ABSTRACT

In this work, a finite element scheme is proposed using a method of Euler-Taylor-Galerkin described in [1], for a non-linear model which describes the behavior of a new chemo-fluidic oscillator, [2]. This model is expressed by the coupling of an ordinary differential equation describing the hydrogel dynamics, the non-linear transport equation and an auxiliary equation determining the flux volume. The numerical solution is constructed by taking a semi-discretization in time of the transport equation, employing forward-time Taylor series expansions including time derivatives of second order and third order, avoiding instabilities problems. In this semi discrete equation, the spatial variable is approximated by the finite element formulation according to Galerkin. Some simulations are carried out taking different initial conditions for the concentration of the hydrogel. The numerical results describes the oscillatory behavior of the system as in [2], where MatLab tools are used as black box.

Facultad de Ciencias Naturales y Matemáticas, Escuela Superior Politécnica del Litoral, Km. 30.5 Vía Perimetral, Guayaquil, Ecuador

ialvarez@espol.edu.ec

Facultad de Ciencias Naturales y Matemáticas, Escuela Superior Politécnica del Litoral, Km. 30.5 Vía Perimetral, Guayaquil, Ecuador

davetera@espol.edu.ec

Facultad de Ciencias Naturales y Matemáticas, Escuela Superior Politécnica del Litoral, Km. 30.5 Vía Perimetral, Guayaquil, Ecuador

wangulo@espol,edu.ec

Facultad de Ciencias Naturales y Matemáticas, Escuela Superior Politécnica del Litoral, Km. 30.5 Vía Perimetral, Guayaquil, Ecuador

dany@espol.edu.ec

Facultad de Ciencias de la Computación y Matemáticas, Universidad de la Habana, calle 25 y Vedado , La Habana , Cuba

angela@matcom.uh.cu

Keywords: [New chemo-fluidic oscillator], [Non-linear model],[Finite element], [hydrogel dynamics,].

Introduction12

Self-oscillating systems play an important role in both the natural sciences (biology or chemistry) and technology (micro electromechanical or electronic systems) because they can be coupled to other systems, one of their most important applications is the use as a system clock to trigger regular events such as circadian rhythm or electronic systems.

This work refers to the use of a Taylor – Galerkin method for applying finite element to the nonlinear system that controls the behavior of the new chemo oscillator – fluidic and determine its numerical modeling. The mathematical problem was raised by Páez who made a numerical approximation of the transport PDA using the well-known Line Method, however, the EDOS system provides a very rough approximation of the solution of the transport equation.

First, this is due to the first-order discretization in space and secondly because it can propagate abrupt changes or steep fronts, which is a well-known computational problem in the numerical solution of hyperbolic PED.

In order to describe the dynamics of the chemo-fluidic oscillator a set of mathematical models was used, which I pose a challenge due to the complexity of the system, since the oscillator is affected by various nonlinearities that come from the characteristics of the hydrogel and the bidirectional coupling between the chemical and fluidic domains. The hydrogel is designed in such a way that an increase in the concentration of alcohol reduces its size and vice versa. Therefore, at low concentrations of alcohol, the hydrogel valve is closed, while high concentrations of alcohol open the valve. A bypass channel is connected to the valve inlet, to allow a continuous flow of unidirectional fluid near the hydrogel independent of whether the hydrogel valve is open or closed.

Therefore to facilitate the modeling process, the system was divided into the fluidic domain describing the behavior of volumetric flows and system pressures during operation and chemical domain which in turn divided into two parts the description of hydrogel dynamics and the modeling of the delay line , resulting in a coupled system composed of the one-dimensional transport EDP, the EDO that models the dynamic behavior of the hydrogel and the equation that determines the volume in the buffer.

To perform this work following very closely what Donea did is semi-discretized the equation of nonlinear transport using Taylor's serial expansions at the time of first, second and third order to obtain a second order differential equation in the space in which we apply Galerkin's variational formulation to use the finite element method and obtain the system of linear equations that needs the value of the variable that determines the the size of the hydrogel that is obtained for each instant of time by applying the Runge -Kutta 4 method and the buffer volume that is found using numerical integration methods.

Analyzing in more detail its mathematical modeling and the numerical solution of this New Chemical-Fluidic Oscillator based on intelligent hydrogels was one of the reasons for the realization of this work in addition to extending the linear method used by Donea [2] for the nonlinear transport equation and providing a solution methodology for models of new oscillators involving the nonlinear one-dimensional transport equation.

