Interpretation:
The given statements are to be stated as true or false along with the appropriate explanation.
Concept introduction:
Two types of the control system to control the dynamics of a process are:
1. Feedback control system.
2. Feedforward control system.
The feedback control system considers the output of the system and then compares it with the desired value to adjust the measured value to provide accurate results. Whereas in the feedforward control system, disturbances are taken into account beforehand and they are rectified to control it from deviating from the desired set point.
Answer to Problem 1.1E
(a) True
(b) True
(c) True
(d) False
(e) True
Explanation of Solution
(a)
In feedback control systems, controlled variables are measured and are compared with the desired values which are then controlled accordingly by adjusting the manipulated variables.In the feedforward control systems, disturbance variables are measured and controlled before it deviates from the set point.
Therefore, in both the control systems, measured variables are required. Thus, the given statement is true.
(b)
In feedforward control systems, necessary corrective measures are taken before the controlled variables are affected by the disturbances so that the controlled variables have not deviated from the desired set point.
Therefore, in this system, the measured variable is the one to be controlled. Thus, the given statement is true.
(c)
When the process model which is used to control the system is designed perfectly, the feedback control can theoretically provide perfect control on the measured variable. The controlled variable is measured and compared with the desired value, which is then manipulated to control the system, accordingly, providing the perfect control for the process.
Thus, the given statement is true.
(e)
As compared to the feedforward control system, the feedback system rectifies the disturbance in the measured value of the controlled variable regardless of the source of error and provides correct value as the set point or the desired value. It is more accurate than the feedforward system where only known sources of errors can be solved. Thus, the given statement that the feedback control system is superior to the feedforward control system is true.
(d)
In the feedforward control system, necessary corrective measures are taken before the controlled variables are affected by the disturbances so that the controlled variables have not deviated from the desired set point. This system has several disadvantages such as:
1. The measurement of the disturbance variables should be done accurately.
2. The disturbances which are not measured are not rectified.
3. A process model is necessary for this control system.
Thus, perfect control of the process cannot be achieved for the imperfect process model having an unknown type of disturbances.
Therefore, the given statement is false.
Want to see more full solutions like this?
- 9.3. An ideal PD controller has the transfer function P Ke (TDs + 1) E An actual PD controller had the transfer function P = Ke E TDS +1 (TDIẞ)s +1 where ẞis a large constant in an industrial controller. If a unit-step change in error is introduced into a controller having the second transfer function, show that P(1) = Kc (1 + Ae˜¯BD) where A is a function of ẞwhich you are to determine. For ẞ=5 and K = 0.5, plot P(t) versus tl tp. As ẞ, show that the unit-step response approaches that for the ideal controller.arrow_forward9.1. A pneumatic PI temperature controller has an output pressure of 10 psig when the set point and process temperature coincide. The set point is suddenly increased by 10°F (i.e., a step change in error is introduced), and the following data are obtained: Time, s psig 0- 10 0+ 8 20 7 60 90 5 3.5 Determine the actual gain (psig per degree Fahrenheit) and the integral time.arrow_forward2. A unit-step change in error is introduced into a PID controller. If Ke TD = 0.5, plot the response of the controller P(t). = =10, 1, andarrow_forward
- A distribution of values is normal with a mean of 211 and a standard deviation of 50.4. Find the probability that a randomly selected value is between 59.8 and 155.6. P(59.8 X 155.6) = Enter your answer as a number accurate to 4 decimal places. Answers obtained using exact z-scores or z- scores rounded to 3 decimal places are accepted.arrow_forwardTopic: Production of propylene glycol from glycerol derived from palm oil. QUESTION:Estimate capital items, operating costs and economics of the plant. Finally, report the estimatedreturn.The Detailed Factorial Method with approximately 25% accuracy must be used for detailedeconomic evaluation.Plant lifetime is fixed at 15 years.1) Depreciation and TaxesCalculate the depreciation using a suitable method (e.g., straight-line, declining