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Temperature Dependence of Single Step Hydrodeoxygenation of Liquid Phase Pyrolysis Oil

机译:液相热解油一步加氢脱氧反应的温度依赖性

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摘要

In this paper, continuous hydrodeoxygenation (HDO) of liquid phase pyrolysis (LPP) oil in lab-scale is discussed. Pyrolysis oil is derived from the bioCRACK pilot plant from BDI - BioEnergy International GmbH at the OMV refinery in Vienna/Schwechat. Three hydrodeoxygenation temperature set points at 350, 375, and 400°C were investigated. Liquid hourly space velocity (LHSV) was 0.5 h−1. Hydrodeoxygenation was performed with an in situ sulfided metal oxide catalyst. During HDO, three product phases were collected. A gaseous phase, an aqueous phase and a hydrocarbon phase. Experiment duration was 36 h at 350 and 375°C and 27.5 h at 400°C in steady state operation mode. Water content of the hydrocarbon phase was reduced to below 0.05 wt.%. The water content of the aqueous phase was between 96.9 and 99.9 wt.%, indicating effective hydrodeoxygenation. The most promising results, concerning the rate of hydrodeoxygenation, were achieved at 400°C. After 36/27.5 h of experiment, catalyst deactivation was observed.
机译:本文讨论了实验室规模的液相热解(LPP)油的连续加氢脱氧(HDO)。热解油来自BDI-BioEnergy International GmbH位于维也纳/ Schwechat的OMV精炼厂的bioCRACK中试工厂。研究了三个加氢脱氧温度设定点,分别为350、375和400°C。液时空速(LHSV)为0.5 h -1 。用原位硫化的金属氧化物催化剂进行加氢脱氧。在HDO期间,收集了三个产品阶段。气相,水相和烃相。在稳态操作模式下,实验持续时间在350和375°C下为36 h,在400°C下为27.5 h。烃相的水含量降低到0.05重量%以下。水相的水含量为96.9-99.9重量%,表明有效的加氢脱氧。关于加氢脱氧速率的最有希望的结果是在400°C下获得的。在36 / 27.5小时的实验后,观察到催化剂失活。

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