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

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PP-IV-18contains phases <strong>of</strong> NiO and MgO with lattice parameter 4.218 Å. It was found that during <strong>the</strong>formation <strong>of</strong> MgO <strong>the</strong> introduction <strong>of</strong> Ni 2+ -cations from oxide layer to support MgO takesplace. In supports I and II, nickel is detected by EDX spectra <strong>of</strong> MgO as spectral lines <strong>of</strong>weak intensity corresponding to a nickel concentration <strong>of</strong> ∼ 2 at.%. In reaction conditions orreduction conditions <strong>the</strong>se Ni 2+ -cations form dispersal nickel crystals.The reduced supported catalysts exhibit phases <strong>of</strong> nickel and solid solution NiO in MgOwhich disappeared in reaction condition. In <strong>the</strong> supported nickel catalysts, dispersal nickelparticles are epitaxially bonded with support MgO, which is evidenced by <strong>the</strong> Moire picture.The conversion value for support MgO I is 52 % and for MgO II - 65 %. The additionaldeposition <strong>of</strong> nickel results in <strong>the</strong> increasing <strong>of</strong> conversion value. Note that <strong>the</strong> preparednickel catalysts on supports I and II are characterized by comparable conversion values.9590Conversion CH 4,%8580757065605512345500 5 10 15 20 25 30 35 40 45 50 55 60t, hFig. Influence <strong>of</strong> reaction time on methane conversion in steam reforming reaction: 1 – 5.0 % Ni/pNi + 5.0 %MgO (I) (plate, V=0.7 сm 3 , m=3.29 g); 2 – 5,7 % Ni/pNi + 5.0 % MgO (II) (plate, V=0.7 сm 3 , m=3.28 g);3 – 7,2% Ni/pNi + 5,0% MgOII (plate, m=3.07g, V=0.7 сm 3 ); 4 – NIAP-18 (fraction 0,25–0,5 mm, m=0,80g);5 – NIAP-18 (1/2 <strong>of</strong> grain, m=1,46 g, V=0,7 сm 3 ).The catalyst activity was stable during 50 hour tests (Fig.). From TEM it was shown that<strong>the</strong>re are not any carbon deposits in <strong>the</strong> tested catalyst samples. We suppose that formed fromsolid solution NiO-MgO or from surface combination dispersal nickel crystals are interactedwith support and so <strong>the</strong>y have increased stability to carbon deposition. The fact <strong>of</strong> interactionbetween nickel and support is confirmed by TEM HR data which do not show oxide layer indispersal nickel particles (∼20 Å) after additional calcinations (Ar, 550 °C, 2 h).Thus, <strong>the</strong> nickel catalysts supported on <strong>the</strong> plate-like porous nickel with <strong>the</strong> MgO precoatare characterized by high and stable activity in <strong>the</strong> reaction <strong>of</strong> methane steam reforming andresistance to carbonization.References1. Kirillov V.A., Kuzin N.A., Kulikov A.V. et al. // Theor.Bases Chem.Techn. 2003, v. 37, No 3, p.300.2. Y.H. Hu, E. Ruckenstein // Catal. Lett., 36 (1996) 145.3. G.C. Bond, S.P. Sarsam // Appl. Catal.A:, General 38 (1988) 365.429

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