Chemical Engineering Or Processor Operator

This assignment will take the form of a Zoom video. The video will consist of six parts; each involving a run of the simulator starting from the same steady state conditions. After starting each run, a different malfunction will be introduced. As the malfunction is progressively affecting the performance of the process you will observe both the graphics display and the historical trends and make observations as to exactly how the malfunction is affecting the ALL of the process values and systems. You should prepare at least one typed page for each malfunction run. On each page, identify each malfunction before describing your observations. Combine all pages together in a single Word document with your name, class and date and assignment title at the top of the first page. Submit that assignment under this page to complete this exercise. (See Scoring Rubric in this assignment for grading criteria)


1) Completion of each exercise will be worth up to 30 points for a total of 6 x 30 = 180 points.

2) Each page of observations for each malfunction should be approximately 1 page in length to avoid losing points. There should be sufficient observations from the graphics display and the historical trends comparison to satisfactorily meet this requirement. To meet this requirement you can explain why individual curves respond the way they do in response to the malfunction.

3) Your responses must be clear and understandable

ASSIGNMENT   Is due Today, Monday dec 7th. 11:59pm.

Tank, Pumps and a Heat Exchanger: Design Operating Conditions

The instrument setpoints at design operating conditions are given below:

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// PID Instrument SP Data

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# Tag


Tag Description SP Eng


1 FC425 Tank, T400 Supply Water Flow 125.00 MLB/HR

2 FC440 Pump Minimum Flow 50.00 MLB/HR

3 FC460 Pump Discharge to Battery Limit Flow 125.00 MLB/HR

4 LC430 Tank, T400 Level 50.00 PCT

5 TC430 Tank, T400 Temperature 140.00 DEG F

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// AI Instrument SP Data

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# Tag


Tag Description SP Eng


1 FI400 E400 Cold Water Supply Flow 250.00 MLB/HR

2 FI420 E400 Hot Water Supply Flow 125.00 MLB/HR

3 LI431 Tank, T400 Level 50.00 PCT

4 PI400 E400 Cold Water Supply Pressure 60.00 PSIG

5 PI410 E400 Cold Water Return Pressure 15.00 PSIG

6 PI420 E400 Hot Water Supply Pressure 75.00 PSIG

7 PI425 E400 Tube Outlet Pressure 60.00 PSIG

8 PI430 Tank, T400 Pressure 0.00 PSIG

9 PI440 Pump, P440 Discharge Pressure 150.00 PSIG

10 PI450 Pump, P450 Discharge Pressure 150.00 PSIG

11 PI460 FC460 Downstream Pressure 75.00 PSIG

12 TI400 E400 Cold Water Supply Temperature 80.00 DEG F

13 TI410 E400 Cold Water Return Temperature 100.00 DEG F

14 TI420 E400 Hot Water Supply Temperature 180.00 DEG F

15 TI425 Tank, T400 Supply Water Temperature 140.00 DEG F

16 TI440 Pump, P440 Discharge Temperature 141.00 DEG F

17 TI450 Pump, P450 Discharge Temperature 141.00 DEG F

18 XI440 P440 Motor Current 50.00 AMPS

19 XI450 P450 Motor Current 50.00 AMPS

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