Skip to main content
U.S. Department of Energy
Office of Scientific and Technical Information

Hydrogenation of carbon monoxide over Raney iron-manganese catalysts

Thesis/Dissertation ·
OSTI ID:7066066

The Raney Fe and Raney Fe-Mn catalysts were prepared by leaching the aluminum from Al-Fe (50/50 wt%) and Al-Fe-Mn (59/38/3 wt%) alloys with an aqueous solution of sodium hydroxide (2 to 20 wt%) in the temperature range of 298 to 363 K by two different leaching modes, caustic or alloy addition. The major phase in all the Raney Fe and Raney Fe-Mn catalysts was found to be ..cap alpha..-Fe from X-ray diffraction study. The BET surface area of the Raney Fe catalyst ranged from 26 to 54 m/sup 2//g, while it ranged from 64 to 116 m/sup 2//g for Raney Fe-Mn catalysts depending on the preparation conditions. The crystallite size of the ..cap alpha..-Fe in the Raney catalysts, estimated by X-ray line broadening, ranged from 70 to 250 Angstrom and it increased with increasing leaching temperature. The optimum reduction temperature was found to be 648 K for the Raney catalysts (Fe and Fe-Mn) and 673 K for the precipitated catalysts (Fe and Fe-Mn) from thermogravimetric analyses. The Raney and precipitated catalysts, reduced in-situ in flowing hydrogen, were evaluated for the hydrogenation of carbon monoxide in a high-pressure fixed-bed reactor at the following standard reaction conditions: pressure = 1465 KPa, space velocity = 3.0 cm/sup 3/g/sup -1/s/sup -1/, H/sub 2//CO = 2.0, and reaction temperature of 423 to 473 K. The Raney Fe and Raney Fe-Mn catalysts were 2 to 4 times more active in terms of carbon monoxide conversion than the corresponding precipitated Fe and Fe-Mn catalysts, respectively, at the standard reaction conditions. The activation energy ranged from 96 to 139 KJ/mol depending on different catalysts.

OSTI ID:
7066066
Country of Publication:
United States
Language:
English