Ni/SBA-15催化剂上乙酰丙酸加氢反应的研究

IF 0.125
Mohan Varkolu, Hari Babu Bathula, Young-Woong Suh, David Raju Burri, Seetha Rama Rao Kamaraju
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引用次数: 5

摘要

采用浸渍法制备了一系列Ni/SBA-15催化剂,用于乙酰丙酸(LA)在固定床常压下加氢制γ-戊内酯。采用XRD、TPR、AAS、脉冲化学吸附、SEM-EDAX、TEM、BET比表面积和XPS对催化剂进行了表征。催化剂?wt% Ni/SBA-15在250℃时表现出优异的催化性能(97%收率)。由于存在大量的活性表面镍。而30 ?wt% Ni/SiO2催化剂的催化活性较低,转化率为87%。甲酸(FA)和水(杂质)与乙酰丙酸共投喂的效果也在30?wt% Ni/SBA-15产生了优异的乙酰丙酸转化率。当FA/LA的摩尔比为5时,得到了显著的结果。在10?h外H2流实验表明了Ni/SBA-15催化剂的坚固性。另一方面,在没有外部H2流动的情况下,转化率和产率略有下降,这是由于碳种在催化剂表面的积累。
本文章由计算机程序翻译,如有差异,请以英文原文为准。

Hydrogenation of levulinic acid with and without external hydrogen over Ni/SBA-15 catalyst

Hydrogenation of levulinic acid with and without external hydrogen over Ni/SBA-15 catalyst

A series of Ni/SBA-15 catalysts were prepared by impregnation method for the hydrogenation of levulinic acid (LA) to γ-valerolactone in a fixed bed reactor at atmospheric pressure. The catalysts were characterized by XRD, TPR, AAS, Pulse chemisorption, SEM-EDAX, TEM, BET Surface area and XPS. The catalyst 30?wt% Ni/SBA-15 exhibited excellent catalytic performance (97% yield) at 250?°C due to the presence of superior number of active surface Ni species. While 30?wt% Ni/SiO2 catalyst showed lower catalytic activity (87% yield) at about similar conversion. The co-feeding of formic acid (FA) and water (impurities) with levulinic acid was also evaluated over 30?wt% Ni/SBA-15 which yielded excellent levulinic acid conversion. The noteworthy results were obtained at a molar ratio of FA/LA?=?5. The constant catalytic activity during 10?h experiment with an external H2 flow has showed the sturdiness of the Ni/SBA-15 catalyst.?On the other hand, a slight decrease in conversion as well as yield during the time-on-stream in the absence of external H2 flow was attributed to the accumulation of carbon species on the catalyst surface.

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来源期刊
Applied Petrochemical Research
Applied Petrochemical Research ENGINEERING, CHEMICAL-
自引率
0.00%
发文量
0
审稿时长
13 weeks
期刊介绍: Applied Petrochemical Research is a quarterly Open Access journal supported by King Abdulaziz City for Science and Technology and all the manuscripts are single-blind peer-reviewed for scientific quality and acceptance. The article-processing charge (APC) for all authors is covered by KACST. Publication of original applied research on all aspects of the petrochemical industry focusing on new and smart technologies that allow the production of value-added end products in a cost-effective way. Topics of interest include: • Review of Petrochemical Processes • Reaction Engineering • Design • Catalysis • Pilot Plant and Production Studies • Synthesis As Applied to any of the following aspects of Petrochemical Research: -Feedstock Petrochemicals: Ethylene Production, Propylene Production, Butylene Production, Aromatics Production (Benzene, Toluene, Xylene etc...), Oxygenate Production (Methanol, Ethanol, Propanol etc…), Paraffins and Waxes. -Petrochemical Refining Processes: Cracking (Steam Cracking, Hydrocracking, Fluid Catalytic Cracking), Reforming and Aromatisation, Isomerisation Processes, Dimerization and Polymerization, Aromatic Alkylation, Oxidation Processes, Hydrogenation and Dehydrogenation. -Products: Polymers and Plastics, Lubricants, Speciality and Fine Chemicals (Adhesives, Fragrances, Flavours etc...), Fibres, Pharmaceuticals.
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