- 2 A Tray Tower Is To Be Designed Fou Stripping Ammonia A From Its Solution In Liquid Water C The Stripping Tray To 1 (29.34 KiB) Viewed 62 times
2. A tray tower is to be designed fou(stripping ammonia (A) from its solution in liquid water (C). The stripping tray to
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2. A tray tower is to be designed fou(stripping ammonia (A) from its solution in liquid water (C). The stripping tray to
2. A tray tower is to be designed fou(stripping ammonia (A) from its solution in liquid water (C). The stripping tray tower must process the liquád mixture containing (8% ammonia by mass, at a feed rate of 100 kg/min. A downstream unit receiving the liquid effluent of the desorber demands that the water delivered to it must not exceed 1% ammonia by mass. Fresh steam (B) is used as the inert stripping gas at a rate of 10% more than the minimum steam rate in kg/min. The ammonia in water equilibrium is given by y* = 1.7x". Estimate the number of ideal trays using the McCabe-Thiele graphical procedure (see the equilibrium Figure 1 on page 3). =
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