Perturbation solutions to the gas-solid reaction model of Part I are obtained for pi --> infinity and beta --> 0, both of which are found to yield the product layer diffusion-controlled shrinking core result in the leading order. In the latter case (i.e. beta --> 0) it is shown that a conceptual difficulty arises for internal structures which require infinite time for complete conversion since a fully reacted product layer cannot form. One-term perturbation corrections for both cases are also obtained using a singular perturbation method. For the first case (i.e. large psi) it is found that the conversion correction to the shrinking core model predicition can be significant even for reasonably large values of psi, and the error is as seriou...
A number of physical and mathematical models have been proposed for noncatalytic solid-gas reactions...
For fluid-solid reactions a random pore model is developed which accounts for arbitrary pore-size di...
AbstractMany chemical engineering processes involve a reaction between a diffusing substance and an ...
Perturbation solutions to the gas-solid reaction model of Part I are obtained for pi --> infinity an...
Perturbation solutions to the gas-solid reaction model of Part I are obtained for ψ → ∞ and β → 0, b...
Gas-solid reactions find importance in numerous processes including conventional ones, involving gas...
A new numerical technique for simulating gas-solid reactions including diffusion through the reactan...
By using a matched asymptotic expansion technique, the shrinking core model (SCM) used in non-cataly...
A numerical comparison between the shrinking core model and the grain model is carried out, in the c...
37-41Gas-solid reaction rates for an ellipsoidal particle have been derived in this paper. The shri...
Reactions between gases and solid particles are commonly modeled using a shrinking core framework, w...
In this paper, a mathematical model is developed to calculate the conversion and the residence time...
The shrinking core model, including the effect of transient diffusion, non-linear kinetics and non-i...
A generalised zone reaction model for gas-solid reactions is proposed. It has been shown that the mo...
The recent random-pore model (Bhatia and Perlmutter, 1980, 1981a; Gavalas, 1980) is further develope...
A number of physical and mathematical models have been proposed for noncatalytic solid-gas reactions...
For fluid-solid reactions a random pore model is developed which accounts for arbitrary pore-size di...
AbstractMany chemical engineering processes involve a reaction between a diffusing substance and an ...
Perturbation solutions to the gas-solid reaction model of Part I are obtained for pi --> infinity an...
Perturbation solutions to the gas-solid reaction model of Part I are obtained for ψ → ∞ and β → 0, b...
Gas-solid reactions find importance in numerous processes including conventional ones, involving gas...
A new numerical technique for simulating gas-solid reactions including diffusion through the reactan...
By using a matched asymptotic expansion technique, the shrinking core model (SCM) used in non-cataly...
A numerical comparison between the shrinking core model and the grain model is carried out, in the c...
37-41Gas-solid reaction rates for an ellipsoidal particle have been derived in this paper. The shri...
Reactions between gases and solid particles are commonly modeled using a shrinking core framework, w...
In this paper, a mathematical model is developed to calculate the conversion and the residence time...
The shrinking core model, including the effect of transient diffusion, non-linear kinetics and non-i...
A generalised zone reaction model for gas-solid reactions is proposed. It has been shown that the mo...
The recent random-pore model (Bhatia and Perlmutter, 1980, 1981a; Gavalas, 1980) is further develope...
A number of physical and mathematical models have been proposed for noncatalytic solid-gas reactions...
For fluid-solid reactions a random pore model is developed which accounts for arbitrary pore-size di...
AbstractMany chemical engineering processes involve a reaction between a diffusing substance and an ...