A flash type evaporator is designed to operate in 75°F sea water, if operated in 50°F sea water, __________.
• Flash-type evaporator operation depends on seawater (feedwater) temperature, vacuum (absolute pressure), and heating steam temperature • At lower feedwater temperatures, more heat is required to reach the same evaporation rate, affecting capacity and/or efficiency • Relationship between boiling point, absolute pressure, and temperature in a vacuum evaporator
• Compare how much additional heating is needed to raise 50°F seawater up to flashing temperature versus 75°F seawater under the same conditions • Think about which design variable is usually kept constant in service: the absolute pressure in the stages, or the heating steam conditions—and what that does to capacity • Ask yourself: in real shipboard practice, when seawater is colder than design, what operational symptom do engineers usually notice first about the evaporator’s output?
• Verify how a fixed absolute pressure in the flash stages sets the corresponding saturation (boiling) temperature • Check whether lowering feed temperature, while keeping stage pressure the same, makes each pound of distillate require more heat input, and how that affects tons/gallons per day output • Confirm whether changes in feed temperature directly change the absolute pressure, or mainly change rate of evaporation / production capacity
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