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II International Symposium on Carbon for Catalysis ABSTRACTS

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PP-<str<strong>on</strong>g>II</str<strong>on</strong>g>-21<br />

THE USE OF ACTIVATED CARBON AS THE SUPPORT OF BIMETALLIC<br />

CATALYSTS USED IN CO OXIDATION AND CO HYDROGENATION<br />

Özkara S., Çağlayan B.S., Avcı B.K., Z. Önsan Z.I., Aksoylu A.E.<br />

Department of Chemical Engineering, Boğaziçi University,34342 Bebek, Istanbul, Turkey<br />

e-mail: aksoylu@boun.edu.tr<br />

Activated carb<strong>on</strong> (AC) is a high surface area support with a very unique property. its<br />

textural and surface chemical properties can be changed by a simple treatment like oxidati<strong>on</strong>;<br />

these changes affect the properties of the resultant catalysts prepared with AC. This paper is<br />

an overview of the studies c<strong>on</strong>ducted in Catalyst Technology and Reacti<strong>on</strong> Engineering Lab<br />

(CATREL) at Boğaziçi University.<br />

Previous studies <strong>on</strong> AC support and AC supported catalysts had clearly shown the effects<br />

of different oxidati<strong>on</strong> treatments <strong>on</strong> both the chemical and physical properties of AC and<br />

catalytic properties of the catalysts [1-3]. The results of CO oxidati<strong>on</strong> and benzene<br />

hydrogenati<strong>on</strong> tests c<strong>on</strong>ducted <strong>on</strong> Pt-Sn/AC had pointed out to the changes in metal<br />

dispersi<strong>on</strong>, the <strong>for</strong>mati<strong>on</strong> of a Pt-rich alloy, Pt 3 Sn, and the resultant high activity in CO<br />

oxidati<strong>on</strong>, all of which stems from the <strong>for</strong>mati<strong>on</strong> of oxygen bearing surface groups, especially<br />

acidic groups, <strong>on</strong> oxidized AC.<br />

The current paper c<strong>on</strong>cerns the use of AC support in the catalysts <strong>for</strong> CO oxidati<strong>on</strong> in<br />

hydrogen rich streams and CO hydrogenati<strong>on</strong>. Bimetallic Pt-Ce and Pt-Sn systems has been<br />

tested <strong>for</strong> CO oxidati<strong>on</strong> as the c<strong>on</strong>tinuati<strong>on</strong> of the previous studies menti<strong>on</strong>ed [1-3]; this time<br />

CO oxidati<strong>on</strong> activity of the AC supported catalysts were tested <strong>for</strong> hydrogen rich streams [4].<br />

Another bimetallic system, Ni-Mo, had been tested in CO hydrogenati<strong>on</strong> previously where<br />

Al 2 O 3 has been used as the support [5-7]. In the current study was used the Ni-Mo system <strong>on</strong><br />

AC supports. The results clearly indicate the beneficial use of AC as the support. Both in CO<br />

oxidati<strong>on</strong> and hydrogenati<strong>on</strong> catalysts, three types of activated carb<strong>on</strong>, namely (i) grinded and<br />

HCl washed activated carb<strong>on</strong> (AC1), (ii) air oxidized <strong>for</strong>m of AC1 (AC2), and (iii) HNO 3<br />

oxidized <strong>for</strong>m of AC1 (AC3), were prepared and used as catalyst supports.<br />

CO oxidati<strong>on</strong> in H 2 -rich streams: The selective oxidati<strong>on</strong> of CO in a H 2 -rich gas stream<br />

was investigated over a series of Pt-Ce and Pt-Sn catalysts supported <strong>on</strong> activated carb<strong>on</strong><br />

(AC). The results have shown that the activities of AC supported catalysts increased with the<br />

increase in reducti<strong>on</strong> temperature. Higher c<strong>on</strong>versi<strong>on</strong> levels were observed <strong>for</strong> 1% CeO x -1%<br />

266

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