scholarly journals Functionalization strategy influences the porosity of amino-containing porous aromatic frameworks and the hydrogenation activity of palladium catalysts synthesized on their basis

2021 ◽  
pp. 112012
Author(s):  
Daria Makeeva ◽  
Leonid Kulikov ◽  
Anna Zolotukhina ◽  
Anton Maximov ◽  
Edward Karakhanov
2007 ◽  
Vol 324 ◽  
pp. 52-61 ◽  
Author(s):  
Lucky M. Sikhwivhilu ◽  
Neil J. Coville ◽  
Dhachapally Naresh ◽  
Komandur V.R. Chary ◽  
Venkataraman Vishwanathan

Catalysts ◽  
2020 ◽  
Vol 10 (10) ◽  
pp. 1106
Author(s):  
Leonid Kulikov ◽  
Maria Kalinina ◽  
Daria Makeeva ◽  
Anton Maximov ◽  
Yulia Kardasheva ◽  
...  

The current work describes an attempt to synthesize hybrid materials combining porous aromatic frameworks (PAFs) and dendrimers and use them to obtain novel highly active and selective palladium catalysts. PAFs are carbon porous materials with rigid aromatic structure and high stability, and the dendrimers are macromolecules which can effectively stabilize metal nanoparticles and tune their activity in catalytic reactions. Two porous aromatic frameworks, PAF-20 and PAF-30, are modified step-by-step with diethanolamine and hydroxyl groups at the ends of which are replaced by new diethanolamine molecules. Then, palladium nanoparticles are applied to the synthesized materials. Properties of the obtained materials and catalysts are investigated using X-ray photoelectron spectroscopy, transmission electron microscopy, solid state nuclear magnetic resonance spectroscopy, low temperature N2 adsorption and elemental analysis. The resulting catalysts are successfully applied as an efficient and recyclable catalyst for selective hydrogenation of alkynes to alkenes at very high (up to 90,000) substrate/Pd ratios.


1997 ◽  
Vol 15 (3) ◽  
pp. 165-172 ◽  
Author(s):  
Nagendranath Mahata ◽  
V. Vishwanathan

A series of catalysts containing 1 wt.% Pd supported on various oxides of commercial origin have been characterised by hydrogen adsorption at 298 K and evaluated for vapour-phase phenol hydrogenation at 473 K employing an H/phenol ratio of 5.4 at atmospheric pressure. The activity of phenol hydrogenation showed a dependence on the irreversible uptake of hydrogen. Among the catalysts studied, Pd/Al2O3 showed a decrease in activity with increasing temperature while Pd/MgO passed through a maximum at 503 K. The Pd/MgO catalysts exhibited a higher dispersion of smaller Pd crystallites leading to higher activity and total selectivity for cyclohexanone. The higher resistance towards deactivation and better stability of the Pd/MgO catalysts suggest that the acidic sites of alumina may be responsible for deactivation, thereby accounting for the lowering of activity with Pd/Al2O3 catalysts.


1980 ◽  
Vol 45 (1) ◽  
pp. 222-230 ◽  
Author(s):  
Libor Červený ◽  
Antonín Marhoul ◽  
Karel Červinka ◽  
Vlastimil Růžička

The decomposition of cupric formate induced by palladium catalysts has been studied in aqueous solution. Effects of the carrier and the proper active component on the cupric formate concentration decrease have been separated. Kinetic data of the decomposition reaction have been obtained, and processes affecting the decomposition have been followed. The decomposition rates found with the use of various catalysts enabled to test the effects of preparation methods of palladium catalysts on their activity. The values found agree with hydrogenation activity of the 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.


1987 ◽  
Vol 52 (8) ◽  
pp. 2019-2027 ◽  
Author(s):  
Libor Červený ◽  
Nguyen Thi Du ◽  
Ivo Paseka

Palladium catalysts have been used to study the hydrogenation of 1-phenyl-2-butene-1-ol which is accompanied by several side reactions considered to be acid-catalysed. Another model reaction studied was dehydration and subsequent hydrogenation or hydrogenolysis of 1-phenyl-1,3-propanediol to 3-phenyl-1-propanol, accompanied by formation of propylbenzene. The dehydration and propylbenzene formation can be again classified as acid-catalysed reactions. Another one is methanolysis of styrene oxide taking place under conditions of liquid phase hydrogenation due to the acid properties of Pd-H systems. Hydrogenation activity of Pd catalysts was tested by hydrogenation of cyclohexene. Sixteen Pd catalysts on different supports and with different content of active component were used, their activity and selectivity was determined and the effect of variable parameters in the synthesis of these catalysts on the activity and selectivity is discussed.


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