Steady-state (chemical engineering)

In chemistry, a steady state is a situation in which all state variables are constant in spite of ongoing processes that strive to change them. For an entire system to be at steady state, i.e. for all state variables of a system to be constant, there must be a flow through the system (compare mass balance). A simple example of such a system is the case of a bathtub with the tap running but with the drain unplugged: after a certain time, the water flows in and out at the same rate, so the water level (the state variable Volume) stabilizes and the system is in a steady state.

The steady state concept is different from chemical equilibrium. Although both may create a situation where a concentration does not change, in a system at chemical equilibrium, the net reaction rate is zero (products transform into reactants at the same rate as reactants transform into products), while no such limitation exists in the steady state concept. Indeed, there does not have to be a reaction at all for a steady state to develop.

The term steady state is also used to describe a situation where some, but not all, of the state variables of a system are constant. For such a steady state to develop, the system does not have to be a flow system. Therefore, such a steady state can develop in a closed system where a series of chemical reactions take place. Literature in chemical kinetics usually refers to this case, calling it ''steady state approximation''.

In simple systems the steady state is approached by state variables gradually decreasing or increasing until they reach their steady state value. In more complex systems state variables might fluctuate around the theoretical steady state either forever (a limit cycle) or gradually coming closer and closer. It theoretically takes an infinite time to reach steady state, just as it takes an infinite time to reach chemical equilibrium.

Both concepts are, however, frequently used approximations because of the substantial mathematical simplifications these concepts offer. Whether or not these concepts can be used depends on the error the underlying assumptions introduce. So, even though a steady state, from a theoretical point of view, requires constant drivers (e.g. constant inflow rate and constant concentrations in the inflow), the error introduced by assuming steady state for a system with non-constant drivers may be negligible if the steady state is approached fast enough (relatively speaking).

Steady state approximation in chemical kinetics

The ''steady state approximation'', occasionally called the ''stationary-state approximation'' or Bodenstein's ''quasi-steady state approximation'', involves setting the rate of change of a reaction intermediate in a reaction mechanism equal to zero so that the kinetic equations can be simplified by setting the rate of formation of the intermediate equal to the rate of its destruction.

In practice it is sufficient that the rates of formation and destruction are ''approximately'' equal, which means that the net rate of variation of the concentration of the intermediate is small compared to the formation and destruction, and the concentration of the intermediate varies only slowly, similar to the reactants and products (see the equations and the green traces in the figures below).

Its use facilitates the resolution of the differential equations that arise from rate equations, which lack an analytical solution for most mechanisms beyond the simplest ones. The steady state approximation is applied, for example, in Michaelis-Menten kinetics.

As an example, the steady state approximation will be applied to two consecutive, irreversible, homogeneous first order reactions in a closed system. (For heterogeneous reactions, see reactions on surfaces.) This model corresponds, for example, to a series of nuclear decompositions like .

If the rate constants for the following reaction are and ; , combining the rate equations with a mass balance for the system yields three coupled differential equations:

Reaction rates

For species A: \frac = -k_1 ce A

For species B: \frac = k_1 ce A- k_2 ce B/math>

:Here the first (positive) term represents the formation of B by the first step , whose rate depends on the initial reactant A. The second (negative) term represents the consumption of B by the second step , whose rate depends on B as the reactant in that step.

For species C: \frac = k_2 ce B/math>

Analytical solutions

The analytical solutions for these equations (supposing that initial concentrations of every substance except for A are zero) are:P. W. Atkins and J. de Paula, ''Physical Chemistry'' (8th edition, W.H.Freeman 2006), p.811

: ce A ce A0 e^
: \left \ce B \right \begin
\left \ce A \right\frac\left( e^-e^ \right);&k_\ne k_ \\\\
\left \ce A \rightk_te^;&k_ = k_ \\
\end

: \left \ce C \right \begin
\left \ce A \right\left( 1+\frac \right);&k_\ne k_ \\\\
\left \ce A \right\left( 1-e^-k_te^ \right);&k_ = k_ \\
\end

Steady state

If the steady state approximation is applied, then the derivative of the concentration of the intermediate is set to zero. This reduces the second differential equation to an algebraic equation which is much easier to solve.

: \frac = 0 = k_1 ce A- k_2 ce B\Rightarrow \; ce B= \frac ce A

Therefore, \tfrac = k_1 ce A so that ce C ce A0 \left (1- e^ \right ).