1.Design of a chemo-fluoscillator

The new fluid chemo oscillator isbased on a negative feedback circuit containing a delay line, where negative feedback is provided by a hydrogel valve that has the ability to change its size depending on the temperature and concentration of the aqueous solution that is in contact with live with the hydrogel. In this new oscillator the temperature remains constant so the only parameter that produces a change in the size of the hydrogel is the concentration of alcohol.

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Figure 1. Photography of the manufactured chemo-fluidic oscillator circuit, filled with a highly dyed solution for better visibility of the channels. External sources of constant flow and pressure are shown schematically. Equivalent fluidic circuit. The hydrogel valve is represented by a controlled flow source.

The oscillator is powered by three constant sources. The first is a constant flow source that supplies the system with an alcohol concentration solution. A second source provides deionized water at a constant pressure located at Node 1. Water flows through a long channel called the damping line and then mixes into Node 2 with the alcohol solution provided by , and then the mixed solution enters the channel of the long fluid that acts as a delay line. Using this channel, the solution is transported at a rate determined by the flow through the delay line and its cross-section. The end of this channel is connected to the inlet of the hydrogel valve, whosefluid behavior is controlled by the alcohol concentration of the solution. Finally, a bypass channel connects to Node 3. to drain the liquid to a conveniently chosen constant flow rate.

The micro-fluid system will be modeled through Kirchhoff's laws, within the framework of network theory for a circuit. This approach is used by how small the dimensions of the magnitudes that govern the operation of the oscillator within the study of the micro fluids since they are in a range of micro nano and peak liter, therefore, the pressure is considered analogous to the voltage and volumetric flow rate to the electric current, as well as the lines of delay to the resistors. In this context, the oscillator can be described by the fluid network presented in Figure 2.

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Figure 2. Equivalent fluidic circuit. The hydrogel valve is represented by a controlled flow source.

2.Mathematical model of chemical oscillator - fluidic.

The mathematical problem to be studied was raised by Páez et al. en , and consists in finding functions : such that:


The data in this problem are the functions , ,, , , and where is the unknown value to be determined from the function at the end ; which must also be determined simultaneously, in this problem, the function : defined by:


Where it is a known function and is a constant also known.

2.1 Semi - discretization in problem time (2)

The transport equation is considered


If it is denoted by the value of the function evaluated on the node, then a schema in finite differences very simple to approximate the temporal derivative in would be the one obtained by the serial expansion of Taylor, in the first order, around the point :


From here, despising him you have to:


which is the well-known forward-time (Euler) scheme.

If the EDP is now evaluated in you have for each EDO:


Now, using the schema type forward – time la expression is transformed into:


Here is the value in which it is determined using Ruge -Kutta 4 applied to the initial problem

Where, in general, is the unknown value at the border for time. For this schema, the known constant is the initial iteration. In the context of the finite differences method, the expression produces an unstable numerical scheme by approx approximation of the spatial derivative term using a centered scheme, i.e.


Lto instability arises because the partial derivative relative to the spatial coordinate is evaluated at a time level earlier than the time level where the term temporal derivative is evaluated. Therefore, a stable schema can be obtained if the two derived terms s and s evaluate at the same time level (at least a second order in ). In this order of ideas, Donea states that the easiest way to make the evaluation of both terms of the expression at the same time level, is by expressing the approximation in difference for the term of temporal derivative at the time level. One way to achieve this is through a forward-looking Taylor serial expansion over time, including second- and third-order derivatives. That is, from the expansion


The term is cleared and (considering again the notation that was introduced for the forward-time scheme) d bypreciatingthe term and using discretization over time, for the transport equation can be replaced by the following:


For each. The second and third derived terms that appear in this expression can be determined first by successive differentiation of the equation and then by evaluating over time. The calculation for the second derivative is illustrated below: On the one hand


Now, combining and, evaluated in , with the equation you have


The expression (12) is similar to that proposed by Leveque when generating stabilized numerical methods by dictating a diffuse term to the nonlinear transport equation. However, it should be noted that the term appears as part of the approximation by difference for the partial derivative of C with respect to time, evaluated at level n. On the other hand, following closely what Donea suggested the term of the third-order partial derivative that appears in Taylor's serial expansion is expressed in a mixed space-time form. This mixed form of the derivative will allow the use of type finite elements with a simple modification of the usual and consistent mass matrix quite similarly as is done in the context of weighted residues of petrov-Galerkin.

