Principal of dual fluidized bed gasification process.
4-Evolution of water vapour pressure as a function of time and particle
Schematic diagram of novel helical fluidized bed pyrolysis reactor.
Contour of solid volume fraction at low (left) and high (right) gas
The change of conversion along the reactor.
Liliana OLIVO, PhD, PhD Chemical Engineer, Instituto Politécnico Nacional, Mexico City, IPN, Centro de Investigación en Ciencia Aplicada y Tecnología Avanzada (CICATA)
Combustion reaction rate of the sampled char at different temperatures
a) TGA analysis and (b) DTG analysis of by-product biochar obtained at
Comparison on experimental results (bars) and simulation data (points)
Contours of volume fraction in tapered bed having taper angle of 4.52 º
PDF) Three-dimensional transient numerical simulation of the solid volume fraction of a fluidized bed: the role of three solution orders using a discretization scheme
Design-expert plots: response surface and contour plots for the
XPS spectra of uncoated anatase TiO2 powders: O 1s (a) without and (b)
The magnitude of the transfer function from mass flow rate fluctuations
Physical features and process parameters
