Please your solution include energy,mole,component and heat balances and please show your mathematical calculations. Also, can you draw a schematic diagram for this question's parallel feed evaporation. Thank you.

parallel feed triple effect evaporator is fed at 10000kg/h of an aqueous solution that contains mass \% solids. The temperature of the feed is 27C and the feed is split 60:20:20. The pecification of the final product is 30 mass % solids. Steam is available at 200kPa and the apour pressure in the third effect is 14kPa. The flowrate of steam is 2000kg/h. dditional information: a. The boiling point rise of the solution is negligible b. The heat transfer surfaces are the same in all three effects c. The heat capacity of the solution is 4.3kJ/kg.K and is constant over temperature and concentration ranges d. The heat of the solution is negligible e. The overall heat transfer coefficients are estimated as U1=4.45;U2=2.67 and U3=2.127kW/m2K f. Perform only one iteration g. As the feed enters as a cold stream the first effect requires more heat. Normally we need to adjust the temperature T1,T2,T3 proportionately. In this case, assume enough heat is available to heat up the cold stream; therefore, you don't need to do a temperature adjustment 3.1. Draw a schematic diagram to depict the evaporation process labelling all process streams and showing all information required for the system. 3.2. Determine the flow rates of vapour and liquid streams for each evaporator. 3.3. Determine the overall steam economy. 3.4. Determine the area of each effect. parallel feed triple effect evaporator is fed at 10000kg/h of an aqueous solution that contains mass \% solids. The temperature of the feed is 27C and the feed is split 60:20:20. The pecification of the final product is 30 mass % solids. Steam is available at 200kPa and the apour pressure in the third effect is 14kPa. The flowrate of steam is 2000kg/h. dditional information: a. The boiling point rise of the solution is negligible b. The heat transfer surfaces are the same in all three effects c. The heat capacity of the solution is 4.3kJ/kg.K and is constant over temperature and concentration ranges d. The heat of the solution is negligible e. The overall heat transfer coefficients are estimated as U1=4.45;U2=2.67 and U3=2.127kW/m2K f. Perform only one iteration g. As the feed enters as a cold stream the first effect requires more heat. Normally we need to adjust the temperature T1,T2,T3 proportionately. In this case, assume enough heat is available to heat up the cold stream; therefore, you don't need to do a temperature adjustment 3.1. Draw a schematic diagram to depict the evaporation process labelling all process streams and showing all information required for the system. 3.2. Determine the flow rates of vapour and liquid streams for each evaporator. 3.3. Determine the overall steam economy. 3.4. Determine the area of each effect