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Introduction

This chapter is from the book

Student Exercises

  1. Discuss the following problems (a–h) in the context of control:

    1. Identify control objectives;

    2. Identify input variables and classify as (a) manipulated or (b) disturbance;

    3. Identify output variables and classify these as (a) measured or (b) unmeasured;

    4. Identify constraints and classify as (a) hard or (b) soft;

    5. Identify operating characteristics and classify as (a) continuous, (b) batch, or (c) semicontinuous (or semibatch);

    6. Discuss safety, environmental, and economic considerations;

    7. Discuss the types of control (feedforward or feedback).

    Measurements and manipulated variables can vary continuously or may be sampled discretely. Select from the following:

    1. Driving a car

    2. One of your favorite activities (skiing, basketball, making a cappuccino, etc.)

    3. A stirred tank heater

    4. Beer fermentation

    5. An activated sludge process

    6. A household thermostat

    7. Air traffic control

    8. Taking a shower, assuming separate hot and cold water valves (this problem is also discussed in the supplemental material)

  2. Literature Review. The process control research literature can be challenging to read, with unique notations and rigorous mathematical analyses. Find a paper from one of the magazines or journals listed in Section 1.5 that you would like to understand by the time you have completed this textbook. You will find many articles to choose from, so use some of the following criteria for your selection:

    • The process is interesting to you (do not choose mainly a theory paper)

    • The modeling equations and parameters are in the paper (make certain the equations are ordinary differential equations and not partial differential equations)

    • There are plots that you can verify (eventually) through simulation (the plots should be based on simulation results)

    • The control algorithm is clearly written

    • The objectives of the paper are reasonably clear to you

    Provide the following:

    1. A short (one paragraph) summary of the overall objectives of the paper; why are you interested in the paper?

    2. A short list of words and concepts in the paper that are familiar to you.

    Suggested Topics (choose one):

    1. Fluid catalytic cracking unit (FCCU)—petroleum refining

    2. Reactive ion etching—semiconductor manufacturing

    3. Rotary lime kiln—pulp and paper manufacturing

    4. Continuous drug infusion—biomedical engineering and anesthesia

    5. Anaerobic digester—waste treatment

    6. Distillation—petrochemical and many other industries

    7. Polymerization reactor—plastics

    8. pH—waste treatment

    9. Beer production—food and beverage

    10. Paper machine headbox—pulp and paper manufacturing

    11. Batch chemical reactor—pharmaceutical production

    12. Automated insulin delivery (closed-loop artificial pancreas) for individuals with type 1 diabetes. See Figure 1-8 and Module 12.

  3. Instrumentation Search. Select one of the following measurement devices and use Internet resources to learn more about it. Determine what types of signals are input to or output from the device. For flow meters, what range of flow rates can be handled by a particular flow meter model?

    1. Vortex-shedding flow meters

    2. Orifice-plate flow meters

    3. Mass flow meters

    4. Thermocouple-based temperature measurements

    5. Differential pressure (delta P) measurements

    6. Control valves

    7. pH

    8. Continuous glucose monitors (CGM) to measure blood glucose level

  4. Work through Module 1: Introduction to MATLAB.

  5. Consider Example 1.1, the liquid surge vessel, which assumed that the outlet stream flowrate was manipulated. Now, perform a complete analysis assuming that the inlet stream flowrate is manipulated.

    1. Draw the instrumentation diagram for this problem.

    2. Should the control valve on the inlet stream be fail-open or fail-closed? Why?

    3. Draw the feedback block diagram for this problem.

    4. Develop the instrumentation diagram for combined feedforward and feedback control for this problem.

  6. A process furnace heats a process stream from near ambient temperature to a desired temperature of 300°C. The process stream outlet temperature is regulated by manipulating the flow rate of fuel gas to the furnace, as shown in this figure:

    1. Discuss the objectives of this control strategy.

    2. What is the measured output?

    3. What is the manipulated input?

    4. What are possible disturbances?

    5. Is this a continuous or batch process?

    6. Is this a feedforward or feedback controller?

    7. Should the control valve fail-open or fail-closed? For the strategy you chose, is the valve gain positive or negative? Why?

    8. Discuss safety, environmental, and economic issues.

    9. Draw the control block schematic diagram and label all signals and blocks on the diagram.

  7. A fluid catalytic cracking unit (FCCU) produces a significant portion of the gasoline produced by a typical petroleum refinery. A typical FCCU processes 30,000 Bbl/day (iequ26-01.jpg) of heavy gas oil from a crude oil distillation unit, producing roughly 15,000 Bbl/day of gasoline, along with streams of other components. The value of gasoline alone produced by this unit is on the order off $500,000/day, so any improvement in yield and energy consumption owing to improved control can have a significant economic impact.

    Question: A control system revamp for a 30,000 Bbl/day FCCU is estimated to cost $2 million. It is expected that the implementation of advanced control schemes will result in an economic increase of 2% in the value of products produced. Based on the value of gasoline alone, how many days will it take to pay back the control system investment?

