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Advanced Process Control
1- Transfer the model described in the paper into Simulink and find the steady state values
2- Draw the block flow diagram of the open and close loop system
3- Find the process response to unit step change in CAi while the other variables remain constant
4- Design a PI controller using Ziegler-Nichols tuning method. The ultimate gain should be determined using the Routh Array method. As Routh Array method requires the use of Pade approximation, the ultimate gain identified using this method should be taken as an estimate (initial guess). The actual ultimate gain and ultimate period should be found by performing closed-loop tests on the identified model (and not on the real plant).
1- Design a PI controller using Skogestad's IMC rules.
2- Using closed-loop simulations obtain and compare the responses of T and Ca for a positive unit step change in the Temperature when a PI controllers designed using ZN and IMC methods are implemented
Article - The Control of Non Isothermal CSTR Using Different Controller Strategies by Zahra'a F. Zuhwar
Need to get the information from the paper for non isothermal CSTR reactor and answer the questions from the separated attached file. (Use bode diagram to find the steady state values)
The oil is burned with 20.0% excess air, based on complete combustion of the carbon to CO2, the hydrogen to H2O, and the sulfur to SO2. The oil is burned completely, but 8% of the carbon forms CO. Calculate the molar composition of the stack gas.
Zirconium is one of the few metals that retains its structural integrity upon exposure to radiation. The fuel rods in most nuclear reactors therefore are often made of zirconium.
Important information about Chemicals for Indoor Concrete Flooring Explanations on high solids floor finish chemicals used on indoor concrete flooring
Calculate the work necessary to isothermally perform compression of 0.1 m^3 of gas in a piston with an external pressure increasing gradually from 1 to 16 bar.
A 95 turn square wire coil of area 0.040 m2 rotates about a vertical axis at 1730 rpm, as indicated in Figure P20.30. The horizontal component of the Earth's magnetic field at the location of the loop is 2.0 10-5 T.
The equilibrium constant should vary with temperature according to the relation Kp = ae-b/T use the results of part (b) to determine the values of a and b by a graphical curve-fitting procedure. [Suggestion: Use the spreadsheet program from part (..
You need to prepare an AUTOCAD file for Mechanical Drawing of Unit Operation, as per the SAMPLE Design - The Deliverables will be AUTOCAD file
A typical feed stream composition is 55% ethylene, 5% inserts, and 40% water. A typical product stream is 52.26% ethylene, 5.49% ethanol, 0.16% ether, 36.81% water, and 5.28% inserts. Calculate the selectivity of ethylene for ethanol and for ether..
For a given power source of 300 kW electrical output, a propellant mass of 6000 lbm, α = 450 W/kg, and a payload of 4000 lbm, determine the thrust, ideal velocity increment, and duration of powered flight for the following three cases
Is it possible to recover 70% of the ethane in the vapor by a single-stage flash at other conditions without losing more than 5% of nC4 to the vapor? Obtain K-values fromFigure.
Determine the maximum amount of work obtainable in a flow process from 1 kg of steam at 3000 kPa and 723.15 K (450°C) for surrounding conditions of 300 K and 101.33 kPa.
The feed is a saturated liquid at 330 kPa. The recovery of toluene in the distillate should be greater than 99%, and the recovery of ethylbenzene in the bottoms should be greater than 99%.
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