Abstract
A model describing the gasification of a spent shale particle in an atmosphere of steam, hydrogen, carbon monoxide and methane is developed. Both diffusion and reaction rate terms are included. Simulations on spent Australian oil shale show that the external mass transfer coefficient has no effect on the overall gasification rate. Increasing the temperature above 1500 K does not increase the gasification rate significantly. No methane was produced under the conditions of the study. The simulations show that neither the homogeneous reaction model nor the shrinking-core model applies for the expected range of operating conditions. Effects of temperature, pressure, particle size and the ratio of carbon dioxide to steam on the conversion and yield are discussed in this paper.
Talk to us
Join us for a 30 min session where you can share your feedback and ask us any queries you have
Schedule a callDisclaimer: All third-party content on this website/platform is and will remain the property of their respective owners and is provided on "as is" basis without any warranties, express or implied. Use of third-party content does not indicate any affiliation, sponsorship with or endorsement by them. Any references to third-party content is to identify the corresponding services and shall be considered fair use under The CopyrightLaw.
