Promotional Effect of Copper on Activity and Selectivity to

Mar 28, 2011 - and a syngas with a H2/CO molar feed ratio of 0.9 in a temperature range of 260А290 °C. The addition of up to 2.0 wt % Cu promoter en...
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Promotional Effect of Copper on Activity and Selectivity to Hydrocarbons and Oxygenates for FischerTropsch Synthesis over Potassium-Promoted Iron Catalysts Supported on Activated Carbon Wenping Ma, Edwin L. Kugler, and Dady B. Dadyburjor* Department of Chemical Engineering, West Virginia University, Morgantown, West Virginia 26506, United States ABSTRACT: The effect of 02 wt % copper on the activity and selectivity to hydrocarbons and oxygenates was studied over activated-carbon (AC)-supported 15.7 wt % Fe and 0.9 wt % K catalysts for the FischerTropsch synthesis (FTS). The catalysts were examined in a fixed-bed reactor at 300 psig, 3 nL (g of catalyst)1 h1, and a syngas with a H2/CO molar feed ratio of 0.9 in a temperature range of 260290 °C. The addition of up to 2.0 wt % Cu promoter enhances iron reduction significantly. However, the improved iron reduction does not benefit the catalyst activity. Instead, both FTS and watergas shift (WGS) activities of the FeK/ AC catalyst are lowered. This may be due to high Cu loadings, suppressing iron carbonization and increasing the deposition of carbon on the catalyst surface during the initial iron carbonization and/or the formation of some FeCu clusters during reduction. The addition of Cu on the FeK/AC catalysts changes selectivities to methane and other hydrocarbons only slightly; however, it increases the internal olefin content and decreases the olefin content. This could be attributed to Cu-promoting hydrogen adsorption and enhanced hydrogenation/isomerization. Cu increases oxygenate selectivity of the FeK/AC catalysts, implying that Cu enhances molecular CO adsorption, but inhibits CO dissociation on the FeK/AC catalyst. The addition of Cu also changes the alcohol distribution of the FeK/AC catalysts. The ethanol formation decreases slightly, but the formation of methanol and C3C5 alcohols increases. The highest Cu loading (2 wt %) reduces this trend somewhat. Furthermore, from the kinetic point of view, the addition of 0.82.0 wt % Cu decreases both the apparent activation energies and the apparent pre-exponential factors of the FTS and WGS reactions over the catalysts. The decrease in the pre-exponential factor is related to the lower activities of the Cucontaining FeK/AC catalysts.

1. INTRODUCTION Potassium and copper are structural promoters often used for industrial iron-based FischerTropsch synthesis (FTS) catalysts for the formation of heavy hydrocarbons (HCs) and/or oxygenates from synthesis gas (syngas) via the nominal reaction. nCO þ ðm þ 2n  2pÞ=2H2 f Cn Hm Op þ ðn  pÞH2 O ð1aÞ Extensive studies have been conducted to discover the functions of the promoters in the FTS reaction.110 It is widely accepted that potassium suppresses methane formation and increases the formation rate of heavier HCs through enhanced CO dissociation on iron-based catalysts.13,8 The appropriate amount of potassium, i.e.,