(231c) Promoted Zno Sorbents for Low Temperature H2S Removal: Influence of Temperature, Support Surface Area, Pore Volume and Pore Size
AIChE Spring Meeting and Global Congress on Process Safety
2008
2008 Spring Meeting & 4th Global Congress on Process Safety
AIChE / ACS Jointly Co-sponsored Sessions
Gas Conversion and Separation Technologies
Thursday, April 10, 2008 - 9:20am to 9:45am
Promoted ZnO sorbents with formulation Zn0.95M0.05O (M = Mn, Fe, Co, Ni, Cu) were supported on silica gels, MCM-41 and MCM-48. H2S adsorption was conducted from room temperature to 400 oC in flowing 1 vol.% H2S/H2 at various levels of relative humidity. Cu-doped ZnO (15wt %)/MCM-41 provided the highest sulfur capacity at room temperature [0.90 mmol S/mmol (Zn+Cu)O]. At low temperatures, the utilization of the reactant (Zn+M) towards H2S removal depended on the support employed in the order MCM-41 > MCM-48 > silica gels. This dependence was investigated in terms of the support: surface area, pore volume, and pore size; using N2 adsorption-desorption isotherms. At equivalent levels of support surface area and pore size, higher pore volumes provided greater low temperature H2S capacities presumably due to diminution in Zn0.95M0.05O crystallite size resulting from the lower Zn (NO3)2.6H2O concentrations used during impregnation. Estimates of crystallite size were assessed from XRD line broadening (where feasible) as well as pulse oxygen chemisorption. The sulfided sorbents were tested for their regeneration and repeated use in multiple adsorption-desorption cycles.
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