Dynamics and Hopf Bifurcation Analysis of a Chemostat Model with Modified Growth Rate and Variable Yield Coefficient ()
1. Introduction
Researchers have been studying extensively to improve product yield in chemical reactors or bio-reactors for many years. To gain desired scale of production, it is necessary to find effective engineering instruments and mechanism in a bio-reactor. One such engineering instrument is application of oscillatory external force. Since implementation of oscillatory external force is costly, it has very limited use in industry [1] [2]. Many researchers have studied the oscillatory operations in more than one reactors combined in series [3] [4] [5] [6] [7]. In an oscillatory operation, the values of the parameters in a model are determined for which a steady concentration of substrate into one reactor stimulates the successive reactors periodically. This automated periodic forcing of a reactor requires no extra energy or logistics. This is why it is very important to determine the dynamic conditions for which natural oscillations occur in a bio-reactor. So that it can be used to force another bio-reactor periodically without any external forcing [3] [6]. Since we would like to use natural oscillations of a reactor to force another one arranged in series periodically, it is practical to determine sufficient conditions for which natural oscillations occur in the first reactor. Nelson and Sidhu [8] believed that it is better to determine a benchmark for the maximum output from a single reactor before investigating a two-reactor system. Balakrishnan and Yang [9] examined a single bio-reactor model by direct integration on limited range of parameter values. On the other hand, Nelson and Sidhu [8] studied the same model analytically by exploiting theory of bifurcation and path following methods.
2. Model Equations
Our aim is to investigate a microbial system, the process of using systems biology to understand microbes and their environment, where growth of the cell mass (X) depends on substrate species (S). In this study, the specific growth rate is taken from the Haldane kinetic model with variable yield coefficient. We are studying a simple chemostat model to optimize the cell mass concentration as a function of residence time in a reactor and similar kind of study of microbial systems can be found in [1] [3] [6] [9].
2.1. Dimensional Model Description
The microbial system which we consider in this study is represented by the following Equations (1)-(4)
(1)
(2)
with the specific growth rate
(3)
and a Monod expression with variable Yield Coefficients
(4)
where F is the flow rate (l·hr−1), Ks is the half-saturation constant (g·l−1), Ki is the inhibitory constant (g·l−1), V is the volume (l), X0 is the initial cell mass concentration (g·l−1), S0 is the initial substrate concentration (g·l−1),
is the maximum specific growth rate (/h), α(-) and β(g·l−1) are constant yield coefficients.
2.2. Dimensionless Model
To make the above model dimensionless, we use the transformations
,
, and
and we get the following dimensionless model containing the parameters
, and
.
(5)
(6)
where
, and
.
We consider a chemostat setup consists of a sterile feed means that
will be zero and assume
(residence time) as our primary bifurcation parameter. Our secondary bifurcation parameters are
(substrate concentration in the feed),
(dimensionless yield coefficient) which depends on specific microbial system and hence not so flexible for tuning, and
(dimensionless inhibitory constant). We will denote the dimensional and dimensionless variables interchangeably by the same names and notations since they are connected by one to one relation. For example, “the yield coefficient” and “the dimensionless yield coefficient” will be denoted by the same notation
.
3. Results
3.1. Steady State Solutions and Their Stability
3.1.1. Steady State Solutions
The system of differential Equations (5) and (6) has one washout steady state solution
, where
(7)
and two no washout steady state solutions
and
where
(8)
and
(9)
If
, then the substrate components,
and
, in (8) and (9) will be real and positive. Conditions for the cell mass concentration component,
, in (8) to be real and non-negative are
and
, and for the cell mass concentration,
, in (9) to be real and non-negative are
and
. These conditions for the cell mass concentration lead us to conclude that both no washout steady state solutions are physically meaningful whenever
and
. We need to study the effect of variation of the residence time on the reactor’s steady state performance. That means, we need to investigate the relationship between the cell mass concentration X and the residence time
in the no washout state. Specially, we want to determine the value of
at which X will have optimum values.
From Equation (8), we can show that
at
(10)
subject to
(11)
and
(12)
will be negative if critical point
in (10) belongs to the following interval
where the upper bound of
depends on
, and
. For example, if we take
, we get an upper bound of
at 3.313471. The
does not exceed the upper bound when
(13)
or
(14)
Therefore, a local maximum value of X has occurred at
.
From Equation (9), we can show that
at
, subject to the restriction that
and
.
will be negative if the critical point
is satisfied the following conditions.
(15)
Therefore, X has a local maximum value at
.
