𝔖 Bobbio Scriptorium
✦   LIBER   ✦

Activity of PNiW/Al2O3 catalysts with varying phosphorus content in the hydrogenation of naphthalene

✍ Scribed by T. Halachev; P. Atanasova; A. Lopez Agudo; M.G. Arias; J. Ramirez


Publisher
Elsevier Science
Year
1996
Tongue
English
Weight
726 KB
Volume
136
Category
Article
ISSN
0926-860X

No coin nor oath required. For personal study only.

✦ Synopsis


A series of co-impregnated (pH 1) P-Ni-W/AI20 3 catalysts of low tungsten content (1.6 W atoms/nm 2) and varying phosphorus concentration (0-5.9 wt.-% P205) have been studied in the reaction of hydrogenation of naphthalene in a batch Parr reactor at 573 K and P = 44 atm. In addition to a previous characterization by XRD, DRS and XPS, the catalysts have been characterized here by DRS, FTIR spectroscopy in their oxide state and by FFIR spectroscopy of NO chemisorbed on the sulphided catalysts. A promoting effect of phosphorus is observed in all phosphorus containing samples. The catalytic activity vs. phosphorus content curve has a complex behavior passing through a maximum and a minimum. Phase transitions are observed in the samples with the change of the phosphorus content. The form of the catalytic activity curve is discussed in the light of these phase transitions and the structure and properties of the different phases. The highest catalytic activity is observed for the sample with 0.6% P205. This sample is also characterized by the highest amount of chemisorbed NO and by a local maximum in the relative number of terminal W=O bonds. When strong overlapping of the bands is observed, the NO adsorption technique should be applied with care. Also, NO might adsorb on sites which are not active in the corresponding hydrotreatment reaction and the trend predicted by the total amount of chemisorbed NO should not necessarily coincide with the form of the catalytic activity


📜 SIMILAR VOLUMES


The intraparticle deactivation of NiSiO
✍ S. Zrnc̆ević 📂 Article 📅 1984 🏛 Elsevier Science 🌐 English ⚖ 403 KB

A-act-The deactivation of the commercial NCSiO,-A&O, catalyst was studied in an isothermal differential flow reactor using the hydrogenation of benzene to cyclohexane as a model reaction. Reaction system behaviour in both the presence and absence of diffusional limits is studied at temperatures rang