Parameter | Value | Units |

Natural gas energy input | 10,595,598 | Btu/hr |

Electrical power output | 944 | KW |

3,221,062 | Btu/hr | |

Net electrical efficiency | 30.4% | - |

Exhaust energy output | 6,713,000 | Btu/hr |

Thermal energy transferred into recycled brine | 3,894,725 | Btu/hr |

Temperature of exhaust entering HE (T | 579 | ˚F |

Temperature of exhaust leaving HE (T | 280 | ˚F |

Temperature of recycled brin entering HE | 170 | ˚F |

Temperature of recycled brine leaving HE | 190.4 | ˚F |

Net thermal efficiency | 36.8% | - |

Overall plant efficiency | 67.2% | - |

Mass flow rate of seawater intake (M | 205,292.20 | lb/hr |

Temperature of seawater intake (T | 68 | ˚F |

Mass flow rate of cooling seawater (M | 166,530.36 | lb/hr |

Temperature of cooling seawater (T | 68 | ˚F |

Mass flow rate of recycled brine (M | 205,292.20 | lb/hr |

Top brine temperature (TBT) | 190.4 | ˚F |

Salinity of recycled brine―first pass (X | 64,481 | ppm |

Mass flow rate of brine blowdown (M | 19,016.07 | lb/hr |

Temperature of brine blowdown (T | 88.4 | ˚F |

Mass flow rate of distillate product (M | 19,745.76 | lb/hr |

39.51 | GPM | |

56,891 | gal/day | |

Salinity of brine blowdown (X | 71,343 | ppm |

Evaporation flux per unit surface area (r | 0.09879 | (lb/hr∙ft |

Estimated average wind speed (V | 7.0 | mph |

Required surface area | 4.42 | acres |

Salt produced | 4.07 | ton/day |