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Dynamic simulation of Steam
and Power System
Dr M S R Murty
msrm1951@gmail.com
Stream
Generators
LP
Process
VHP HP MP
PRDS
Process Process
Process
HRSGs
UBs
G
Typical Steam and Power System
Headers
107/ 510 45/ 400 20/ 340 5.5/ 220
Kg/Cm2 o C
C
G
GAS TURBINE
G
Steam
Turbine
Captive Power Plant - General Overview
NAPHTHA
GAS OIL
GAS TURBINE
NAPHTHA
GAS OIL
8 X 125 TPH HRSG
AUX
BOILERS
4 x 125 TPH
Refinery Fuel Oil
STEAM
TURBINE
HP steam 42 Kg/cm2
MP steam 17 Kg/cm2
To
Refinery
Power Steam
INSTALLED CAPACITY 360 MW 1500 TPH
PRESENT GENERATION 269 MW 979 TPH
EXPORT TO GEB CAPABILITY 80 MW ------------
TO GEB 132/220 kV
TO REFINERY
4 X 30 MW
8 X 30 MW
11 KV
33 KV
33 KV
11 KV
Reliance Jamnagar
• All 4 STGs are tested to deliver 30 MW of power.
• Steam turbines are provided with HP and MP extractions
• Maximum steam flow through one steam turbine shall be as follows
262 TPH HHP steam (Max)
Pr: 109 Kg/CM^2 @ 505 DegC
180 TPH HP steam (Max)
149 TPH HP steam (Normal)
Pr: 44.8 Kg/CM^2 @ 383 DegC
80 TPH MP steam (Max)
53 TPH MP steam (Normal)
Pr: 18.8 Kg/Cm^2 @ 282 DegC
60 TPH to Condenser (Max.)
20 TPH to Condenser (Min.)
Steam Turbine
MP
133
TPH
LP
60
TPH
Normal steam flow
HP section =15.27 MW
MP section = 5.73 MW
LP section = 11.81 MW
Reliance Jamnagar
Typical Steam and Power System
• 8 GTGs, 4 STGs (extraction types)
• 8 HRSGs, 4 Aux Boilers
• Steam generators and Consumers within
Process
• Turbine driven equipment in Process
• Limits on Header pressure:+3 %,- 10 %
Temperature: + or – 10 %
Set point
Process
Steam
Pressure
STEAM
GENERATORs
V
H
P
H
E
A
D
E
R
GOVERNING
SYSTEM
G
UPSET : SUDDEN STEAM DEMAND CHANGE
MP
LP
tph
sec
Set point
Process Steam
Pressure
STEAM
GENERATORs
V
H
P
H
E
A
D
E
R
GOVERNING
SYSTEM
G
UPSET : STEAM TURBINE TRIP
MP
LP
C
ST
G
G
G
GAS TURBINE
Div Damper
HRSG
VHP STEAM
HEADER
Upset: GT TTRIP or HRSG Trip
Fuel
Inlet Air
Steam and Power system Dynamics
Steam
System
Power
System
Fuel
System
Upsets in one system can influence the other
Header Pr Variations For T-C Upset
Steam Flows for Upset condition
Dynamic simulation of Steam and Power System.ppt
Dynamic simulation of Steam and Power System.ppt
Dynamic simulation of Steam and Power System.ppt
Summary
• Dynamic simulation helps in predicting
transient deviations in critical process
parameters
• Tuning of control system parameters can be
done based on simulation study
• Different control strategies can be evaluated

More Related Content

Dynamic simulation of Steam and Power System.ppt

  • 1. Dynamic simulation of Steam and Power System Dr M S R Murty msrm1951@gmail.com
  • 2. Stream Generators LP Process VHP HP MP PRDS Process Process Process HRSGs UBs G Typical Steam and Power System Headers 107/ 510 45/ 400 20/ 340 5.5/ 220 Kg/Cm2 o C C G GAS TURBINE G Steam Turbine
  • 3. Captive Power Plant - General Overview NAPHTHA GAS OIL GAS TURBINE NAPHTHA GAS OIL 8 X 125 TPH HRSG AUX BOILERS 4 x 125 TPH Refinery Fuel Oil STEAM TURBINE HP steam 42 Kg/cm2 MP steam 17 Kg/cm2 To Refinery Power Steam INSTALLED CAPACITY 360 MW 1500 TPH PRESENT GENERATION 269 MW 979 TPH EXPORT TO GEB CAPABILITY 80 MW ------------ TO GEB 132/220 kV TO REFINERY 4 X 30 MW 8 X 30 MW 11 KV 33 KV 33 KV 11 KV Reliance Jamnagar
  • 4. • All 4 STGs are tested to deliver 30 MW of power. • Steam turbines are provided with HP and MP extractions • Maximum steam flow through one steam turbine shall be as follows 262 TPH HHP steam (Max) Pr: 109 Kg/CM^2 @ 505 DegC 180 TPH HP steam (Max) 149 TPH HP steam (Normal) Pr: 44.8 Kg/CM^2 @ 383 DegC 80 TPH MP steam (Max) 53 TPH MP steam (Normal) Pr: 18.8 Kg/Cm^2 @ 282 DegC 60 TPH to Condenser (Max.) 20 TPH to Condenser (Min.) Steam Turbine MP 133 TPH LP 60 TPH Normal steam flow HP section =15.27 MW MP section = 5.73 MW LP section = 11.81 MW Reliance Jamnagar
  • 5. Typical Steam and Power System • 8 GTGs, 4 STGs (extraction types) • 8 HRSGs, 4 Aux Boilers • Steam generators and Consumers within Process • Turbine driven equipment in Process • Limits on Header pressure:+3 %,- 10 % Temperature: + or – 10 %
  • 8. C ST G G G GAS TURBINE Div Damper HRSG VHP STEAM HEADER Upset: GT TTRIP or HRSG Trip Fuel Inlet Air
  • 9. Steam and Power system Dynamics Steam System Power System Fuel System Upsets in one system can influence the other
  • 10. Header Pr Variations For T-C Upset
  • 11. Steam Flows for Upset condition
  • 15. Summary • Dynamic simulation helps in predicting transient deviations in critical process parameters • Tuning of control system parameters can be done based on simulation study • Different control strategies can be evaluated