Water-gas shift reaction in a Pd membrane reactor over Pt/Ce)_(0. 6)Zr_(0. 4)O_2 catalyst

摘要

A water-gas shift (WGS) Pt/Ce_(0.6)Zr_(0.4)O_2 catalyst has been prepared, which exhibits much faster kinetics than conventional high-temperature ferrochrome catalysts in the temperature range most suitable for operation of WGS Pd membrane reactors, i.e. above 623 K. The performance of the Pt catalyst was tested in a reactor furnished with a supported, 1.4 μm thick high-flux Pd membrane using feeds obtained by autothermal reforming of natural gas. CO conversion remained above thermodynamic equilibrium up to feed space velocities of 91001 kg~(-1) h~(-1) at 623 K, P_(total) = 1.2 MPa and steam-to-carbon ratio S/C = 3, but H_2 recovery decreased from 84.8% at GHSV = 40501 kg~(-1) h~(-1) to 48.7% at the highest space velocity. This rapid decline of separation performance is attributed to slow H_2 diffusion through the catalyst bed, suggesting that external mass flow resistance has a significant impact on the H_2 permeation rate in such membrane reactors. This could be minimized by the development of WGS catalysts with even faster kinetics which would allow further reduction of the catalyst bed height.