Ideal Reactor Design Equations and Formulas Calculator
Chemical Engineering Wastewater Water Treatment
Solving For Theoretical Mean Residence Time
Inputs:
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Conversions:
reactor volume (V)
= 0
= 0
meter^3
flow rate (Q)
= 0
= 0
meter^3/second
Solution:
theoretical mean residence time (tR) = NOT CALCULATED
Other Units:
Change Equation
Select to solve for a different unknown
Residence Time
Step input for completely mixed or
continuously stirred tank reactor CSTR
Pulse Input for completely mixed or
continuously stirred tank reactor CSTR
Plug Flor Reactor PFR
Where
Select to solve for a different unknown
Residence Time
 | theoretical mean residence time |
 | reactor volume |
 | reactor flow rate |
Step input for completely mixed or
continuously stirred tank reactor CSTR
 | concentration |
 | initial concentration |
 | time |
 | theoretical mean detention time |
Pulse Input for completely mixed or
continuously stirred tank reactor CSTR
 | concentration |
 | initial concentration |
 | time |
 | theoretical mean detention time |
 | concentration at n tank in series |
Plug Flor Reactor PFR
 
| step input: when t < tR, C = 0 when t >= tR, C = C0 pulse input: when t = tR, C = C0 when t < tR, C = 0 when t > tR, C = 0 |
Where
| tR | = | theoretical mean residence time |
| V | = | reactor volume |
| Q | = | reactor flow rate |
| C | = | concentration at time |
| C0 | = | initial concentration |
| Cn | = | concentration at tank n |
| t | = | time |
| n | = | number of tanks |
References - Books:
1) Warren Viessman and Mark J. Hammer. 1993. Water Supply and Pollution Control. Harper Collins College Publishers, Inc. 5th ed.
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