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Boreskov Institute of Catalysis of the Siberian Branch of Russian ...

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PP-IV-34W 0, μmol O 2/min0,25 1. 1%Pt/Degussa P 25 (SCR)2. pure Degussa P250,203. R20,154. 1% Pt/Hombifine N (SCR)0,105. pure Hombifine N6. R10,050,001 2 3 4 5 6Fig. 1. The initial rate <strong>of</strong> oxygen production over different catalysts.One can see that <strong>the</strong> best catalyst is rutile syn<strong>the</strong>sized by TTIP hydrolysis in hydrochloricacid solution. This catalyst consists <strong>of</strong> rutile, which is <strong>the</strong> best phase <strong>of</strong> TiO 2 forphotocatalytic oxygen production [2], and has quite high surface area (~100 m 2 /g) due to lowtemperature <strong>of</strong> calcination. Pure and platinized Degussa P25, which consists <strong>of</strong> two phases –anatase and rutile – show a very high activity, too. The activity <strong>of</strong> pure rutile R1 is very lowlikely due to <strong>the</strong> very low specific surface area (~5 m 2 /g). Small amount <strong>of</strong> hydrogen wasdetected in <strong>the</strong> case <strong>of</strong> platinized specimens. So rutile (R2) and pure Degussa P25 are <strong>the</strong> bestphotocatalysts for individual oxygen production.Hydrogen can evolve only on platinized titania [3] so only platinized Degussa P25 andHombifine N were used for photocatalytic hydrogen production. The hydrogen emission rateon 1%Pt/P25 (SCR) was 0,01 μmol/min. It exceeds that in <strong>the</strong> case <strong>of</strong> 1%Pt/Hombifinene Nby a factor <strong>of</strong> three. The rate <strong>of</strong> hydrogen evolution for 1%Pt/P25 (PD) is lower than for1%Pt/P25 (SCR) and it is equal to 0,0081 μmol/min, despite many researchers in <strong>the</strong> fieldsuppose that <strong>the</strong> photodeposition (PD) <strong>of</strong> platinum is preferred. Thus, using self syn<strong>the</strong>sizedrutile and platinized commercial Degussa P25 we can produce oxygen and hydrogen fromwater solution <strong>of</strong> ceric and cerious salts, respectively. Combining two photocatalytic reactorsand enter changing <strong>the</strong> reaction solutions <strong>of</strong> Ce 3+ to Ce 4+ we manage to obtain a cycle forphotocatalytic water splitting.AcknowledgementsThe authors want to acknowledge NATO grant SfP-981461 and ISTC grant 3305.References1. G. R. Bamwenda, H. Arakawa, Solar Energy Materials & Solar Cells, 70, 1-14 (2001).2. M. Ni, M. K. H. Leung, D. Y. C. Leung, K. Sumathy, Renewable and Sustainable Energy Reviews, 11, 401-425 (2007).3. S. Sato, Journal <strong>of</strong> Physical Chemistry, 69, 3531-3537 (1981).456

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