results in a high freezing point.
机译:在这项工作中,加氢处理被用作在0.5 wt%Pd / Al 2 O 3催化剂存在下从精制漂白脱臭棕榈油(RPO)中生产生物氢化煤油(BHK)的替代途径。 Box-Behnken设计用于确定反应温度,H 2压力和反应时间(以液时空速(LHSV)表示)对BHK生产的影响。煤油的选择性用作静态解释的响应。结果表明,温度和LHSV均产生显着影响,而H 2压力则没有。发现最佳条件为483°C,5.0 MPa和1.4 h?1 LHSV。这些条件提供了约57.30%的煤油选择性和47.46%的产率。 BHK产品具有良好的发热量和闪点。然而,根据通过形成CO和CO 2的反应路径的碳损失,碳和氢的质量百分比为99.1%,刚好低于最低标准(99.5%)。从除氧引起的反应中会产生水,导致冰点高。

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