Model Reduction in Chemical Systems- an Alternative Method Applying Discrete Approximation

2018 ◽  
Author(s):  
Magne Fjeld

<div><div>This paper addresses model reduction in large or spatially distributed systems including diffusion of matter and chemical reactions. If diffusion is present, it would be represented by a diffusion operator (always including a spatial second derivative term). If diffusion is not present, spatial discretization is straightforward. In the latter case, applying the concept of chemical invariants, or the concept of asymptotic chemical invariants, paves the way for model reduction through elimination of the invariants. Inclusion of diffusion destroys the opportunity to obtain invariants , when numerical discretization of the diffusion term is applied. However, the paper demonstrates that application of the invariant concept may be applied even in the case of diffusion of matter in a chemical tubular reactor, if relying on an approximation in modelling of a tubular reactor by a tank-in-the series model. For nonreacting matter, the quality and numerical properties of the tanks-in-the-series model approximation of a tubular reactor is well documented in the literature. However, there is no general proof available for the quality and effectiveness of such an approximation when chemical reactions are present, although example cases show good approximation.<br></div></div><div><div><br></div></div>

2018 ◽  
Author(s):  
Magne Fjeld

<div><div>This paper addresses model reduction in large or spatially distributed systems including diffusion of matter and chemical reactions. If diffusion is present, it would be represented by a diffusion operator (always including a spatial second derivative term). If diffusion is not present, spatial discretization is straightforward. In the latter case, applying the concept of chemical invariants, or the concept of asymptotic chemical invariants, paves the way for model reduction through elimination of the invariants. Inclusion of diffusion destroys the opportunity to obtain invariants , when numerical discretization of the diffusion term is applied. However, the paper demonstrates that application of the invariant concept may be applied even in the case of diffusion of matter in a chemical tubular reactor, if relying on an approximation in modelling of a tubular reactor by a tank-in-the series model. For nonreacting matter, the quality and numerical properties of the tanks-in-the-series model approximation of a tubular reactor is well documented in the literature. However, there is no general proof available for the quality and effectiveness of such an approximation when chemical reactions are present, although example cases show good approximation.<br></div></div><div><div><br></div></div>


2018 ◽  
Author(s):  
Magne Fjeld

No numerical data. <p><b><br> </b>Dynamic model reduction techniques based on the decomposition of the stoichiometric matrix to find the chemical invariant, break down if axial diffusion is present in a tubular reactor.</p> <p>Straightforward discretization of the partial differential operator does indeed show that the resulting discrete dynamic model cannot generally be partioned to obtain the reaction variant vector and the reaction invariant (asymptotic) vector. However, the paper demonstrate that, if the diffusional tubular reactor is discretely and approximatively represented by tanks-in-series, then matrix approaches to successfully find the chemical variant and invariant vectors of the resulting chemical process model is possible. </p>


2018 ◽  
Author(s):  
Magne Fjeld

No numerical data. <p><b><br> </b>Dynamic model reduction techniques based on the decomposition of the stoichiometric matrix to find the chemical invariant, break down if axial diffusion is present in a tubular reactor.</p> <p>Straightforward discretization of the partial differential operator does indeed show that the resulting discrete dynamic model cannot generally be partioned to obtain the reaction variant vector and the reaction invariant (asymptotic) vector. However, the paper demonstrate that, if the diffusional tubular reactor is discretely and approximatively represented by tanks-in-series, then matrix approaches to successfully find the chemical variant and invariant vectors of the resulting chemical process model is possible. </p>


1983 ◽  
Vol 20 (04) ◽  
pp. 877-883
Author(s):  
Peter Hall

Several stochastic models have been proposed to describe the kinetic theory of reversible chemical reactions. However, in macroscopic systems the effects of stochastic variability are often outweighed by mean effects. In the present paper we show that some observed phenomena can be explained quite adequately by a stochastic model in which the stochastic variability is not negligible in comparison with mean effects. Our argument involves approximations to a stochastic model for competing chemical reactions.


2019 ◽  
Vol 16 (150) ◽  
pp. 20180586 ◽  
Author(s):  
Yutaka Hori ◽  
Hiroki Miyazako

Diffusion and flow-driven instability, or transport-driven instability, is one of the central mechanisms to generate inhomogeneous gradient of concentrations in spatially distributed chemical systems. However, verifying the transport-driven instability of reaction–diffusion–advection systems requires checking the Jacobian eigenvalues of infinitely many Fourier modes, which is computationally intractable. To overcome this limitation, this paper proposes mathematical optimization algorithms that determine the stability/instability of reaction–diffusion–advection systems by finite steps of algebraic calculations. Specifically, the stability/instability analysis of Fourier modes is formulated as a sum-of-squares optimization program, which is a class of convex optimization whose solvers are widely available as software packages. The optimization program is further extended for facile computation of the destabilizing spatial modes. This extension allows for predicting and designing the shape of the concentration gradient without simulating the governing equations. The streamlined analysis process of self-organized pattern formation is demonstrated with a simple illustrative reaction model with diffusion and advection.


1996 ◽  
Vol 1 (1) ◽  
Author(s):  
Gerhard J. Pietsch

AbstractThe dielectric barrier discharge consists of numerous non-thermal microdischarges which are temporally and spatially distributed within the reactor volume. From a refined modeling of microdischarges, chemical reactions, and the interaction of discharges and process gas, the properties of the reactor can be evaluated. Quantitative results for the ozone generation process are presented.


2006 ◽  
Vol 6 (1) ◽  
pp. 187-195 ◽  
Author(s):  
A. Sandu ◽  
R. Sander

Abstract. This paper presents the new version 2.1 of the Kinetic PreProcessor (KPP). Taking a set of chemical reactions and their rate coefficients as input, KPP generates Fortran90, Fortran77, Matlab, or C code for the temporal integration of the kinetic system. Efficiency is obtained by carefully exploiting the sparsity structures of the Jacobian and of the Hessian. A comprehensive suite of stiff numerical integrators is also provided. Moreover, KPP can be used to generate the tangent linear model, as well as the continuous and discrete adjoint models of the chemical system.


2021 ◽  
Author(s):  
Anne-Déborah C. Nguindjel ◽  
Peter A. Korevaar

Out-of-equilibrium chemical systems, comprising reaction networks and molecular self-assembly pathways, rely on the delivery of reagents. Rather than via external flow, diffusion or convection, we aim at self-sustained reagent delivery. Therefore, we explore how the coupling of Marangoni flow with chemical reactions can generate self-sustained flows, driven by said chemical reactions, and – in turn – sustained by the delivery of reagents for this reaction. We combine a photoacid generator with a pH-responsive surfactant, such that local UV exposure decreases the pH, increases the surface tension and triggers the emergence of a Marangoni flow. We study the impact of reagent concentrations and identify threshold conditions at which flow can emerge. Surprisingly, we unraveled an antagonistic influence of the reagents on key features of the flow such as interfacial velocity and duration, and rationalize these findings via a kinetic model. Our study displays the potential of reaction-driven flow to establish autonomous control in fuel delivery of out-of-equilibrium systems.


Sign in / Sign up

Export Citation Format

Share Document