3.1.2. Stability of the Washout Steady State Solution
Jacobian Matrix: At the washout steady state solution (7), the system (5) and (6) has the following Jacobian matrix which has the eigenvalues
and
.
(16)
Therefore, if
then the washout steady state solution will be stable.
3.1.3. Stability of No Washout Steady State Solution (8)
Jacobian Matrix: At the washout steady state solution (8), the system (5) and (6) has the following Jacobian matrix
where
(17)
(18)
(19)
and
.
By following the restrictions (11), (12), (13) and (14), it can be shown that
is negative and
is positive at the critical point
. Hence, we can make a conclusion that the steady state solution (8) is stable at
and has practical importance to study.
If
or
, then
and Jacobian matrix has a zero eigenvalue. The required conditions to have double zero eigenvalues of the Jacobian matrix are
It can be shown that the conditions to have double zero eigenvalues are satisfied when
Here
is positive since
and
. This positivity of
in the feed immediately implies that double zero eigenvalues can occur.
3.1.4. Stability of No Washout Steady State Solution (9)
Jacobian Matrix: At the washout steady state solution (9), the system (5) and (6) has the following Jacobian matrix
where
(20)
(21)
(22)
and
.
By following the condition (15), the
is never negative and the
is never positive at the critical point. Therefore, the maximum steady state solution (9) is not stable.
If
or
, then
and Jacobian matrix has a zero eigenvalue. But the later value of
is not relevant. The required conditions to have double zero eigenvalues of the Jacobian matrix are
It can be shown that the conditions to have double zero eigenvalues are satisfied when
Here
is positive since
and
. This positivity of
in the feed immediately implies that double zero eigenvalues can occur.
3.1.5. Hopf Bifurcation on the No Washout Steady State Solution (8)
A Hopf bifurcation will take place if
and
.
will be negative when
(23)
These conditions are equivalent to the following three cases. In each case, the values of the residence time correspond to the root of
at which Hopf bifurcations occur .
Case I:
,
, and
. If we take
, and
, then
at
(Figure 1) (other values are possible).
A Degenerate Hopf bifurcation occurs at a value of residence time
where two Hopf points resulting in a single point by annihilating each other which is known as H21 degeneracy and it occurs when
and
[10].
In this case, it is possible to show that when
,
vanishes for suitable values of
and
. For example, if we take
,
, then
vanishes at
. Therefore, if the substrate concentration
is adequately small (
) or (
) natural oscillations are not possible to occur for
,
.
Case II:
,
, and
. Let
,
,
, then
at
and
(Figure 2) (other values are possible).
Figure 1. Hopf point unfolding curve. Parameter values:
.
Figure 2. Hopf point unfolding curve. Parameter values:
.
For this situation, it is possible to show that when
,
vanishes for appropriate values of
and
. For example, if
,
, then
vanishes at
. Therefore, if the substrate concentration
is sufficiently small (
) or (
) natural oscillations are not possible for
,
.
Case III:
,
, and
. Let
,
,
, then
at
and
(Figure 3) (other values are possible).
In this case, it is possible to show that when
,
vanishes for appropriate values of
and
. For example, if we take
,
, then
Figure 3. Hopf point unfolding curve. Parameter values:
.
vanishes at
. Therefore, if the substrate concentration
is small enough (
) or (
) natural oscillations are not possible for
,
.
In all cases above, we have used parameter values
,
,
,
, and
from [6] [9].
The work reported in [3] [6] [9] used
without confirming conditions under which natural oscillations are possible. The work in [8] reported that natural oscillations are impossible for sufficiently small substrate concentration
, for
. Both cases above were observed for the specific growth rate equation
. In our work, we have used
. It is possible to gain natural oscillations for even significantly smaller values of
.
4. Conclusion
We have studied, analytically, a simple chemostat model in a flow reactor with a variable yield coefficient in which the growth rate is taken to be a Haldane expression. In this study, three steady-state solutions have been discussed, which characterize no washout and washout circumstances in the closed photobioreactor. Under suitable parameter values, a stable steady-state solution attains its maximum value. We also corroborated the parameter ranges for the model with variable yield coefficient and growth rate, which describes natural oscillations in the chemostat. In all three cases of Hopf bifurcation analysis, we have found that natural oscillations can be achieved at significantly lower values of the substrate concentrations. In cases I, II, and III, the value is
,
, and
respectively. A previous study reported that natural oscillation is achieved at a substrate concentration
and results claim that natural oscillations are possible for sufficiently large values of substrate concentration (
) but the conditions of natural oscillations were not reported.