1. An evaporation-crystallization process is used to obtain solid potassium sulphate from an aqueous solution of this salt. Fresh feed to the process 18.6 wt% K2SO4. The wet filter cake consists of solid K2SO4 crystals and a 40 wt% K2SO4 solution, in a ratio 10 kg crystals/kg solution. The filtrate also a 40 % solution, is recycled to join the fresh feed. Of the water feed to the evaporator, 42.66 % is evaporated. The evaporator has a maximum capacity of 155 kg water evaporated/min. Calculate:
Rate at which fresh feed must be supplied for the maximum evaporation rate in the evaporator
The ratio kg recycled / kg fresh feed
Maximum production rate of solid if the wet filter cake is later dried completely.
Water to be evaporated= 150 kg this corresponds to 42.66% water. So total water entering the evaporator= 150/0.4266=363.38 kg
Total water entering the evaporator= 363.38 kg
Let F= Feed and R= Recycle
Water entering evaporator is through recycle and through Fresh feed
F*(1-0.186)+R*0.6= 363.38 kg
F*0.814+R*0.6= 363.38 (1)
Solids entering Crystallizer F*0.186+R*0.4
If R is Recyle solution , 10R = Crystals
F*0.186+R*0.4= 10R+R*0.4
F*0.186= 10R (2)
From 1 , 10*0.814*R+R*0.6= 363.38
8.74R= 363.38 R= 41.58
F= 10*41.58/0.186=2235.48 kg
Crystals from the system = 10*R= 10*41.58= 415.8 kg
R/F= 41.58/2235.48=0.0186
When t he cake is dried separately
Amount of cake in the solution = 41.58*0.4/100=0.16 kg
Total solids = 415.8+0.16= 415.96 kg
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