In a continuousβstirredβtank reactor (CSTR) the reactants are perfectly mixed, so the composition inside the reactor is identical to that of the outlet stream. This idealization allows us to write a material balance that directly relates the reaction rate to the residence time of the fluid.
For a single, irreversible, firstβorder reaction (A rightarrow products) the rate expression is (r_A = -k C_A), where (k) is the firstβorder rate constant (sβ»ΒΉ) and (C_A) is the concentration of A. Substituting this rate into the CSTR steadyβstate balance yields a simple algebraic relationship between conversion, rate constant, and residence time.
The conversion (X) (fraction of A that reacts) can therefore be expressed as a function of the kinetic parameter (k) and the hydraulic residence time (tau). This closedβform solution is widely used for quick design checks and for coupling kinetic models with process simulators.
What is a continuous-stirred-tank reactor (CSTR)?
How do you calculate reaction conversion in a CSTR?
What does first-order reaction mean in this context?
How does residence time affect conversion in a CSTR?
What is the significance of the rate constant (k) in this calculation?
Can this calculator be used for reversible reactions?
What units should I use for the rate constant (k)?
Results are for informational purposes only and do not constitute professional advice.