balance) andincorporate tax implications based on current tax laws applicable to chemical plants. Use following attached Process Flow Diagram as reference for this question.arrow_forwardTopic: Production of propylene glycol from glycerol derived from palm oil. QUESTION:Estimate capital items, operating costs and economics of the plant. Finally, report the estimatedreturn.The Detailed Factorial Method with approximately 25% accuracy must be used for detailedeconomic evaluation.Plant lifetime is fixed at 15 years.1) Revenue EstimationEstimate the annual revenue based on the production capacity, product selling price, and marketdemand. Groups should also consider potential market fluctuations. Use following attached Process Flow Diagram as reference for this question.arrow_forward
- Topic: Production of propylene glycol from glycerol derived from palm oil. QUESTION:Estimate capital items, operating costs and economics of the plant. Finally, report the estimatedreturn.The Detailed Factorial Method with approximately 25% accuracy must be used for detailedeconomic evaluation.Plant lifetime is fixed at 15 years.TASKS:1) Capital Cost EstimationProvide a detailed breakdown of the initial capital investment, including land, building,equipment, and installation costs. Include any assumptions made in the estimation. Use following attached Process Flow Diagram as reference for this question.arrow_forwardTopic: Production of propylene glycol from glycerol derived from palm oil. QUESTION:Estimate capital items, operating costs and economics of the plant. Finally, report the estimatedreturn.The Detailed Factorial Method with approximately 25% accuracy must be used for detailedeconomic evaluation.Plant lifetime is fixed at 15 years.1) Breakeven Year CalculationUsing the cash flow analysis, calculate the breakeven year when the cumulative cash inflowequals the initial investment. Groups should graphically represent the breakeven point. Use following attached Process Flow Diagram as reference for this question.arrow_forwardTopic: Production of propylene glycol from glycerol derived from palm oil. QUESTION:Estimate capital items, operating costs and economics of the plant. Finally, report the estimatedreturn.The Detailed Factorial Method with approximately 25% accuracy must be used for detailedeconomic evaluation.Plant lifetime is fixed at 15 years.1) Cash Flow AnalysisDevelop a projected cash flow statement for the first 10 years of plant operation, consideringall the costs and revenues. Include working capital, loans, and interest payments if applicable. Use following attached Process Flow Diagram as reference for this question.arrow_forward
- Topic: Production of propylene glycol from glycerol derived from palm oil.QUESTION:Estimate capital items, operating costs and economics of the plant. Finally, report the estimatedreturn.The Detailed Factorial Method with approximately 25% accuracy must be used for detailedeconomic evaluation.Plant lifetime is fixed at 15 years.1) Operational Cost AnalysisCalculate the yearly operational costs, including raw materials, labor, utilities, maintenance,and other recurring expenses. Provide a clear explanation of how these costs are derived. Use following attached Process Flow Diagram as reference for this question.arrow_forwardChemical Engineering Questionarrow_forwardA steam boiler or steam generator is a device used to produce steam by transferring heat to water. In our case, the combustion chamber is fueled with propane (C3H8) at a flowrate of 50.0 mol/h in an excess air of 50%. Assume that both propane and air are fed at 25ºC and the combustion gases leave the chamber at 200ºC. Pressure can be assumed to be atmospheric.* Determine: 1. The heat obtained assuming complete combustion. Compare the results using elements or compounds 2. The steam flowrate that could be generated if the heat is directed to obtain superheated steam at 2 bar and 160ºC from saturated liquid water at this pressure solvearrow_forward
- Introduction to Chemical Engineering Thermodynami...Chemical EngineeringISBN:9781259696527Author:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark SwihartPublisher:McGraw-Hill EducationElementary Principles of Chemical Processes, Bind...Chemical EngineeringISBN:9781118431221Author:Richard M. Felder, Ronald W. Rousseau, Lisa G. BullardPublisher:WILEYElements of Chemical Reaction Engineering (5th Ed...Chemical EngineeringISBN:9780133887518Author:H. Scott FoglerPublisher:Prentice Hall
- Industrial Plastics: Theory and ApplicationsChemical EngineeringISBN:9781285061238Author:Lokensgard, ErikPublisher:Delmar Cengage LearningUnit Operations of Chemical EngineeringChemical EngineeringISBN:9780072848236Author:Warren McCabe, Julian C. Smith, Peter HarriottPublisher:McGraw-Hill Companies, The