Figure I shows the process and the known data. You are asked to calculate the compositions of every flow stream, and the traction of the sugar in the cane that is recovered. M, Sugar oce F. Cane 16% Sugar 25% Water 59% Pulp Oe warer L, water Crystallize 13% Sugar 14% Pulp 7670Ware K, 40% sugar J. watei Mill Screen Evaporator D, Bagasse 80% Pulp G, Solids 95% Pulp c*to Sugar b7o water Crystallize k=LA1000. Sugar 4K= 0+1000 k= a,500 b/nr L=1500 nr evoporator Sugar Hi 3.500 + I XH = 4(a,500) + O