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

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PP-IV-26MCM-41-SUPPORTED PdNi CATALYSTS FOR DRY REFORMINGOF METHANEK. Arishtirova 1 , C. Sener 2 , B. Pawelec 3 , T. Dogu 2 , G. Dogu 4 , J.L.G. Fierro 3 ,S. Damyanova 11<strong>Institute</strong> <strong>of</strong> <strong>Catalysis</strong>, Bulgarian Academy <strong>of</strong> Sciences, 1113 S<strong>of</strong>ia, Bulgaria2 Department <strong>of</strong> Chemical Engineering, METU, 06531 Ankara, Turkey3 Instituto de Catalisis y Petroleoquimica, CSIC, Cantoblanco, Madrid, Spain4 Department <strong>of</strong> Chemical Engineering, Gazi University, 06531 Ankara, TurkeyThe reforming <strong>of</strong> methane with carbon dioxide (dry reforming) <strong>of</strong>fers an alternative wayto produce hydrogen, efficient and low cost energy fuel. This reaction has received muchinterest from environmental point <strong>of</strong> view because <strong>of</strong> <strong>the</strong> possibility to reduce CO 2 andmethane emissions as both gases are contributors to <strong>the</strong> greenhouse effect. Nickel-basedcatalysts have been proved to be <strong>the</strong> most suitable catalysts due to <strong>the</strong>ir high activity, lowprice and inherent availability. The addition <strong>of</strong> small amount <strong>of</strong> noble metal prevents <strong>the</strong>ir fastdeactivation caused by coke deposition on <strong>the</strong> active nickel phase [1]. The aim <strong>of</strong> <strong>the</strong> work isto investigate <strong>the</strong> effect <strong>of</strong> <strong>the</strong> Ni/noble metal ratio on <strong>the</strong> surface and catalytic properties <strong>of</strong>PdNi/MCM-41 catalysts in <strong>the</strong> reaction <strong>of</strong> dry methane reforming.MCM-41 obtained by hydro<strong>the</strong>rmal syn<strong>the</strong>sis was used as carrier for catalysts.Monometallic Ni/MCM-41 and bimetallic PdNi/MCM-41 with Ni/Si ratio <strong>of</strong> 0.2, 0.3 and 0.4were obtained by impregnation technique. Pd content was about 0.6 wt%. The samples werecharacterized by N 2 iso<strong>the</strong>rms, XRD, TPR, XPS and catalytic test.The introduction <strong>of</strong> Pd into monometallic Ni catalyst leads to increase in <strong>the</strong> conversions<strong>of</strong> CH 4 and CO 2 (Table 1). The activity <strong>of</strong> <strong>the</strong> bimetallic PdNi catalysts depends <strong>of</strong> <strong>the</strong> nickelcontent. Maximum conversions <strong>of</strong> CH 4 and CO 2 are obtained for sample with ratio Ni/Si=0.3.The H 2 /CO ratio is lower than 1, which is an indication <strong>of</strong> <strong>the</strong> occurrence <strong>of</strong> reverse water gasshift reaction. The addition <strong>of</strong> Pd into Ni/MCM-41 changes <strong>the</strong> catalytic behavior <strong>of</strong> <strong>the</strong>catalysts with time-on-stream. Bimetallic PdNi catalysts are more stable than monometallicNi catalyst..XRD analysis showed that <strong>the</strong> structure <strong>of</strong> MCM-41 was retained in all supportedcatalysts. The addition <strong>of</strong> Pd into Ni containing catalyst provokes a decrease <strong>of</strong> <strong>the</strong> NiO sizeand S BET surface area compared to that <strong>of</strong> Pd-free Ni sample. PdNi catalyst with Ni/Si ratio <strong>of</strong>0.3 possesses <strong>the</strong> smallest nanosized NiO particles (Table 1).442

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