The system shown below is a steady-state continuous separation process. Stream 3 40 g A/s Stream...

 

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The system shown below is a steady-state continuous separation process. Stream 3 40 g A/s Stream 5 F5 g's Stream 7 F7g/s 0.2 g A/g Stream 1 x7 g A/g x5 y7 gB/g F1 g/s y5 g C/g 0.1 g C/g 0.50 g A/g 0.40 g B/g Unit 1 Stream 4 Unit 2 0.10 g C/g Stream 2 F2 g/s x2 gA/g 0.25 gB/g y2 g C/g 0.4 g Dig Unit 3 Stream 6 F6BgB/s F6C g C/s Stream 8 F8 g's x8 gB/g F6Dg D/s 0.70 g Dig y8 gC/g a. Finish labelling the diagram b. number of unknowns number of independent mass balance equations c. Using information from the diagram, write a balance for component A on unit 1 d. Using information from the diagram, write an overall balance for component A e. If 80.0% of the component A in stream 1 is recovered in stream 3. What will be the value of F1? f. If FS has a value of 80, what will be the value of F2? g. Using information from the diagram, write a total mass balance for the overall system h. Write a total mass balance for the unit 1 and unit 2 combined The system shown below is a steady-state continuous separation process. Stream 3 40 g A/s Stream 5 F5 g's Stream 7 F7g/s 0.2 g A/g Stream 1 x7 g A/g x5 y7 gB/g F1 g/s y5 g C/g 0.1 g C/g 0.50 g A/g 0.40 g B/g Unit 1 Stream 4 Unit 2 0.10 g C/g Stream 2 F2 g/s x2 gA/g 0.25 gB/g y2 g C/g 0.4 g Dig Unit 3 Stream 6 F6BgB/s F6C g C/s Stream 8 F8 g's x8 gB/g F6Dg D/s 0.70 g Dig y8 gC/g a. Finish labelling the diagram b. number of unknowns number of independent mass balance equations c. Using information from the diagram, write a balance for component A on unit 1 d. Using information from the diagram, write an overall balance for component A e. If 80.0% of the component A in stream 1 is recovered in stream 3. What will be the value of F1? f. If FS has a value of 80, what will be the value of F2? g. Using information from the diagram, write a total mass balance for the overall system h. Write a total mass balance for the unit 1 and unit 2 combined