Pressurised chemical-looping combustion of an iron-based oxygen carrier: Reduction kinetic measurements and modelling

• Published in: Fuel processing technology Vol. 171; pp. 205 - 214
• Main Authors: Zhang, Z., Yao, J.G., Boot-Handford, M.E., Fennell, P.S.
• Format: Journal Article
• Language: English
• Published: Amsterdam Elsevier B.V 01.03.2018; Elsevier Science Ltd
• Subjects: Aluminum oxide; Atmospheric models; Atmospheric pressure; Carbon dioxide; Carbon sequestration; Chemical-looping combustion; Combined cycle engines; Computer simulation; Feasibility studies; Fluidised bed; Fluidized bed combustion; Fluidized bed reactors; Gasification; Hematite; Intrinsic kinetic model; Iron oxides; Nuclear fuels; Oxygen; Pressure effects; Pressurised; Random pore model; Rate constants; Reaction kinetics; Reaction mechanisms; Solid fuels; Intrinsic kinetic model; Chemical-looping combustion; Fluidised bed; Pressurised
• ISSN: 0378-3820; 1873-7188
• DOI: 10.1016/j.fuproc.2017.11.018

Chemical-looping combustion (CLC) is a novel combustion techology offering the potential to provide uninterrupted and reliable heat and power production from fossil or bio-derived fuels with integrated, intrinsic CO2 capture and minimal energy penalty. Operation of CLC at elevated pressures provides the potential for integration with a combined cycle, which makes the use of solid fuels significantly more feasible. To date, only a few experimental studies investigating CLC processes and oxygen carrier performance under pressurised conditions have been reported in the open literature. This article reports findings from investigations into the effect of pressure, temperature and CO concentration on the intrinsic reaction kinetics of an Al2O3-supported Fe-based oxygen carrier. Our study employed an innovative pressurised fluidised-bed reactor, designed for operation at temperatures up to 1273K and pressures up to 20bara, to simulate ex-situ gasification of solid fuels at elevated pressures. An intrinsic reaction model was developed and pseudo-intrinsic rate constants were derived. Differences in the activation energies and pre-exponential factors of the Al2O3-supported Fe2O3 and a pure Fe2O3 oxygen carriers were observed, indicating a change in reaction mechanism when Al2O3 was present. Subsequently, an adapted random pore model was developed to describe the variation of reaction rate with solid conversion. The good agreement between the adapted random pore model and empirical measurements indicated that the change in mechanism was due to a significantly higher product layer diffusivity for the Al2O3-supported Fe2O3 oxygen carrier compared with the pure Fe2O3 material. When pressurised, the observed reaction order with respect to CO was slightly lower than 1. The model developed using atmospheric pressure measurements was successfully applied to predict reaction kinetics at elevated pressures up to 5bara providing further validation of the model. •Reduction kinetics of Fe-based oxygen carriers with CO at pressures up to 5 bara were measured in a fluidised bed reactor.•A change in reduction mechanism was observed for the alumina supported oxygen carrier compared with pure Fe2O3 material.•The change in mechanism was attributed to a significantly improved product layer diffusivity when alumina was present.•An adapted random pore model was developed to describe the variation in reduction rate with Fe2O3 conversion.•The adapted random pore model was successful deployed to predict the reduction kinetics at elevated pressure up to 5 bara.