Since ce B= \tfrac ce A= \tfrac ce A0 e^ , the concentration of the reaction intermediate B changes with the same time constant as and is not in a steady state in that sense.

Validity

The analytical and approximated solutions should now be compared in order to decide when it is valid to use the steady state approximation. The analytical solution transforms into the approximate one when $k_2 \gg k_1 ,$ because then $e^ \ll e^$ and $k_2-k_1 \approx \; k_2.$ Therefore, it is valid to apply the steady state approximation only if the second reaction is much faster than the first ( is a common criterion), because that means that the intermediate forms slowly and reacts readily so its concentration stays low.

The graphs show concentrations of A (red), B (green) and C (blue) in two cases, calculated from the analytical solution.

When the first reaction is faster it is not valid to assume that the variation of is very small, because is neither low or close to constant: first A transforms into B rapidly and B accumulates because it disappears slowly. As the concentration of A decreases its rate of transformation decreases, at the same time the rate of reaction of B into C increases as more B is formed, so a maximum is reached when $t=\begin \frac & \, k_\ne k_ \\\\ \frac & \, k_ = k_ \\ \end$
From then on the concentration of B decreases.

When the second reaction is faster, after a short induction period during which the steady state approximation does not apply, the concentration of B remains low (and more or less constant in an absolute sense) because its rates of formation and disappearance are almost equal and the steady state approximation can be used.

The equilibrium approximation can sometimes be used in chemical kinetics to yield similar results to the steady state approximation. It consists in assuming that the intermediate arrives rapidly at chemical equilibrium with the reactants. For example, Michaelis-Menten kinetics can be derived assuming equilibrium instead of steady state. Normally the requirements for applying the steady state approximation are laxer: the concentration of the intermediate is only needed to be low and more or less constant (as seen, this has to do only with the rates at which it appears and disappears) but it is not required to be at equilibrium.

Example

The reaction has the following mechanism:

The rate of each species are:

\frac = k_2 ce Br ce H_2+ k_3 ce H ce Br_2-k_4 ce H ce HBr/math>

\frac = k_2 ce Br ce H_2- k_3 ce H ce Br_2- k_4 ce H ce HBr/math>

\frac = 2 k_1 ce Br_2+ k_3 ce H ce Br_2+ k_4 ce H ce HBr- 2 k_5 ce Br2

\frac = -k_1 ce Br_2- k_3 ce H ce Br_2+ k_5 ce Br2

\frac = -k_2 ce Br ce H_2+k_4 ce H ce HBr/math>

These equations cannot be solved, because each one has values that change with time. For example, the first equation contains the concentrations of r and , which depend on time, as can be seen in their respective equations.

To solve the rate equations the steady state approximation can be used. The reactants of this reaction are and , the intermediates are H and Br, and the product is HBr.

For solving the equations, the rates of the intermediates are set to 0 in the steady state approximation:

\begin
& \frac = k_2 ce Br ce H_2-k_3 ce H ce HBrk_4 ce H ce HBr0 \\
& \qquad \longrightarrow k_2 ce Br ce H_2 k_3 ce H ce HBr_2\end

\frac = 2 k_1 ce Br_2- k_2 ce Br ce H_2+ k_3 ce H ce Br_2+ k_4 ce H ce HBr- 2 k_5 ce Br2

From the reaction rate of H, , so the reaction rate of Br can be simplified:

\begin
& 2 k_1 ce Br_2- 2k_5 ce Br2 = 0 \\
& \qquad \longrightarrow ce Br= \frac^\frac ce Br\frac
\end

\frac = k_2 ce Br ce H_2+k_3 ce H ce Br_2- k_4 ce H ce HBr/math>

\begin
& k_2 ce Br ce H_2k_4 ce H ce Br k_3 ce H ce HBr_2\\
& \qquad \longrightarrow \frac =2k_3 ce H ce Br_2\end

The reaction rate of HBr can also be simplifed, changing to , since both values are equal.

The concentration of H from equation 1 can be isolated:

ce H = \frac
=\frac .

The experimentally observed rate is

$v=\frac .$

The experimental rate law is very similar to the rate obtained with the steady state approximation, if is $2k_3 k_2 \sqrt$ and is .

See also

* Lindemann mechanism
* Reaction progress kinetic analysis

Notes and references

{{reflist

External links

* https://chem.libretexts.org/Core/Physical_and_Theoretical_Chemistry/Kinetics/Reaction_Mechanisms/Steady-State_Approximation

Chemical kinetics
Physical chemistry