1 / 24

Homework 2: Interacting Tank-in-Series System

Chapter 2. Examples of Dynamic Mathematical Models. Homework 2: Interacting Tank-in-Series System. Chapter 2. General Process Models. State Equations. A suitable model for a large class of continuous theoretical processes is a set of ordinary differential equations of the form:.

syshe
Download Presentation

Homework 2: Interacting Tank-in-Series System

An Image/Link below is provided (as is) to download presentation Download Policy: Content on the Website is provided to you AS IS for your information and personal use and may not be sold / licensed / shared on other websites without getting consent from its author. Content is provided to you AS IS for your information and personal use only. Download presentation by click this link. While downloading, if for some reason you are not able to download a presentation, the publisher may have deleted the file from their server. During download, if you can't get a presentation, the file might be deleted by the publisher.

E N D

Presentation Transcript


  1. Chapter 2 Examples of Dynamic Mathematical Models Homework 2: Interacting Tank-in-Series System

  2. Chapter 2 General Process Models State Equations • A suitable model for a large class of continuous theoretical processes is a set of ordinary differential equations of the form: t : Time variable x1,...,xn : State variables u1,...,um :Manipulated variables r1,...,rs :Disturbance, nonmanipulable variables f1,...,fn :Functions

  3. Chapter 2 General Process Models Output Equations • A model of process measurement can be written as a set of algebraic equations: t : Time variable x1,...,xn : State variables u1,...,um :Manipulated variables rm1,...,rmt :Disturbance, nonmanipulable variables at output y1,...,yr : Measurable output variables g1,...,gr :Functions

  4. Chapter 2 General Process Models State Equations in Vector Form • If the vectors of state variables x, manipulated variables u, disturbance variables r, and vectors of functions f are defined as: Then the set of state equatios can be written compactly as:

  5. Chapter 2 General Process Models Output Equations in Vector Form • If the vectors of output variables y, disturbance variables rm, and vectors of functions g are defined as: Then the set of algebraic output equatios can be written compactly as:

  6. Chapter 2 General Process Models Heat Exchanger in State Space Form Tl q V ρ T cp T q Tj If , then State Space Equations

  7. Chapter 2 Linearization Linearization • Linearization is a procedure to replace a nonlinear original model with its linear approximation. • Linearization is done around a constant operating point. • It is assumed that the process variables change only very little and their deviations from steady state remain small. Operating point Linearization Taylor series expansion Nonlinear Model Linear Model

  8. Chapter 2 Linearization Linearization • The approximation model will be in the form of state space equations • An operating point x0(t) is chosen, and the input u0(t) is required to maintain this operating point. • In steady state, there will be no state change at the operating point, or x0(t) = 0

  9. Chapter 2 Linearization Taylor Expansion Series • Scalar Case A point near x0 Only the linear terms are used for the linearization

  10. Chapter 2 Linearization Taylor Expansion Series • Vector Case where

  11. Chapter 2 Linearization Taylor Expansion Series n: Number of states m : Number of inputs

  12. Chapter 2 Linearization Taylor Expansion Series Performing the same procedure for the output equations,

  13. Chapter 2 Linearization Taylor Expansion Series r: Number of outputs

  14. Chapter 2 Linearization Taylor Expansion Series Nonlinear Model Linear Model

  15. Chapter 2 Linearization Single Tank System qi • The model of the system is already derived as: V h qo v1 • The relationship betweenh and h in the above equation is nonlinear. • An operating point for the linearization is chosen, (h0,qi,0).

  16. Chapter 2 Linearization Single Tank System • The linearization around (h0,qi,0) for the state equation can be calculated as:

  17. Chapter 2 Linearization Single Tank System • The linearization for the ouput equation is: • Note that the input of the linearized model is now Δqi. • To obtain the actual value of state and output, the following equation must be enacted:

  18. Chapter 2 Linearization Single Tank System • The Matlab-Simulink model of the linearized system is shown below. All parameters take the previous values.

  19. Chapter 2 Linearization Single Tank System • The simulation results : Original model : Linearized model

  20. Chapter 2 Linearization Single Tank System • If the input qi deviates from the operating point, the linearized model will deliver inaccurate output. : Original model : Linearized model

  21. Chapter 2 Linearization Single Tank System • If the input qi deviates from the operating point, the linearized model will deliver inaccurate output. : Original model : Linearized model

  22. Chapter 2 Linearization Homework 3: Interacting Tank-in-Series System Linearize the the interacting tank-in-series system for the operating point resulted by the parameter values as given in Homework 2. • For qi, use the last digit of your Student ID. For example: Kartika qi= 8 liters/s. • Submit the mdl-file and the screenshots of the Matlab-Simulink file + scope. qi h1 h2 q1 a1 a2 v2 v1

  23. Chapter 2 Linearization Homework 3: Triangular-Prism-Shaped Tank Linearize the the triangular-prism-shaped tank for the operating point resulted by the parameter values as given in Homework 2 (New). • For qi2, use the last 2 digits of your Student ID. For example: Bernard Andrew  qi2= 0.3 liter/s, Sugianto qi2= 1.0 liter/s. • Submit the mdl-file and the screenshots of the Matlab-Simulink file + scope. NEW qi2 qi1 hmax h a qo v

More Related