Year: 1979
Type: article
Abstract: A two-phase fluidized-bed model can be used to predict the conversion observed in the char-steam gasification reaction in a 5.08-cm fluidized-bed reactor. The best fit of the experimental data was obtained using the K and L model to calculate the mass exchange between the bubble and particulate phases.
Language: English
Subfield: Fuel Technology
Field: Energy
Domain: Physical Sciences
Open Access status: green
OpenAlex ID: W205488812
