Solving For Flow Rate

reactor volume (V) = 0 = 0 meter^3 |

theoretical mean residence time (t _{R})= 0 = 0 second |

reactor flow rate (Q) = NOT CALCULATED |

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 < t _{R}, C = 0when t >= t _{R}, C = C_{0}pulse input: when t = t _{R}, C = C_{0}when t < t _{R}, C = 0when t > t _{R}, C = 0 |

Where

t_{R} | = | theoretical mean residence time |

V | = | reactor volume |

Q | = | reactor flow rate |

C | = | concentration at time |

C_{0} | = | initial concentration |

C_{n} | = | 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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