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Available fuel：Nature gas, methanol, liquid propane gas, diesel, heavy oil, light oil, crude oil, etc.
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We have a steam genereting facilty using process heat. The condenser is a vertical condenser with process vapours on tube side and boiler feed water on shell side. The outlet of the shell side is a two phase flow. Pipe thickness reduction of the shell side outlet pipe is observed for last couple of years.
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• Only slight change in water temp through pump • The steam generator consists of boiler (two-phase heat transfer) and superheater • Turbine outlet is high-quality steam • Condenser is cooled by water (eg. lake, river, cooling tower) or by air (when water is Cycle
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Steam with a temperature equal to the boiling point at that pressure is known as dry saturated steam. However, to produce dry steam in an industrial boiler designed to produce saturated steam is rarely possible, and the steam will usually contain droplets of water.
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Problem •Liquid water is fed to a boiler at 23 C under a pressure of 10 bar, and is converted at constant pressure to saturated steam. •Calculate Δhfor this process and the heat input required for producing 15,000 m3/h of steam at the exit conditions. •Assume that
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Steam with a temperature equal to the boiling point at that pressure is known as dry saturated steam. However, to produce dry steam in an industrial boiler designed to produce saturated steam is rarely possible, and the steam will usually contain droplets of water.
Get price
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