催化作用
氢解
金属间化合物
双金属片
扩展X射线吸收精细结构
镍
煅烧
材料科学
无机化学
选择性
X射线光电子能谱
氧烷
化学
化学工程
冶金
有机化学
吸收光谱法
合金
工程类
物理
量子力学
光谱学
作者
Elmira Soghrati,Chee Kok Poh,Yonghua Du,Feng Gao,Sibudjing Kawi,Armando Borgna
出处
期刊:Chemcatchem
[Wiley]
日期:2018-09-26
卷期号:10 (20): 4652-4664
被引量:33
标识
DOI:10.1002/cctc.201800783
摘要
Abstract In this study, we report a series of bimetallic Ni−WO x catalyst for the ring‐opening of THFA into 15PDO. The structure‐performance relationship of the catalysts was discussed based on extensive characterization using techniques such as BET, H 2 ‐TPR, NH 3 ‐TPD, Pyr‐IR, IPA‐TPD‐MS, XRD, XPS and EXAFS/XANES. The acidity measurements show that higher W density leads to the higher amount of acid density, which could be assigned to the creation of Lewis acid sites mainly on the surface of the calcined catalysts. H 2 ‐TPR profiles of Ni−WO x catalysts show that there is a strong interaction between Ni and W species, enhancing the reducibility of WO x . XRD measurements of calcined Ni−WO x catalysts reveal that the dispersion of Ni particles is enhanced after addition of WO x species. After reduction, different peaks corresponding to metallic Ni and WO 3−x are identified for 10Ni−WO x catalysts, as well as new peak assigned to Ni−W intermetallic phase on 10Ni−30WO x catalyst. The formation of Ni−W intermetallic phase was further proved using XPS and EXAFS studies. THFA hydrogenolysis was also conducted under aqueous‐phase conditions over Ni−WO x catalysts, yielding up to 47 % selectivity to 15PDO, along with a highest combined C 5 polyols (i. e., 15PDO and 125PTO) selectivity of approximately 64 %. However, the Ni−WO x catalytic system suffers from deactivation process due to the hydrothermal dissolution of the active phase. Further investigation reveals the better stability of metallic tungsten and Ni−W intermetallic phase (Ni 4 W) against leaching since their corresponding peaks in the XRD patterns of spent catalysts remains nearly unchanged. Finally, 1,4‐dioxane as an organic solvent was employed in THFA hydrogenolysis reaction, resulting in different product distribution, with a THP yield of around 54 %. The catalyst crystalline structure is preserved because of very low Ni and W leaching when 1,4‐dioxane is used as solvent.
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