Multivariable Processes Control-Process Control-Lecture Slides, Slides of Process Control

This lecture was delivered by Dr. Sakal Japendu for Process Control course at Ambedkar University, Delhi. It includes: Control, Multivariable, Process, Plants, Sensor, Manipulated, Variables, Single-loop, Independent

Typology: Slides

2011/2012

Uploaded on 07/17/2012

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CONTROL OF MULTIVARIABLE PROCESSES
Process plants ( or complex experiments) have many
variables that must be controlled. The engineer must
1. Provide the needed sensors
2. Provide adequate manipulated variables
3. Decide how the CVs and MVs are paired
(linked via the control design)
Fortunately, most of what we learned about single-loop
systems applies, but we need to learn more!
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Download Multivariable Processes Control-Process Control-Lecture Slides and more Slides Process Control in PDF only on Docsity!

CONTROL OF MULTIVARIABLE PROCESSES

Process plants ( or complex experiments) have manyvariables that must be controlled. The engineer must1.

Provide the needed sensors

Provide adequate manipulated variables

Decide how the CVs and MVs are paired(linked via the control design)

Fortunately, most of what we learned about single-loopsystems applies, but we need to learn more!

CONTROL OF MULTIVARIABLE PROCESSES

Two control approaches are possible

We will concentrate on

MULTILOOP

L

F

T

A

Multiloop: many

independent PID controllers

Centralized

L

F

T

A

CentralizedController

CONTROL OF MULTIVARIABLE PROCESSES

Some key questions whose answers help us

design a multiloop control system.

IS INTERACTION PRESENT?

  • If no interaction

All single-loop problems

IS CONTROL POSSIBLE?- Can we control the specified CVs with the

available MVs?

WHAT IS S-S AND DYNAMIC BEHAVIOR?- Over what range can control keep CVs near the setpoints?

Let’s start

here to build

understanding

CONTROL OF MULTIVARIABLE PROCESSES

T

A

What is different when we have multiple MVs and CVs?

INTERACTION!!

Definition: A multivariable process has interaction wheninput (manipulated) variables affect more than one output(controlled) variable.

Does this process have interaction?

CONTROL OF MULTIVARIABLE PROCESSES

How can we determine how much interaction exists?

Second way - Empirical modelling (process reaction curve)

0

20

40

60

80

100

120

0.9880.9860.9840.

Time (min)

XD (mol frac)

0

20

40

60

80

100

120

Time (min)

XB (mol frac)

0

20

40

60

80

100

120

x 10

4

Time (min)

R (mol/min)

0

20

40

60

80

100

120

1.56151.56151.56141.56141.56131.

x 10

4

Time (min)

V (mol/min)

Step change to reflux with constant reboiler

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CONTROL OF MULTIVARIABLE PROCESSES

How can we determine how much interaction exists?

Second way - Empirical modelling (process reaction curve)

.

s

F

s

e

s

F

s

e

s

x

s

F

s

e

s

F

s

e

s

x

V

s

R

s

B

V

s

R

s

D

2

3

3

2

3

F

R

F

V

x

B

x

D

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CONTROL OF MULTIVARIABLE PROCESSES

How can we determine how much interaction exists?

Use the model; if model can be arranged so that it has a

“diagonal” form, no interaction exists.

T

A

Does this CSTR reactorprocess have

interaction?

v

v

G

11

(s)

G

21

(s)

G

12

(s)

G

22

(s)

G

d

(s)

G

d

(s)

D(s)

CV

1

(s)

CV

2

(s)

MV

2

(s)

MV

1

(s)

CONTROL OF MULTIVARIABLE PROCESSES

We will use a block diagram to represent the dynamics of a2x2 process, which involves multivariable control.

G

11

(s)

G

21

(s)

G

12

(s)

G

22

(s)

G

d

(s)

G

d

(s)

Let’s relate the block diagram to a typical physical process.

What are the MVs, CVs, and a disturbance, D?

T

A

Reactor

CONTROL OF MULTIVARIABLE PROCESSES

v

v

CONTROL OF MULTIVARIABLE PROCESSES

Some key questions whose answers help us

design a multiloop control system.

IS INTERACTION PRESENT?

  • If no interaction

All single-loop problems

IS CONTROL POSSIBLE?- How many degrees of freedom exist?- Can we control CVs with MVs?

WHAT IS S-S AND DYNAMIC BEHAVIOR?- Over what range can control keep CVs near the setpoints?

Let’s learn how

to answer this

key question

CONTROL OF MULTIVARIABLE PROCESSES

DEGREES OF FREEDOM

A requirement for a successful design is:

The number of valves

number of CV to be controlled

v

Hot Oil

v

v

L

v

v

v

Hot Oil

F

T

T

T

F

T

T

F

T

T

F

L

v

T

P

F

F

T

OK, but this does not ensure that we can

control the CVs that we want to control!

CONTROL OF MULTIVARIABLE PROCESSES

CONTROLLABILITY

A system is controllable if its CVs can be maintained at

their set points, in the steady-state, in spite of disturbances

entering the system.

A system is controllable when the matrix of process gains canbe inverted, i.e., when the determinant of K

D

K

K

MV

MV

K

K

K

K

CV

CV

d

d

  

  

  

  

  

  

=

  

  

=

  

  

1 2

1 2

22

21

12

11

1 2

0 0

Modelfor 2x2system

I am in desperate need of examples

CONTROL OF MULTIVARIABLE PROCESSES

For the autos in the figure

Are they independently controllable?

Does interaction exist?

Connected by spring

CONTROL OF MULTIVARIABLE PROCESSES

For the autos in the figure

Are they independently controllable?

Does interaction exist?

Connected by beam