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It is desired to concentrate an incoming solution of 3 w t % brine ( solution of salt and water ) to 5 w t

It is desired to concentrate an incoming solution of 3wt% brine (solution of salt and water) to 5wt% before sending to a crystallizer using a series of evaporators as shown in the Figure 1. Water leaving each evaporator is collected together to form Stream 8. Each evaporator removes the same quantity (mass) of water from its inlet solution. Assuming a suitable basis calculate at steady state,
F'igure 1: vaporators in series
(a) The mass flow rate of the concentrated brine solution leaving evaporator 3(Stream 7)
(b) The mass flow rate of water exiting each evaporator and Stream 8
(c) The mass fraction of salt in the intermediate streams (Streams 3 and 5)
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