Stream V-30 L/min CA Mixing tee Stream 1 C, 1. V=10 L/min V=150L CM Stream 2 CL V20 L/min To reactor Heater The process

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Stream V 30 L Min Ca Mixing Tee Stream 1 C 1 V 10 L Min V 150l Cm Stream 2 Cl V20 L Min To Reactor Heater The Process 1 (33.82 KiB) Viewed 14 times

Stream V-30 L/min CA Mixing tee Stream 1 C, 1. V=10 L/min V=150L CM Stream 2 CL V20 L/min To reactor Heater The process is running along at steady state. The concentration of Ain stream 1 is 1 g/L and in stream 2 is 4 g/L. At 3:00 P.M. the shift changes at the plant. The new operator on our unit misreads the flowmeters for the process and switches the flow rates of the two streams. Stream 1 is switched to 20 L/min, and stream 2 is switched to 10 L/min. At 3:30 PM. the shift supervisor hurries to the control room to determine the source of the problem now being experiencing with the reactor. 1. What was the net result of the operator's error on the concentration feed to the reactor? [1. Mathematical and scientific terms, 2. Theory in Engineering problems] 2. Given that the residence time of the heating vessel (Volume of tank/ Outlet flowrate) is 5 min. Predict the behaviour of this part of the process since the shift and the unfortunate error by the operator [1. Mathematical methods. 2. Calculations A] 3. Graphically illustrate the outlet concentration from reactor as a function of time [Statistical analysis] 4. Determine the steady state heat input required from the heater to the heating vessel [Calculations B] 5. Determine the transfer function of the reactor tank system that relates the output to the input after the error has occurred. Given that a reversible reaction occurs: A - B [1. Mathematical methods, 2. Calculations]