mixing constant (k)

= 0

= 0

fluid dynamic viscosity (μ)

= 0

= 0

newton-second/meter^2

revolution per second (n)

= 0

= 0

impeller diameter (D)

= 0

= 0

meter

power requirement (P)

= NOT CALCULATED

Select to solve for a different unknown

propeller and turbine mixers

power requirement (laminar flow) Reynolds number < 10 | |

mixing constant (laminar flow) | |

fluid dynamic viscosity | |

rotation speed revolutions per second (laminar flow) | |

impeller diameter (laminar flow) |

power requirement (turbulent flow) Reynolds number >10000 | |

mixing constant (turbulent flow) | |

fluid mass density | |

rotation speed revolutions per second (turbulent flow) | |

impeller diameter (turbulent flow) |

Reynolds number | |

impeller diameter | |

rotation speed revolutions per second | |

liquid mass density | |

fluid dynamic viscosity |

static mixers

dissipated power | |

specific weight water | |

flowrate | |

dissipated headloss |

pneumatic bubble mixers

power dissipated | |

volume of air at atmospheric pressure | |

discharge point air pressure |

power dissipated | |

volume of air at atmospheric pressure | |

discharge point air pressure |

References - Books:

George Tchobanoglous, Franklin L. Burton. 1991. Wastewater Engineering Treatment, Disposal and Reuse. McGraw Hill, Inc.

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