National Repository of Grey Literature 4 records found  Search took 0.00 seconds. 
Užití kalcinovaných LDH jako katalyzátorů pro odstranění emisí N2O
Obalová, L. ; Kovanda, F. ; Jirátová, Květa ; Pacultová, K. ; Lacný, Z.
Mixed oxide catalysts were prepared by calcination of LDH containing as divalent ions Ni, Co, Cu and /or Mg and as trivalent ions Mn, Fe and/or Al. The highest conversion was reached over Ni-Al and Co-Mn-Al mixed oxides. N2O conversion decreased slightly with the presence of NO2 over Co-Mn-Al catalyst, but strongly over Ni-Al catalyst. Water vapor inhibited the N2O decomposition over all tested catalysts.
Vliv velikosti krystalitů TiO2 na jeho fotokatalytickou reaktivitu
Kočí, K. ; Obalová, L. ; Matějová, Lenka ; Šolcová, Olga ; Plachá, D. ; Lacný, Z.
The aim of this work is to assess the effect of particle size on photocatalytic reactivity of TiO2 exemplified by the photoreduction of CO2 by water. As the particle size decreased higher methane yields over the TiO2 nanoparticles under the illumination of the light were obtained. Results were compared with yields of mathane over Degussa P25, which in non-porous. We demonstrated that photoreactivity of Degussa P25 was lower than all tested TiO2 nanoparticles.
N2O Decomposition over Promoted Mixed Oxide Catalysts.
Galejová, K. ; Obalová, L. ; Pacultová, K. ; Lacný, Z. ; Kovanda, F. ; Jirátová, Květa
Mixed oxide Co-Mn-Al catalysts were promotes by metals Pd, Pt, La, K and Ce. In simulated proces conditions (in the presence of O2, NO, NO2, H2O) catalytic activity, as well as thein regeneration was studied. The most active catalyst is that one with 3 wt. % K.
Catalytic Methods in Decrease of N2O Emissions: II. Catalysts Based on Hydrotalcites – Results of Investigation.
Pacultová, K. ; Obalová, L. ; Kovanda, F. ; Jirátová, Květa ; Lacný, Z. ; Valášková, M.
Activity of the two- and three component catalysts prepared by calcinations of Ni, Cu, Co, Mn, Mg, Al hydrotalcites in various molar ratios, partly modified with Pt, Pd, La, or K, was studied. Influence of O2, NOx, or H2O present in the reaction mixture on activity and stability of the most active catalyst was also investigated. Based on the laboratory results the size of a hypothetical industrial reactor was calculated.

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