Chestermiller said:
Please tell us your rationale for arriving at these conclusions. Also, let's see the charts.
I just realized that I can get the specific enthalpy of stream S at 3.5 bar, by interpolating from 3.4 bar to 3.6 bar from from this table:
Table1: Properties of saturated steam: Pressure table
For stream F, I can obtain the specific enthalpy from these charts:
Chart1: Enthalpy of NaOH solution given mixture boiling temperature and mass fraction.
Chart2: Boiling temperature of an aqueous solution of NaOH given the mass fraction and temperature of the boiling water.
For streams V1 and V2, I assumed that the temperature of the steam is 100 degC, or assume that the pressure is the same as the evaporator (50kPa) so I can find it from the literature values, though I'm not sure if my assumption is valid.
For streams F1 and F2, the specific enthalpies can't be found because we don't know how much of steam is evaporated and so we don't know the w/w% of NaOH solution in these streams.
However, can the specific enthalpies of streams C1, C2 be found? The temperature and pressure of these streams are not known so I'm guessing we can't unless we assume the pressure of C1 is 50kPa, but I'm not sure if this assumption is valid.