Within a process plant, a stream consisting of a mixture of components A and B (stream 1) is mixed with a stream of pure component B (Stream 2) in a process vessel called a mixer. Stream 1 is 50 mass%...


Within a process plant, a stream consisting of a mixture of<br>components A and B (stream 1) is mixed with a stream of pure<br>component B (Stream 2) in a process vessel called a mixer.<br>Stream 1 is 50 mass% B. The outlet stream of the mixer<br>(stream 3) is 40 mass% A. Stream 3 is fed into a separator<br>which brings the mixture to equilibrium at 70°C and 1atm.<br>Within the separator, the mixture forms two separate phases.<br>The less dense phase exits the separator in stream 4 and the<br>more dense phase exits the separator in stream 5. The<br>processes operate at steady state, and no reactions happen in<br>either process vessel. A process diagram is shown below, with<br>known compositions and flow rates labeled. A temperature-<br>composition diagram for mixtures of A and B at 1 atm is<br>available below.<br>a. What is the mass fraction of B in stream 4?<br>b. What is the total mass flow rate of the stream 4?<br>c. What is the mass flow rate of B in stream 4?<br>d. Write a mass balance equation for component B in the<br>mixer<br>e. What is the total mass of B entering the mixture every<br>hour in Stream 2<br>

Extracted text: Within a process plant, a stream consisting of a mixture of components A and B (stream 1) is mixed with a stream of pure component B (Stream 2) in a process vessel called a mixer. Stream 1 is 50 mass% B. The outlet stream of the mixer (stream 3) is 40 mass% A. Stream 3 is fed into a separator which brings the mixture to equilibrium at 70°C and 1atm. Within the separator, the mixture forms two separate phases. The less dense phase exits the separator in stream 4 and the more dense phase exits the separator in stream 5. The processes operate at steady state, and no reactions happen in either process vessel. A process diagram is shown below, with known compositions and flow rates labeled. A temperature- composition diagram for mixtures of A and B at 1 atm is available below. a. What is the mass fraction of B in stream 4? b. What is the total mass flow rate of the stream 4? c. What is the mass flow rate of B in stream 4? d. Write a mass balance equation for component B in the mixer e. What is the total mass of B entering the mixture every hour in Stream 2
Stream 4<br>Stream 1<br>8kg/h<br>50 mass% B<br>Stream 3<br>50 mass% A<br>SEPARATOR<br>WA3 = 0.4<br>70°C<br>WB3 = 0.6<br>1atm<br>MIXER<br>Stream 5<br>Stream 2<br>Pure B<br>flowchart<br>100<br>V<br>MA=10kg/kmol<br>MB=30kg/kmol<br>80<br>T(°C)<br>L+V<br>LB+V<br>60<br>LA<br>LB<br>La+LB<br>40<br>O 10 20 30 40 50 60 70 80 90 100<br>Mass Percent B<br>

Extracted text: Stream 4 Stream 1 8kg/h 50 mass% B Stream 3 50 mass% A SEPARATOR WA3 = 0.4 70°C WB3 = 0.6 1atm MIXER Stream 5 Stream 2 Pure B flowchart 100 V MA=10kg/kmol MB=30kg/kmol 80 T(°C) L+V LB+V 60 LA LB La+LB 40 O 10 20 30 40 50 60 70 80 90 100 Mass Percent B

Jun 10, 2022
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