ROTARY VACUUM FILTER
Mud = 42.44920 tons/hr % Sucrose = 2% Temperature = 85 ˚C
Filtrate % Sucrose
Filter Cake = 11.2 tons/hr % Sucrose = 1.5% Material Balance Mud = Filter cake + Filtrate 42.44920 = 11.2 + Filtrate Filtrate = 31.2492
Component Mass Balance Sucrose Balance:
Mx m = Filter Cake (x c ) + Filtrate(x f ) 42.44920(0.02) = 11.2(0.015) + 31.2492(x f ) x f = 0.0218
FLASH TANK Milk of lime
F = 31.2492 tons/hr Tf = 220oF
Incondensable Gas
FLASH TANK Lime Juice Tp = 213oF
Assuming negligible amount of incondensable gas, Feed + Milk of Lime = Limed Juice + Incondensable gas Feed + Milk of Lime = Limed Juice
Amount of Milk of Lime used: CaO used: 31.2492
tons 0.5 kg CaO kg CaO × = 15.6246 hr 1ton cane hr
Weight of Lime: 15.6246
kg CaO 1kg Lime kg Lime × = 18.3818 hr 0.85 kg CaO hr
Milk of Lime: 18.3818
kg Lime 1kg solution 1ton tons of milk lime × × = 0.3342 hr 0.055 kg solid lime 1000 kg hr
Feed + Milk of Lime = Limed Juice tons tons 31.2492 + 0.3342 = Limed Juice hr hr tons Limed Juice = 31.5834 hr
CLARIFIER
Limed Juice=31.5834 tons/hr 14 Brix Tf = 213oF
CLARIFIER
Mud (2% sucrose)
Clarified Juice 16 Brix Tf = 213oF
Material Balance Limed Juice = Filter Cake + Clarified Juice
Component Mass Balance Fx f = Filter Cake(0.02) + Px p tons 31.5834 (0.14) = Filter Cake 0.02 + 0.16P hr tons Clarified Juice, P = 27.0715 hr tons Mud = 4.5119 hr tons Sucrose(2%of mud) = 0.090238 hr