Introduction to PEF3006 Process Control · 2018. 8. 5. · Introduction to PEF3006 Process Control...
Transcript of Introduction to PEF3006 Process Control · 2018. 8. 5. · Introduction to PEF3006 Process Control...
Introduction toPEF3006 Process Control
By Finn Aakre Haugen, PhD, Docent([email protected])
105 Aug 2018. PEF3006 Process Control.
USN.
205 Aug 2018. PEF3006 Process Control. USN.
Course organization:
• Lectures - in classroom and on video
• Theoretical exercises
• Labs and simulations (compulsory)
- individual and in groups
• Written exam counting 100%
- without aids but with formula list known in advance
305 Aug 2018. PEF3006 Process Control.
USN.
Course contents ...
PID feedback control
405 Aug 2018. PEF3006 Process Control.
USN.
(PID = Proportional + Interal + Derivative)
Demo:
Simulation of a temperature control system of a liquid tank
(This tank may be a biogas reactor.)
505 Aug 2018. PEF3006 Process Control. USN.
Cascade control - several PID loops inside each other
605 Aug 2018. PEF3006 Process Control. USN.
Feedforward control - using measured environmental
variables for control
705 Aug 2018. PEF3006 Process Control.
USN.
MPC (Model-based Predictive Control)
- using simulations into the future to find the optimal
control signal
Timetk tk+1 tk+Ntk+(N-1)
y (predicted by model)
uopt (predicted)
d (assumed)
x(tk) (known from
meas or estimator)
Prediction horizon (N+1 points of time)
Main aim is to calculate
uopt(tk) = uopt(1)= ?
Present
point of
time Future
ysp (known)
Ts
y(tk) (known from
meas or estimator)
d(tk) (known from meas
or estimator or assumed)
x (predicted by model)
805 Aug 2018. PEF3006 Process Control. USN.
Plant-wide control structures
- to control flow, material (inventories or accumulated
amounts of solids, liquid and gas) and temperature in
industrial plants
Nitric acid plant with control system (simplified):
Tank T1
Mixer
M1
Process
water
Reactor
R1
Compressor
K1
NH3
FT
2FFC
1
LC
1
LT
1
PT
1
PC
1
Evaporator
E1
Cold
water
Liquid
Gas
Ammonia
(liquid)
LT
2
LC
2
Condenser C1
LT
3
LC
3
O2
890 oC
NO + H2O
Raw
nitric
acid
HNO3
H2OAbsorber
A1
N2 and NOx
Liquid (acid)
Gas
Shaft 1
Turbine/
generator
TG2
Tail gas
Liquid down
Gas upHeater H1
Air with NOx
FC
3
FT
3
Feed:
Gas
V4
Valve
V1
V2
V3
V5
P1
Manual
setpoint
adjustment
QT
1
NH3
Ammonia
(gas)
Feed:
ST
1
SC
1Air
Turbine/
generator
TG1
Steam
Steam
Steam
drum
D1
Water
Gas
Gas
Specified
Amm./Air
ratio
Liq.
Lab
analysis
Production rate
setpoint
Meas.
rot. speedMULT
kMeas.
air flow
(From bleacher)
NO2
+ H2O
Compressor
K2
Shaft 1
905 Aug 2018. PEF3006 Process Control. USN.
LabVIEW programming for measurement, control and
simulation applications
1005 Aug 2018. PEF3006 Process Control. USN.
MATLAB programming
for control system simulation and analysis
1105 Aug 2018. PEF3006 Process Control. USN.
K-Spice simulation of industrial plants
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Labs: Implementing a simulator and temperature control
system of a laboratory-scale air heater
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Theory about control systems:
• Differential equations
• State-space models
• Transfer functions
• Dynamics
• Stability
• Simulation