o) A two stage chemostate system is used for production of se 3 ry metabolite. The volume of each reactor is 2 m'...
o) A two stage chemostate system is used for production of se 3 ry metabolite. The volume of each reactor is 2 m'; the flow rate of feed is 200 ocurs in the both ractors but the scecond reactor is used for L/h. Mycelial growth for product synthesis. The concentration of substrate in the feed is 20 g/1. Kinetic and yield parameters for the organisms are: Yxs = 0.5 kg/kg Ks 1.0 kg/m Hm 0.12/h ms = 0.025 kg/kg-h p 0.16kg/kg-h Yps 0.85kg/kg Assume that product synthesis is negligible in the first reactor. i. Determine the cell concentration entering the second reactor. ii. What is the final concentration of the product?
o) A two stage chemostate system is used for production of se 3 ry metabolite. The volume of each reactor is 2 m'; the flow rate of feed is 200 ocurs in the both ractors but the scecond reactor is used for L/h. Mycelial growth for product synthesis. The concentration of substrate in the feed is 20 g/1. Kinetic and yield parameters for the organisms are: Yxs = 0.5 kg/kg Ks 1.0 kg/m Hm 0.12/h ms = 0.025 kg/kg-h p 0.16kg/kg-h Yps 0.85kg/kg Assume that product synthesis is negligible in the first reactor. i. Determine the cell concentration entering the second reactor. ii. What is the final concentration of the product?