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Sulfur Interaction and Regeneration of CaMn(0.775)Ti(0.125)Mg(0.1)O(2.9−δ) Perovskite as Oxygen Carrier during Combustion of Sour Gas in a 500 W(th) Chemical Looping Combustion Unit

[Image: see text] In the present study, the performance of a CaMn(0.775)Ti(0.125)Mg(0.1)O(2.9−δ) perovskite used as an oxygen carrier to burn sour gas with different H(2)S concentrations (up to 3000 vppm) in a continuous 500 W(th) chemical looping combustion (CLC) prototype was investigated. After 2...

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Detalles Bibliográficos
Autores principales: Cabello, A., Abad, A., Mendiara, T., de las Obras Loscertales, M., de Diego, L. F.
Formato: Online Artículo Texto
Lenguaje:English
Publicado: American Chemical Society 2023
Acceso en línea:https://www.ncbi.nlm.nih.gov/pmc/articles/PMC10526641/
https://www.ncbi.nlm.nih.gov/pubmed/37771886
http://dx.doi.org/10.1021/acs.energyfuels.3c02391
Descripción
Sumario:[Image: see text] In the present study, the performance of a CaMn(0.775)Ti(0.125)Mg(0.1)O(2.9−δ) perovskite used as an oxygen carrier to burn sour gas with different H(2)S concentrations (up to 3000 vppm) in a continuous 500 W(th) chemical looping combustion (CLC) prototype was investigated. After 29 h of sour gas combustion, the combustion efficiency had dropped by 18% in comparison with the reference test without sulfur addition. The characterization of the used particles of the perovskite confirmed that the presence of sulfur in the fuel gas had a poisonous effect through the formation of undesired compounds, such as CaSO(4). The reactivity with CH(4) and oxygen uncoupling capacity decreased, which could explain the decrease in the combustion efficiency. Two regeneration processes, one at high temperature (1273 K) and another one at low temperature (773–873 K), were carried out in a batch fluidized bed reactor to remove the amount of sulfur accumulated in the oxygen carrier particles. The detection of appreciable amounts of gaseous sulfur-based compounds (SO(2) and H(2)S) during the experimentation and the postcharacterization results obtained through different techniques such as X-ray diffraction, ultimate analysis, and thermogravimetric analysis confirmed the effectiveness of both processes. Finally, the feasibility of implementation of the regeneration processes in a commercial CLC unit was thoroughly analyzed.