Diffusion-reaction model for a porous catalyst has been widely studies for the past three decades or so. However, intraparticle convection has not been accounted for in the majority of reaction-diffusion studies in porous catalysts till recently. Though it has been reported in some early works that the intraparticle convection plays significant role in enhancing the substrate transport inside the porous solid especially for the case of large pores (Nir and Pismen, 1977; Rodrigues and Orfao, 1984; Stephanopoulos and Tsiveriotis; 1989), but later studies have largely neglected this important effect. The forced intraparticle flow can contribute significantly to the total intraparticle nutrient transport rate in general. This becomes more signi...
We review and generalize a recent theoretical framework that provides a sound physicochemical basis ...
The actual transient characteristics of the effectiveness factor for reactions in porous catalyst pa...
The prior random pore model for kinetically controlled fluid-solid reaction (Bhatia and Perlmutter, ...
Diffusion-reaction problem in a porous solid catalyst is important in the design and analysis of het...
The effect of internal diffusion on the overall reaction rate in a biocatalyst having slab geometry ...
This contribution deals with effectiveness factor (η) and concentration profile of key component est...
Computational fluid dynamics (CFD) modeling plays a pivotal role in optimizing fixed bed catalytic c...
Immobilized biocatalysts have many advantages in large scale processing such as retention of enzyme ...
Most porous media (just like catalyst pellets) have complicated pore structures, and understanding...
This work investigates the transient behavior of a chemically-reacting system inside a porous cataly...
In the present study, mass transport accompanied by chemical reactions in porous media is studied ac...
For fluid-solid reactions a random pore model is developed which accounts for arbitrary pore-size di...
Internal mass transport limitations inside Fischer–Tropsch catalysts due to the slow diffusion of re...
A dynamic mechanistic model of a multi-phase heterogeneous batch reactor processing a non-catalytic ...
The mass balances to a spherical bead with increasing porosity, e (obtained by plain expansion of a...
We review and generalize a recent theoretical framework that provides a sound physicochemical basis ...
The actual transient characteristics of the effectiveness factor for reactions in porous catalyst pa...
The prior random pore model for kinetically controlled fluid-solid reaction (Bhatia and Perlmutter, ...
Diffusion-reaction problem in a porous solid catalyst is important in the design and analysis of het...
The effect of internal diffusion on the overall reaction rate in a biocatalyst having slab geometry ...
This contribution deals with effectiveness factor (η) and concentration profile of key component est...
Computational fluid dynamics (CFD) modeling plays a pivotal role in optimizing fixed bed catalytic c...
Immobilized biocatalysts have many advantages in large scale processing such as retention of enzyme ...
Most porous media (just like catalyst pellets) have complicated pore structures, and understanding...
This work investigates the transient behavior of a chemically-reacting system inside a porous cataly...
In the present study, mass transport accompanied by chemical reactions in porous media is studied ac...
For fluid-solid reactions a random pore model is developed which accounts for arbitrary pore-size di...
Internal mass transport limitations inside Fischer–Tropsch catalysts due to the slow diffusion of re...
A dynamic mechanistic model of a multi-phase heterogeneous batch reactor processing a non-catalytic ...
The mass balances to a spherical bead with increasing porosity, e (obtained by plain expansion of a...
We review and generalize a recent theoretical framework that provides a sound physicochemical basis ...
The actual transient characteristics of the effectiveness factor for reactions in porous catalyst pa...
The prior random pore model for kinetically controlled fluid-solid reaction (Bhatia and Perlmutter, ...