Hydrogenolytic cleavage of pyridine on different cobalt-molybdenum and nickel-tungsten catalysts

1981 ◽  
Vol 46 (6) ◽  
pp. 1348-1354 ◽  
Author(s):  
Mirko Černý ◽  
Miloš Kraus

Composition of the reaction products formed by hydrogenation of pyridine at 300 °C and 15 MPa in the presence of 15 sulphided and unsulphided molybdenum and tungsten catalysts promoted by cobalt and by nickel, respectively, using alumina as the support in most cases, has been examined. It has been proved that the catalyst composition affects both its hydrogenation activity and the ratio of transalkylation to cracking (or hydrocracking) reactions. Relations between the catalyst composition and its activity and selectivity found for the reaction of pyridine differ from those reported for hydrogenolytic cleavage of thiophene, hydrogenation and isomerization of cyclohexene.

1977 ◽  
Vol 50 (1) ◽  
pp. 79-82 ◽  
Author(s):  
Shoko Yamadaya ◽  
Masaaki Oba ◽  
Yasuo Miki

1983 ◽  
Vol 48 (6) ◽  
pp. 1703-1709 ◽  
Author(s):  
Rafael López ◽  
Miloš Kraus

A series of nickel or cobalt promoted molybdenum catalysts and one nickel-tungsten catalyst have been studied by oxygen chemisorption on reduced oxidic samples, by activities of oxidic and sulphided samples for 1-hexene hydrogenation and by activities of sulphided samples for benzothiophen and pyridine hydrogenolyses. A good correlation was obtained between oxygen chemisorption and hydrogenation activity on oxidic, partially reduced, forms of the catalysts, and a limited correlation for activities of sulphided forms. Parallel activities for hydrogenation and hydrogenolyses were observed.


2014 ◽  
Vol 16 (7) ◽  
pp. 3580-3588 ◽  
Author(s):  
Katarína Fabičovicová ◽  
Oliver Malter ◽  
Martin Lucas ◽  
Peter Claus

Molecules ◽  
2021 ◽  
Vol 26 (13) ◽  
pp. 3782
Author(s):  
Alevtina N. Gosteva ◽  
Mayya V. Kulikova ◽  
Yulya P. Semushina ◽  
Mariya V. Chudakova ◽  
Nikita S. Tsvetov ◽  
...  

Currently, the processes of obtaining synthetic liquid hydrocarbons and oxygenates are very relevant. Fischer-Tropsch synthesis (FTS) is the most important step in these processes. The products of thermal destruction in argon of the mixture [Co(NH3)6][Fe(CN)6] and Al(OH)3 were used as catalysts for CO hydrogenation. The resulting compositions were studied using powder X-ray diffraction, IR spectroscopy, elemental analysis, SEM micrographs. The specific surface area, pore and particle size distributions were determined. It was determined that the DCS-based catalysts were active in the high-temperature Fischer-Tropsch synthesis. The effect of aluminum in the catalyst composition on the distribution of reaction products was revealed.


1994 ◽  
Vol 37 (6) ◽  
pp. 594-602 ◽  
Author(s):  
Nobuyuki MATSUBAYASHI ◽  
Masaaki TAMAYAMA ◽  
Hiromichi SHIMADA ◽  
Toshio SATO ◽  
Yuji YOSHIMURA ◽  
...  

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