# Continuous stirred-tank reactor

The **continuous stirred-tank reactor** (**CSTR**), also known as vat- or backmix reactor, or a continuous-*flow* stirred-tank reactor (**C FSTR**)

^{[1]}

^{[2]}, is a common model for a chemical reactor in chemical engineering. A CSTR often refers to a model used to estimate the key unit operation variables when using a continuous agitated-tank reactor to reach a specified output.

^{[notes 1]}The mathematical model works for all fluids: liquids, gases, and slurries.

The behavior of a CSTR is often approximated or modeled by that of a Continuous Ideally Stirred-Tank Reactor (CISTR). All calculations performed with CISTRs assume perfect mixing. In a perfectly mixed reactor, the output composition is identical to composition of the material inside the reactor, which is a function of residence time and rate of reaction. If the residence time is 5-10 times the mixing time, this approximation is valid for engineering purposes. The CISTR model is often used to simplify engineering calculations and can be used to describe research reactors. In practice it can only be approached, in particular in industrial size reactors.

## The modelEdit

Assume:

- perfect or ideal mixing, as stated above

Integral mass balance on number of moles *N*_{i} of species *i* in a reactor of volume *V*.

1. ^{[3]}

where *F _{io}* is the molar flow rate inlet of species

*i*,

*F*the molar flow rate outlet, and stoichiometric coefficient. The reaction rate,

_{i}*r*, is generally dependent on the reactant concentration and the rate constant (

*k*). The rate constant can be determined by using a known empirical reaction rates that is adjusted for temperature using the Arrhenius temperature dependence. Generally, as the temperature increases so does the rate at which the reaction occurs. Residence time, , is the average amount of time a discrete quantity of reagent spends inside the tank.

Assume:

- constant density (valid for most liquids; valid for gases only if there is no net change in the number of moles or drastic temperature change)
- isothermal conditions, or constant temperature (
*k*is constant) - steady state (
*G*_{A}=*r*_{A}*v*) - single, irreversible reaction (
*ν*_{A}= −1) - first-order reaction (
*r*=*kC*_{A})

*A* → products

*N*_{A} = *C*_{A} *V* (where *C*_{A} is the concentration of species *A*, *V* is the volume of the reactor, *N*_{A} is the number of moles of species *A*)

2. ^{[3]}

The values of the variables, outlet concentration and residence time, in Equation 2 are major design criteria.

To model systems that do not obey the assumptions of constant temperature and a single reaction, additional dependent variables must be considered. If the system is considered to be in unsteady-state, a differential equation or a system of coupled differential equations must be solved.

Deviations of the CSTR behaviour can be considered by the dispersion model.^{[4]}

CSTR's are known to be one of the systems which exhibit complex behavior such as steady-state multiplicity, limit cycles and chaos.

## ApplicationEdit

Continuous flow stirred-tank reactors are usually applied in waste water treatment processes. CSTRs facilitate rapid dilution rates which make them resistant to both high pH and low pH volatile fatty acid wastes. CSTRs are less efficient compared to other types of reactors as they require larger reactor volumes to achieve the same reaction rate as other reactor models such as Plug Flow Reactors.

## See alsoEdit

## NotesEdit

**^**Chemical reactors often have significant heat effects, so it is important to be able to add or remove heat from them. In a CSTR (continuous stirred tank reactor) the heat is added or removed by virtue of the temperature difference between a jacket fluid and the reactor fluid. Often, the heat transfer fluid is pumped through agitation nozzle that circulates the fluid through the jacket at a high velocity. The reactant conversion in a chemical reactor is a function of a residence time or its inverse, the space velocity. For a CSTR, the product concentration can be controlled by manipulating the feed flow rate, which changes the residence time for a constant chemical reactor. Occasionally the term "continuous" is misinterpreted as a modifier for "stirred", as in 'continuously stirred'. This misinterpretation is especially prevalent in the civil engineering literature. As explained in the article,"continuous" means 'continuous-flow' — and hence these devices are sometimes called, in full,*continuous-flow stirred-tank reactors*(*CFSTR's*).

## ReferencesEdit

**^**Enzyme Technology. Continuous flow stirred tank reactors. Martin Chaplin; 6 August, 2014. Accessed 2018-10-13.**^**Reactor Theory and Practice. Continuous Flow Stirred Tank Reactor (CFSTR), in Chapter 8: Methods for Studying Biofilms; Section 2: Reactor Theory and Practice;*The Biofilms Hypertextbook*; Alfred B. Cunningham, John E. Lennox, and Rockford J. Ross (Eds.); Version 4.2; 04 January 2010. Accessed 2018-10-13.- ^
^{a}^{b}Schmidt, Lanny D. (1998).*The Engineering of Chemical Reactions*. New York: Oxford University Press. ISBN 0-19-510588-5. **^**Colli, A. N.; Bisang, J. M. (December 2011). "Generalized study of the temporal behaviour in recirculating electrochemical reactor systems".*Electrochimica Acta*.**58**: 406–416. doi:10.1016/j.electacta.2011.09.058.