Preparation of Metal-Acid bifunctional catalyst Ni/ZSM-22 for palmitic acid catalytic deoxygenation

被引:13
|
作者
Li, Xiaoxian [1 ]
Lin, Min [2 ]
Li, Rui [2 ]
Lu, Qiang [3 ]
Yang, Mingde [1 ,4 ]
Wu, Yulong [1 ,4 ]
机构
[1] Tsinghua Univ, Inst Nucl & New Energy Technol, Beijing 100084, Peoples R China
[2] Beijing Forestry Univ, MOE Engn Ctr Forestry Biomass Mat & Bioenergy, Beijing 100083, Peoples R China
[3] North China Elect Power Univ, Natl Engn Res Ctr New Energy Power Generat, Beijing 102206, Peoples R China
[4] Tsinghua Univ, Key Lab Adv Reactor Engn & Safety, Minist Educ, Beijing 100084, Peoples R China
基金
中国国家自然科学基金; 国家重点研发计划;
关键词
Bio-oil; Hydrodeoxygenation; Palmitic acid; Bifunctional Catalyst; DIESEL-RANGE ALKANES; FATTY-ACIDS; HYDROTHERMAL DECARBOXYLATION; PRODUCT DISTRIBUTION; ISO-ALKANES; BIO-OIL; HYDRODEOXYGENATION; NICKEL; NANOPARTICLES; HYDROGENATION;
D O I
10.1016/j.fuel.2022.126139
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
In this work, methods employing ethanol for dispersion as well as precursor combination by rotary evaporation were combined to produce Ni-based ZSM-22 catalysts. The catalytic activity in palmitic acid deoxygenation over Ni/Z22@E was enhanced compared with that of the wet-impregnated method. The conversion of palmitic acid reached 98.9 %, in which C16/C15 alkane was as high as 4.07. The Ni species on the surface of catalysts showed strong stability so that not susceptible to inactivation by coking or leaching. In addition, the mechanism and kinetics of the palmitic acid deoxygenation reaction were analyzed. The results showed that the ethanol dehy-dration reaction was the most difficult to occur, and the high C16 alkanes selectivity can be attributed to the low activation energy of the hydrodeoxygenation (HDO) pathway. Both experimental and kinetics calculation results suggested that there may be a mechanistic change in the fatty acid deoxygenation reaction at around 240 degrees C that resulted in a large increase in the hydrodecarboxylation (HDX) pathway. Based on this, selected adjustments of the products were proposed for fatty alcohols below 220 degrees C, C16 alkanes between 260 and 280 degrees C, and C15 al-kanes above 280 degrees C.
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页数:13
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