Insights in steam reforming of glycerol in a fluidized bed by CFD modeling
In this study, computational fluid dynamics (CFD) is used to investigate the performance of glycerol steam reforming in a fluidized bed system.
Modelling of methane dry reforming over Ni/Al2O3 catalyst in a fixed-bed catalytic reactor
The dry reforming of CH4 in a fixed-bed catalytic reactor for the production of hydrogen at different temperatures over supported Ni catalyst is studied in this paper.
Three Dimensional Kinetic Modeling of Fluidized Bed Biomass Gasification
In this study by Loha, Chattopadhyay, and Chatterjee, simulated gas compositions are found to be in good agreement with experimental data for a bubbling fluidized bed biomass gasifier.
Determination of intrinsic rate constants of the CaO–CO2 reaction
The rate constant of the CaO–CO2 reaction was studied for two sorbents using an atmospheric thermogravimetric analyzer (ATGA) and a pressurized thermogravimetric analyzer (PTGA). A grain model was used to determine the rate-controlling steps.
Sorption-Enhanced Reaction Process With Reactive Regeneration
A mathematical model taking into account multicomponent (six species) mass balances, overall mass balance, Ergun relation for the pressure drop, energy balance for the bed-volume element including the heat transfer to the column wall, and nonlinear adsorption equilibrium isotherm coupled with three main reactions was derived to model SESMR.
Methane steam reforming, methanation and water-gas shift: I. Intrinsic kinetics
In this paper, intrinsic rate equations were derived for the steam reforming of methane, accompanied by water-gas shift on a Ni/MgAl2O4 catalyst. A large number of detailed reaction mechanisms were considered