A generalized two-timing technique and finite Sturm-Liouville integral transforms are used to derive theoretical expressions for the time-dependent effectiveness factors of finite-length cylindrical catalyst pellets of various aspect ratios. Parallel and series poisoning processes are considered with both film and pore diffusional resistances acting. For Thiele moduli of unity or less, it is found that infinite-cylinder results can be used with only trivial error but for Thiele moduli greater than 5 the effectiveness factors for pellets of unit aspect ratio, and shorter, differ markedly from their infinite cylinder counterparts
In this paper, a multi-region model based on the unified Maxwell-Stefan diffusion theory is develope...
In the present work the results of the investigations on dead zone formation conditions in catalyst ...
The actual transient characteristics of the effectiveness factor for reactions in porous catalyst pa...
A combination of generalized two-timing with a novel application of finite Sturm-Liouville integral ...
A lumping technique is used to show that the rate equations governing the deactivation of variously ...
The method of matched asymptotic expansions is used to obtain simple analytical expressions for the ...
New efficient analytical expressions for steady-state concentration profile in an isothermal permeab...
Catalyst deactivation in single catalyst pellets and in an isothermal catalytic fixed bed reactor ha...
This contribution undertakes the evaluation of one-dimensional (1D) models to approximate the behavi...
This work investigates the influence of internal diffusional and external mass transfer resistances ...
A one-dimensional model, called generalized cylinder (GC), is employed to analyze the diffusion-reac...
The elimination of concentration profiles in porous catalyst pellets is not straightforward for tran...
This work investigates the effect of the distribution of catalytic activity within a porous pellet o...
Previous modelling of fixed-bed, Fischer-Tropsch (FT) reactors has demonstrated the advantages relat...
A novel one-dimensional (1D) model to account for the diffusion-reaction problem in catalytic pellet...
In this paper, a multi-region model based on the unified Maxwell-Stefan diffusion theory is develope...
In the present work the results of the investigations on dead zone formation conditions in catalyst ...
The actual transient characteristics of the effectiveness factor for reactions in porous catalyst pa...
A combination of generalized two-timing with a novel application of finite Sturm-Liouville integral ...
A lumping technique is used to show that the rate equations governing the deactivation of variously ...
The method of matched asymptotic expansions is used to obtain simple analytical expressions for the ...
New efficient analytical expressions for steady-state concentration profile in an isothermal permeab...
Catalyst deactivation in single catalyst pellets and in an isothermal catalytic fixed bed reactor ha...
This contribution undertakes the evaluation of one-dimensional (1D) models to approximate the behavi...
This work investigates the influence of internal diffusional and external mass transfer resistances ...
A one-dimensional model, called generalized cylinder (GC), is employed to analyze the diffusion-reac...
The elimination of concentration profiles in porous catalyst pellets is not straightforward for tran...
This work investigates the effect of the distribution of catalytic activity within a porous pellet o...
Previous modelling of fixed-bed, Fischer-Tropsch (FT) reactors has demonstrated the advantages relat...
A novel one-dimensional (1D) model to account for the diffusion-reaction problem in catalytic pellet...
In this paper, a multi-region model based on the unified Maxwell-Stefan diffusion theory is develope...
In the present work the results of the investigations on dead zone formation conditions in catalyst ...
The actual transient characteristics of the effectiveness factor for reactions in porous catalyst pa...