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Flexibility of multi-fuel plants -
Needs, possibilities and
solutions
31.10.2016, Tero Joronen, Plant Solutions Manager
Drivers: Future multi-fuel CHP
Future multi-fuel CHP: Next level
Dynamic model for design and testing
0 5 10 15
Main steam mass flow
Δ 5 bar
Δ 10 bar
CFB boiler process model in
MATLAB Simulink
•  A dynamic simulator is applied in testing
flexibility
•  Process parameter studies
•  Output constraints
•  Process design improvement
Temperature change in the drum
Time [min]
0 5 10 15 20
[o
C]
-9
-8
-7
-6
-5
-4
-3
-2
-1
0
•  Coupled CFD-
Apros process
simulator
•  Dynamic models
that can calculate
ramps
•  Emissions,
controls, local
conditions inside
the boiler
Dynamic CFD modelling
Solids vertical velocity [m/s]
-  Biomass CHP needs fuel, operational and solution
flexibility
-  Biomass CHP is needed also 2050 in windy scenario
-  Boiler design needs renewal
-  Tools for testing new designs are now available
-  Further development is needed
SUMMARY

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EFEU / FLEXe Joronen Tero flexibility of multi-fuel plants - needs, possibilities and solutions

  • 1. Flexibility of multi-fuel plants - Needs, possibilities and solutions 31.10.2016, Tero Joronen, Plant Solutions Manager
  • 4.
  • 5. Dynamic model for design and testing 0 5 10 15 Main steam mass flow Δ 5 bar Δ 10 bar CFB boiler process model in MATLAB Simulink •  A dynamic simulator is applied in testing flexibility •  Process parameter studies •  Output constraints •  Process design improvement
  • 6. Temperature change in the drum Time [min] 0 5 10 15 20 [o C] -9 -8 -7 -6 -5 -4 -3 -2 -1 0
  • 7. •  Coupled CFD- Apros process simulator •  Dynamic models that can calculate ramps •  Emissions, controls, local conditions inside the boiler Dynamic CFD modelling Solids vertical velocity [m/s]
  • 8. -  Biomass CHP needs fuel, operational and solution flexibility -  Biomass CHP is needed also 2050 in windy scenario -  Boiler design needs renewal -  Tools for testing new designs are now available -  Further development is needed SUMMARY