An ESP was designed to treat 5500 m3/mm of flue gas from a coal combustion unit and achieve a 98,5% PM removal efficiency. A certain drift velocity was assumed. The unit was built with exactly the collect ion. area called for in the design, but by the time the unit was started up, the actual flow rate had increased to 5900 m3/min, and the actual efficiency was really 98,5%,. Was the actual drift velocity the same as had been assumed? Prove your answer mathematically.
An ESP was designed to treat 5500 m3/mm of flue gas from a coal combustion unit and achieve a 98,5% PM removal efficiency. A certain drift velocity was assumed. The unit was built with exactly the collect ion. area called for in the design, but by the time the unit was started up, the actual flow rate had increased to 5900 m3/min, and the actual efficiency was really 98,5%,. Was the actual drift velocity the same as had been assumed? Prove your answer mathematically.
Chapter2: Loads On Structures
Section: Chapter Questions
Problem 1P
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An ESP was designed to treat 5500 m3/mm of flue gas from a coal combustion unit and achieve a 98,5% PM removal efficiency. A certain drift velocity was assumed. The unit was built with exactly the collect ion. area called for in the design, but by the time the unit was started up, the actual flow rate had increased to 5900 m3/min, and the actual efficiency was really 98,5%,. Was the actual drift velocity the same as had been assumed? Prove
your answer mathematically.
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