Modeling of biomass gasification in fluidized bed

Coal gasification in CO2 atmosphere and its kinetics since 1948: A brief review

The effect of particle size and size distribution on the behaviour of gas-fluidised beds

Methane steam reforming is the most common industrial process used for almost the 50% of the world’s hydrogen production. Commonly, this reaction is performed in fixed bed reactors and several stages are needed for separating hydrogen with the desired purity. The membrane reactors represent a valid alternative to the fixed bed reactors, by combining the reforming reaction for producing hydrogen and its separation in only one stage. This article deals with the recent progress on methane steam reforming reaction, giving a short overview on catalysts utilization as well as on the fundamentals of membrane reactors, also summarizing the relevant advancements in this field.

Advances on methane steam reforming to produce hydrogen through membrane reactors technology: A review

Gas absorption mechanism in catalytic slurry reactors

Bubble assemblage model for fluidized bed catalytic reactors

Comparison of zone-reaction model and unreacted-core shrinking model in solid—gas reactions—II non-isothermal analysis

Kinetic studies on the reactions involved in the hot gas desulfurization using a regenerable iron oxide sorbent—I

Kinetic studies on the reactions involved in the hot gas desulfurization using a regenerable iron oxide sorbent—II: Reactions of iron sulfide with oxygen and sulfur dioxide

Effectiveness factors and instability in solid-gas reactions

C.Y. Wen

Papers

Bubble assemblage model for fluidized bed catalytic reactors

Comparison of zone-reaction model and unreacted-core shrinking model in solid—gas reactions—II non-isothermal analysis

Kinetic studies on the reactions involved in the hot gas desulfurization using a regenerable iron oxide sorbent—I

Kinetic studies on the reactions involved in the hot gas desulfurization using a regenerable iron oxide sorbent—II: Reactions of iron sulfide with oxygen and sulfur dioxide

Effectiveness factors and instability in solid-gas reactions