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

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PP-IV-34PHOTOCATALYTIC WATER SPLITTING WITH HYDROGENEVOLUTION IN Ce 3+ /Ce 4+ SYSTEMSEkaterina Kozlova a,b , Aleksander Vorontsov a,b , Tatayna Korobkina a,ba <strong>Boreskov</strong> <strong>Institute</strong> <strong>of</strong> <strong>Catalysis</strong> SB RAS, Novosibirsk, 630090, Novosibirsk, Russia,tel/fax: +7-383-333-16-17, e-mail: kozlova@catalysis.nsk.sub Novosibirsk State University , Novosibirsk, 630090, RussiaHydrogen as environmental friendly and high-energy fuel has attracted attention all over<strong>the</strong> world for <strong>the</strong> last decade. Photocatalytic emission <strong>of</strong> hydrogen from water solution <strong>of</strong>organic compounds is a very promising and interesting method <strong>of</strong> hydrogen obtaining.Quantum efficiency <strong>of</strong> hydrogen emission per one electron can exceed 10% overphotocatalyst platinized titania. Unfortunately we can produce only mixture <strong>of</strong> hydrogen andcarbon dioxide using organic donors. It is more pr<strong>of</strong>itable for pure hydrogen production to useinorganic donors, for example Ce 3+ ions. The use <strong>of</strong> <strong>the</strong> two-step photocatalytic andphotochemical splitting <strong>of</strong> water to oxygen and hydrogen using semiconducting metal oxidesand system Ce 3+ /Ce 4+ is considered imperative because <strong>of</strong> its promising application in solarenergy conversion systems [1]. In our work, we used solution <strong>of</strong> Ce 2 (SO 4 ) 3 for hydrogenproduction and solution <strong>of</strong> Ce(SO 4 ) 2 for photocatalytic oxygen production. Bare andplatinized titania was used as a photocatalyst.Photocatalytic hydrogen and oxygen emission from Ce 2 (SO 4 ) 3 and Ce(SO 4 ) 2 solution wascarried out by <strong>the</strong> following method. Water suspension with catalyst and <strong>the</strong> initial compoundwas placed in a sealed <strong>the</strong>rmostated reactor under argon atmosphere and illuminated by a1000-W high-pressure mercury lamp under continuous stirring. The concentration <strong>of</strong>Ce 2 (SO 4 ) 3 or Ce(SO 4 ) 2 was varied from 1 to 2 mM, catalyst concentration was 0.75 g/L,temperature 20 °C. Concentration <strong>of</strong> hydrogen and oxygen was measured by means <strong>of</strong> a gaschromatograph LChM-8, that <strong>of</strong> Ce 3+ and Ce 4+ by means <strong>of</strong> Lambda 35 Perkin-ElmerUV/Vis-spectrometer. Bare and platinized commercial TiO 2 Degussa P25 and Hombifine N,and self-syn<strong>the</strong>sized rutile were used as catalysts. Ruthile was syn<strong>the</strong>sized by Degussa P25calcination at 950 °C (R1) and by hydrolysis <strong>of</strong> titanium tetraisopropoxide (TTIP) in 1M HClsolution with calcination at 350 °C (R2). Noble metals were deposited by s<strong>of</strong>t chemicalreduction (SCR) and photodeposition (PD) techniques.We have carried out experiments for oxygen production from water solution <strong>of</strong> Ce(SO 4 ) 2 .Fig. 1 shows <strong>the</strong> initial rate <strong>of</strong> oxygen production for six catalysts.455

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