作者: M.M. Yazdanpanah , A. Forret , T. Gauthier , A. Delebarre
DOI: 10.1016/J.APENERGY.2013.06.054
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摘要: Abstract This paper presents a reactor model for combustion of CH4 with NiO/NiAl2O4 oxygen carriers in the Fuel Reactor Chemical Looping Combustion (CLC) process. The hydrodynamics is based on two phase bubble - emulsion concept bubbling fluidized beds, validated by residence time distribution tests conducted 10 kWth equivalent cold flow prototype. kinetics literature and adjusted experimental results from CLC pilot plant. Results show necessity including both non-direct catalytic non-catalytic direct reaction gases carriers. shows good agreement if some kinetic hydrodynamic modifications are considered, impact gas adsorption falling particles exchange coefficient thermodynamic limitation CO H2 combustion.