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In-situ upgrading of bio-tar over Mg-Ni-Mo catalyst supported by KOH treated activated charcoal in supercritical ethanol

机译:KOH处理的活性炭在超临界乙醇中负载的Mg-Ni-Mo催化剂上生物焦油的原位提质

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In-situ catalytic hydrodeoxygenation (HDO) of bio-tar in supercritical ethanol for upgraded biofuel was investigated. Highly mesoporous KOH-treated AC (KOH-AC) was synthesized by chemical activation and used as the support for Ni-based catalysts. Among the tested catalysts (AC, KOH-AC, Mg-Ni-Mo/AC, and Mg-Ni-Mo/KOH-AC), Mg-Ni-Mo/KOH-AC with a high surface area of 1310.1 m(2)/g and a well-developed mesoporous structure exhibited much higher catalytic performance for the HDO of bio-tar. The effects of different reaction temperatures (300-400 degrees C) and residence time (0-120 min) on the HDO of bio-tar over Mg-Ni-Mo/KOH-AC were also examined. Enhanced properties of liquid fuel with a higher heating value (HHV) of 36.2 MJkg(-1), an oxygen content of 11.7 wt%, and a total acid number (TAN) value of 8.6 mgKOHg(-1) were obtained from bio-tar over a Mg-Ni-Mo/KOH-AC at 400 degrees C for 120 min. In these conditions, acids, aldehydes, and oxygenated phenols present in bio-tar ( > 67 area%) were effectively converted to high value-added species including aromatics, hydrocarbons, and alkyl phenols in upgraded bio-tar ( > 77 area%) via esterification, hydrogenation, deoxygenation, and ring-alkylation reactions. A series of Mg-Ni-Mo/KOH-AC catalyst recycle test showed the deposition of coke on the catalyst, which became a major reason for the catalyst deactivation.
机译:研究了超临界乙醇中生物焦油的原位催化加氢脱氧(HDO),用于升级生物燃料。高度介孔的KOH处理过的AC(KOH-AC)通过化学活化合成,并用作Ni基催化剂的载体。在经过测试的催化剂(AC,KOH-AC,Mg-Ni-Mo / AC和Mg-Ni-Mo / KOH-AC)中,Mg-Ni-Mo / KOH-AC的高表面积为1310.1 m(2 )/ g和发达的介孔结构对生物焦油的HDO表现出更高的催化性能。还研究了不同反应温度(300-400摄氏度)和停留时间(0-120分钟)对生物焦油在Mg-Ni-Mo / KOH-AC上的HDO的影响。从生物燃料中获得了更高的热值(HHV)为36.2 MJkg(-1),氧含量为11.7 wt%,总酸值(TAN)为8.6 mgKOHg(-1)的液体燃料。在400摄氏度的Mg-Ni-Mo / KOH-AC上焦油干燥120分钟。在这些条件下,生物焦油中存在的酸,醛和氧化酚(> 67面积%)被有效地转化为高附加值的物种,包括升级版生物焦油中的芳烃,碳氢化合物和烷基酚(> 77面积%)通过酯化,氢化,脱氧和环烷基化反应。一系列的Mg-Ni-Mo / KOH-AC催化剂循环测试表明,焦炭在催化剂上沉积,这成为催化剂失活的主要原因。

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