By developing the specified products and grouping the terms we have that the problem raised in (11) is semi discretized over time and for each the next problem arises,

Given , find , such that:


To be able to solve the differential equation of Second Order posed in (15) we need 2 conditions, but the problem only provides us with a condition so it was necessary to impose asecond condition to solve the problem, which we induc from the mathematical model for the problem of transport proper to the chemo-fluid oscillator:


Deduction of the condition in

From the EDP:


semi-discretization of


That by evaluating her in, we have a Condition of Robin.

2.2 Taylor Method - Galerkin

Considering the internal product on the range :


Applying the definition of the internal product in the spaces, with border conditions of Dirilecht and Robin, applying the integration formula in parts and replacing the functions in a way that we have for the problem:

2.3 Finite Element Method

We will consider a discretization of finite elements as explained above, but adapted to the working interval. In effect the partition of this interval corresponds to the longitudinal discretization of the delay line channel into length elements for Being , the partition represents a mesh of points that we will denote by .

If we write using the elementary formulation we would have:

3.Numerical experimentation.

After raising the mathematical part for the model and obtaining the system of equations, a program was designed in Matlab for the coupled system where several tests were performed with their respective numerical adjustments based on the theoretical definitions explained in chapters 2 and 3.

Each experiment details the change in the initial concentration which is a unique experimental value for the operation of the hydrogel that is not listed as data in Páez and has been imposed on it according to the physical model.

Experiment 1

Values are taken in the space of (nodes);  ;  ;  ; Courant 0.1

A constant value was taken as a condition which in this case is the experimental value with which the numerical part worked in the initial study.

The values of those derived from the concentration found in are replaced by forward differences (Euler) for .

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Figure 3. Response of the chemo-fluidicoscillator modeled by the system.

Periodic behavior can be observed in the Hidrogel which is what allows the device to function as an oscillator with negative feedback resulting from the increase and decrease of the alcohol mixture in the hydrogel chamber but at the beginning of the flow of mixture of alcohol and water there is instability in the wave fronts that are then regularized as the process of opening and closing the valve progresses that because the hydrogel suffers deformation greater than the length of the camera

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Figurineat 4. Response of the chemo-fluidic oscillator modeled by state variables.

Experiment 2

In this trial, a quadratic profile was taken as an initial condition since there is a mixture of water and alcohol in the canal resulting from deionized water flows and alcohol but not reaching the minimum concentration level so that the hydrogel reacts and begins to compress due to the increase in alcohol, periodic behavior occurs , but with less disturbance at the beginning of the process allowing a more stable and smooth concentration flow on the wave fronts.

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Figurineat 5. Response of the chemo-fluidic oscillator modeled by state variables.

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Figure 3. Response of the chemo-fluidicoscillator modeled by the system.

4. CONCLUSIONS AND RECOMMENDATIONS.

The first observation that can be made is that the method applied to the system composed of equations reproduces the dynamics of the original numerical model of Paez, with small differences in amplitude and period, but that it is able to produce stable periodic signals for parameter configuration without needing any external forging, which means that the oscillating behavior is self-excited.

The second observation is that from a numerical approximation of the linear transport equation (constant velocity) based on the Euler-Taylor-Galerkin method for discretization over time and the Finite Elements Method for discretization in the space posed by Donea, by applying the same method with some variations in the initial conditions and border equation in the equation of the transport of the nonlinear system that is also coupled to a nonlinear ordinary differential equation that governs the behavior of the hydrogel and another equation that controls the volume of the buffert resulting in a complex system of solving, satisfactory results were obtained in relation to its oscillation and its periodic and dimensioned movement. It is very important to note that this numerical model makes it possible to observe that if we change the initial value there will be a variation at the beginning of the hydrogel's operation that would be in the stationary regimen but that after this initial regimen the hydrogel shows an oscillating and periodic behavior typical of Paez's initial analysis.

The third observation is that this numerical analysis applied to the chemo-fluidic oscillator analytically contributes to the understanding that the valve composed of the hydrogel is extremely sensitive to the variation of the parameters, i.e. it has the ability to drastically change its volume under small variations of special thermodynamic parameters.

In this research another option could be given to mathematically model the domains of the oscillator, in the fluidic domain given by the flow network, the transport of concentration through the delay line and in the chemical domain given by the behavior of the hydrogel and the concentration of alcohol that produce a smooth dynamic system in parts.

It is recommended to use for future studies a mathematical refinement method such as the Galerkin-Discontinuous method to be able to model in more detail the behavior of the Chemo-fluidic Oscillator.

5. References.

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Jean Donea, A Taylor – Galerkin Method for Convective Transport problems.

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