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一步法植物油加氢处理制备高质量柴油烷烃。

One-step hydrotreatment of vegetable oil to produce high quality diesel-range alkanes.

机构信息

Dalian National Laboratory for Clean Energy, Dalian Institute of Chemical Physics, Chinese Academy of Sciences, 457 Zhongshan Road, Dalian 116023, PR China.

出版信息

ChemSusChem. 2012 Oct;5(10):1974-83. doi: 10.1002/cssc.201200219. Epub 2012 Jul 4.

Abstract

A one-step hydrotreatment of vegetable oil combining deoxygenation and isomerization to directly produce low cloud point, high quality diesel is devised. The Pt/zeolite bifunctional catalysts prepared by using SAPO-11 and ZSM-22 zeolites as supports are used in this process. Catalytic reactions are conducted in a fixed-bed reactor under a hydrogen atmosphere. Over the bifunctional catalyst, 100 % conversion of soybean oil is obtained at 357 °C, 4 MPa, and 1 h(-1), and 80 % organic liquid yield is achieved, which is close to the maximum theoretical liquid yield. In the organic products, the alkanes selectivity is 100 % with an i-alkanes selectivity above 63 %. NH(3)-temperature programmed desorption (TPD), pyridine IR spectroscopy, and other characterization techniques are used to study the effect of the support acidity on the reaction pathway. Over the Pt/zeolite bifunctional catalyst with less strong Lewis acid sites, the reaction proceeds via the decarboxylation plus decarbonylation pathway. This one-step method provides a new strategy to produce low cloud point, high quality diesel from biomass feedstock in a more economic and attractive way.

摘要

设计了一种一步法加氢处理植物油,将脱氧和异构化结合起来,直接生产低浊点、高质量的柴油。该过程使用 SAPO-11 和 ZSM-22 沸石作为载体制备的 Pt/沸石双功能催化剂。在氢气氛下的固定床反应器中进行催化反应。在双功能催化剂上,在 357°C、4 MPa 和 1 h(-1)的条件下,大豆油的转化率达到 100%,有机液体收率达到 80%,接近最大理论液体收率。在有机产物中,烷烃的选择性为 100%,正构烷烃的选择性高于 63%。采用 NH(3)-程序升温脱附(TPD)、吡啶红外光谱等表征技术研究了载体酸度对反应途径的影响。在具有较少强路易斯酸位的 Pt/沸石双功能催化剂上,反应通过脱羧加脱羰途径进行。这种一步法为从生物质原料生产低浊点、高质量的柴油提供了一种更经济、更有吸引力的新策略。

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