Laboratory- and bench-scale studies of a sweet water–gas-shift catalyst for H₂ and CO₂ production in pre-combustion CO₂ capture

Sánchez, J.M.; Maroño, M.; Cillero, D.; Montenegro, L.; Ruiz, E.

Laboratory- and bench-scale studies of a sweet water–gas-shift catalyst for H₂ and CO₂ production in pre-combustion CO₂ capture

2013

Sánchez, J.M. | Maroño, M. | Cillero, D. | Montenegro, L. | Ruiz, E.

In the first section of this paper, the activity of an iron–chromium-based catalyst for the water–gas-shift reaction is studied at laboratory scale. The influence on the activity of the sweet shift catalyst of the main operating parameters-temperature, space velocity, excess steam, pressure, and gas composition-is evaluated. Base case gas composition M1 was set according to that of the IGCC Power Plant of Puertollano, Spain (ELCOGAS): N₂ 13.4vol%, CO 60.7vol%, H₂ 22.3vol%, and CO₂ 3.6vol%. The effect of gas hourly space velocity GHSV (2000–5000h⁻¹), steam to CO ratio R, (1–3molmol⁻¹), pressure P (0.1–2MPa), and temperature (523–653K) has been determined. In order to study the effect of gas composition on the activity of the WGS catalyst, the following gas mixtures have been evaluated: M2 (CO 60.7vol%, H₂ 22.3vol%, and CO₂ 17vol%); M3 (CO 60vol%, N₂ 40vol%); and M4 (CO 60vol%, and CO₂ 40vol%). The second part of this paper deals with subsequent WGS testing at bench-scale level, based on the results obtained at laboratory scale. Tests were performed using a gas composition according to that of ELCOGAS IGCC plant. The operating temperature was 583K, pressure was set at 1MPa, and gas space velocity was 4715h⁻¹. The effect of steam to CO ratio was evaluated.

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