There are two main basic vessel types:
- a tank
- a pipe
Both types can be used as continuous reactors or batch reactors. Most commonly, reactors are run at steady-state, but can also be operated in a transient state. When a reactor is first brought back into operation (after maintenance or inoperation) it would be considered to be in a transient state, where key process variables change with time. Both types of reactors may also accommodate one or more solids (reagents, catalyst, or inert materials), but the reagents and products are typically liquids and gases.
There are three main basic models used to estimate the most important process variables of different chemical reactors:
- batch reactor model (batch),
- continuous stirred-tank reactor model (CSTR),
- plug flow reactor
model (PFR).Furthermore, catalytic reactors require separate treatment, whether they are batch, CST, or PF reactors, as the many assumptions of the simpler models are not valid.
Key process variables include
- residence time (τ, lower case Greek tau)
- volume (V)
- temperature (T)
- pressure (P)concentrations of chemical species (C1, C2, C3, ... Cn)
- heat transfer coefficients (h, U)
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