proposal_sample

Selected Topics for final proposal

1 automotive industry

1) antilock braking system

2) vehicle suspension

2 energy

3) fuel cell

4) heating, ventilating and air conditioning(HVAC)

5) High voltage DC (HVDC) transmission systems

6) energy and comfort management in a building environment

7) solar air conditioning plant

8) solar collector field（吕庆）

9) solar cooling

10) power system

11) greenhouse

3 flight control

12)

4 mechanical electronics

13. electro-hydraulic test machine

14. Hard-Disk Drive

15. induction motor

16. DC Motor

17. piezo-positioning system

18. DC-DC power converter

19. precision machine tool drive

5 process control

20) CSTR (Continuous Stirred Tank Reactor)

21) distillation column control ( 温莲芹)

22) fed-batch biological reactors

23) heating process

24) industrial oil-cooling process

25) PH neutralization reaction

26) cascaded water tank

27) Surge vessel level

6 medical

28) hyperglycaemia

29) artificial_heart

30) blood glucose levels

7 robotics

31) mobile robot

32) robot manipulator

Sample proposal

Adaptive control of continuously stirred tank reactor (CSTR)

Name

(Address/Email)

1. Background

(Short introduction similar to the below should be included in the proposal, no more than 1 pages, font should be10 pt or songti/5)

The most important unit operation in a chemical process is generally a chemical reactor. Chemical reactions are either exothermic (release energy) or endothermic (require energy input) and therefore require that energy either be removed or added to the reactor for a constant temperature to be maintained. Exothermic reactions are the most interesting systems to study because of potential safety problems (rapid increases in temperature, sometimes called "ignition" behavior) and the possibility of exotic behavior such as multiple steady-states (for the same value of the input variable there may be several possible values of the output variable).

In this module we consider a perfectly mixed, continuously stirred tank reactor (CSTR), shown in Figure 1. The case of a single, first-order exothermic irreversible reaction, A --> B. We will show that very interesting behavior that can arise in such a simple system.

In Figure 1 we see that a fluid stream is continuously fed to the reactor and another fluid stream is continuously removed from the reactor. Since the reactor is perfectly mixed, the exit stream has the same concentration and temperature as the reactor fluide. Notice that a jacket surrounding the reactor also has feed and exit streams. The jacket is assumed to be perfectly mixed and at a lower temperature than the reactor. Energy then passes through the reactor walls into the jacket, removed the heat generated by reaction.

There are many examples of reactors in industry similar to this one. Examples include various types of polymerization reactors, which produce polymers that are used in plastic products such as polystyrene coolers or plastic bottles. The industrial reactors typically have more complicated kinetics than we study in this module, but the characteristic behavior is similar.

2. The Modeling Equations of the process

(The model should be nonlinear state space model, not less than two-order. The detailed stated here)

2.1 Statements of Parameters and Variables

(The parameters and variables that will appear in the modeling equations are listed below for convenience. The real values of parameters used in the process model are also listed here).

2.2 The physical theory for modeling

(The detailed stated here)

2.3 Nonlinear state space model

(The detailed stated here)

2.4 linearized State space model

(By approximated linearization technique about the equilibrium point, the linearized state space model of the original process can be easily conducted as follows: The detailed stated here)

2.5 Input-output model of linearized model

(By selecting appreciate input/output, to obtain the continuous/discrete transferfunction model . The detailed stated here)

3 Adaptive control design

(The procedure is divided into three parts: The detailed stated here)

3.1 model reference adaptive control design

(The detailed stated here)

3.2 self-tuing control design

(The detailed stated here)

3.3 nonlinear adaptive control design (one of parameterized nonlinear adaptive control,NN-based, Fuzzy-based)

(The detailed stated here)

4 Simulation results

(Brief view of the simulation procedure and the results figures. The values of simulation parameters and figures should be listed as appendex)

5. Reference (more than 5 international Journal papers or books)

Appendex A

Figure 1. Continuous Stirred Tank Reactor with Cooling Jacket

Requirement:

1) the reports like the sample (at least 10 A4 pages, not including the

appendixes )

2) complte simulation codes

additional reading material(not complete):

1. J.P. Corriou, Process control theory and application. Springer, 2004.

2. B.W.Bequette, Process control modeling design and simulation. Pretice

Hall,2003.

3. P. E. Rutquist, and Marcus M. Edvall, PROPT - Matlab Optimal Control

Software.

4. 李果，车辆防抱死制动控制理论与应用。国防工业出版社，2009年8月。