  8. Furnaces are often used to heat process streams to temperatures above 400°F. A typical fired furnace may have a heat duty of iequ27-01.jpg Btu/hour, requiring roughly 1667 scfm (standard cubic feet per minute) of natural gas (methane has a fuel value of approximately 1000 Btu/scf). The cost of this fuel gas is on the order of $5/1000 scf, yielding an annual fuel cost of $4.4 million/year. Excess combustion air is needed to assure complete combustion; however, too much excess air wastes energy (the heated air simply goes out the exhaust stack). Too little excess air leads to incomplete combustion, wasting energy and polluting the atmosphere with unburned hydrocarbons. It is important, then, to deliver an optimum amount of combustion air to the furnace. With the large flow rates and high temperatures involved, maintaining safe operation is also very important. The control system must be designed so that excess combustion air is maintained, no matter what is happening to the fuel gas flow rate. A fired furnace control system clearly needs to satisfy safety, environmental, and economic criteria.

    Question: An advanced control scheme is estimated to save 2% in energy costs, for a fired furnace with a heat duty of iequ27-01.jpg Btu/hour. If it is desired to have a 2-year payback period on this control system investment, what is the maximum investment allowable?

  9. Consider the surge vessel process in Example 1.3. If the steady-state volume is 500 liters, and the steady-state inlet and outlet flow rates are 50 liters/minute, find how the liquid volume varies with time if the inlet flow rate is iequ27-02.jpg, while the outlet flow rate remains constant at 50 liters/minute.

  10. The human body is composed of many innate feedback and feedforward control loops. For example, insulin is a hormone produced by the pancreas to regulate the blood glucose concentration. The pancreas in an individual with type 1 (insulin dependent) diabetes has lost the ability to produce significant insulin. This person must monitor her/his blood glucose (blood glucose strips have been on the market for years) and administer insulin injections several times per day. It is particularly important to use knowledge of the meal carbohydrates to determine the amount of insulin necessary to compensate for the carbohydrates. There are short- and long-term risks associated with the over- and under-dosing of insulin. If too much insulin is injected, there is a short-term risk of hypoglycemia (low blood sugar), which can lead to dizziness, a coma, and even death if hypoglycemia occurs for an extended period of time. On the other hand, under-dosing insulin can lead to hyperglycemia (high blood sugar); higher average blood glucose levels are known to result in greater risk of retinal and other diseases.

    1. Discuss the actions taken by an individual with type 1 diabetes in terms of the formulation of a control problem. State the objectives and list all variables, etc.

    2. It is desirable to form an automated closed-loop system, sometimes called a closed-loop artificial pancreas, using a continuous blood glucose measurement and a continuous insulin infusion pump. Draw a “process and instrumentation” diagram (similar to Figure 1-8) and the corresponding control block diagram. Discuss whether a continuous insulin infusion pump should fail-closed or fail-open.

  11. Consider the following three heat exchanger control instrumentation diagrams. For each diagram (a, b, and c), the objective is to maintain a desired cold stream outlet temperature. Since the cold stream exiting the exchanger is fed to a reactor, it is important that the stream temperature never be substantially higher than the setpoint value. Please answer the two basic questions about each strategy, then the final question (part d).

    1. Basic cold stream temperature control strategy.

      Is the process gain relating the manipulated flow rate to the measured temperature positive or negative? Should the control valve be fail-open or fail-closed? Why?

    2. Temperature control using hot stream bypass strategy.

      Is the process gain relating the manipulated flow rate to the measured temperature positive or negative? Should the control valve be fail-open or fail-closed? Why?

    3. Temperature control using cold stream bypass strategy.

      Is the process gain relating the manipulated flow rate to the measured temperature positive or negative? Should the control valve be fail-open or fail-closed? Why?

    4. Which strategy (a, b, or c) will have the fastest dynamic behavior? Why?

  12. During surgery it is important for an anesthesiologist to regulate a patient’s blood pressure to a desired value. She does this by changing the infusion rate of vasoactive drugs to the patient. In addition to the effect of manipulated vasoactive drugs, blood pressure is affected by the level of anesthetic given to the patient. Discuss actions taken by an anesthesiologist in the context of feedback control. Sketch a control block diagram for an automated system that measures blood pressure and manipulates the infusion rate of a vasoactive drug.

  13. An aeration basin (a very large “vessel”) is used to continually treat a wastewater stream aerobically. A number of mechanical agitators at the surface can be used to “pump” air into the basin; these can be independently turned on or off to change the level of dissolved oxygen in the basin. The microbes that “eat” the waste function best in a small pH range. Acid and base stream flowrates into the basin can be manipulated. An analytical device that can measure the concentration of waste material in terms of BOD (biochemical oxygen demand) is placed in the outlet stream of the basin. The liquid level in the basin is relatively constant, since the effluent flows over a weir. The outlet flowrate can be estimated by the height of liquid over the weir. Provide a sketch of this process and discuss it in the context of a control problem, identifying objectives, disturbances, etc.

  14. A gas surge drum, shown below, is used to buffer the effect of gas flow between two operating units. It is important that the gas drum pressure be controlled not to exceed low and high pressure limits. Consider two possible scenarios: (a) the inlet flowrate (qi) is manipulated, and (b) the outlet flowrate (q) is manipulated. In each case, sketch the process and instrumentation diagram with a pressure sensor, controller, and control valve. Discuss whether the control valve should be fail-open or fail-closed.

    01un05.jpg
  15. Often chemical reactors must be heated or cooled, depending upon whether the reaction is endothermic or exothermic. Consider the temperature control strategy shown below, under two different scenarios: (a) an endothermic reaction, and (b) an exothermic reactor. For each case, discuss whether the jacket fluid is a hot or a cold stream. Also discuss whether the control valve should be designed to fail-open or fail-closed.

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