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I NTRODUCTION   T HERMODYNAMIC METHODS   O PTIMIZATION METHODS   C ARBON CONSTRAINED SCENARIO   S UMMARY




            O PTIMAL SYNTHESIS OF STEAM AND POWER
                                            PLANTS


                                     Rahul Anantharaman

                            Department of Energy & Process Engineering
                           Norwegian University of Science and Technology


                                       PhD Trial Lecture
                                    Trondheim, 06.12.2011
I NTRODUCTION    T HERMODYNAMIC METHODS   O PTIMIZATION METHODS   C ARBON CONSTRAINED SCENARIO   S UMMARY



O UTLINE
       1   I NTRODUCTION
                The topic
                Boundary conditions and components
                Process Synthesis Methods
       2   T HERMODYNAMIC METHODS
                Early work
                Targeting methodologies
       3   O PTIMIZATION METHODS
                Background
                Early work
                Recent Trends in synthesis
       4   C ARBON CONSTRAINED SCENARIO
                CCS
                Bio-energy
       5   S UMMARY
I NTRODUCTION    T HERMODYNAMIC METHODS   O PTIMIZATION METHODS   C ARBON CONSTRAINED SCENARIO   S UMMARY



O UTLINE
       1   I NTRODUCTION
                The topic
                Boundary conditions and components
                Process Synthesis Methods
       2   T HERMODYNAMIC METHODS
                Early work
                Targeting methodologies
       3   O PTIMIZATION METHODS
                Background
                Early work
                Recent Trends in synthesis
       4   C ARBON CONSTRAINED SCENARIO
                CCS
                Bio-energy
       5   S UMMARY
I NTRODUCTION   T HERMODYNAMIC METHODS   O PTIMIZATION METHODS   C ARBON CONSTRAINED SCENARIO   S UMMARY


T HE TOPIC
AND MY INTEPRETATION




                    Optimal Synthesis of Steam and Power Plants
I NTRODUCTION   T HERMODYNAMIC METHODS   O PTIMIZATION METHODS   C ARBON CONSTRAINED SCENARIO   S UMMARY


T HE TOPIC
AND MY INTEPRETATION




                    Optimal Synthesis of Steam and Power Plants
I NTRODUCTION   T HERMODYNAMIC METHODS   O PTIMIZATION METHODS   C ARBON CONSTRAINED SCENARIO   S UMMARY


T HE TOPIC
AND MY INTEPRETATION




                    Optimal Synthesis of Steam and Power Plants
I NTRODUCTION   T HERMODYNAMIC METHODS   O PTIMIZATION METHODS   C ARBON CONSTRAINED SCENARIO   S UMMARY


T HE TOPIC
AND MY INTEPRETATION




                    Optimal Synthesis of Steam and Power Plants
I NTRODUCTION   T HERMODYNAMIC METHODS   O PTIMIZATION METHODS   C ARBON CONSTRAINED SCENARIO   S UMMARY


T HE TOPIC
AND MY INTEPRETATION




                    Optimal Synthesis of Steam and Power Plants
I NTRODUCTION    T HERMODYNAMIC METHODS   O PTIMIZATION METHODS   C ARBON CONSTRAINED SCENARIO   S UMMARY



O UTLINE
       1   I NTRODUCTION
                The topic
                Boundary conditions and components
                Process Synthesis Methods
       2   T HERMODYNAMIC METHODS
                Early work
                Targeting methodologies
       3   O PTIMIZATION METHODS
                Background
                Early work
                Recent Trends in synthesis
       4   C ARBON CONSTRAINED SCENARIO
                CCS
                Bio-energy
       5   S UMMARY
I NTRODUCTION   T HERMODYNAMIC METHODS   O PTIMIZATION METHODS   C ARBON CONSTRAINED SCENARIO   S UMMARY



C OMBINED H EAT AND P OWER (CHP) PLANT
I NTRODUCTION   T HERMODYNAMIC METHODS   O PTIMIZATION METHODS   C ARBON CONSTRAINED SCENARIO   S UMMARY



C OMBINED H EAT AND P OWER (CHP) PLANT
I NTRODUCTION          T HERMODYNAMIC METHODS    O PTIMIZATION METHODS     C ARBON CONSTRAINED SCENARIO   S UMMARY


P RIME MOVER
T YPICAL CHARACTERISTICS




                                   Gas         Micro-    Reciprocating     Steam           Fuel
                                 turbine      turbine       engine         turbine          cell
                               NG, biogas   NG, biogas    NG, biogas                     H2 , NG,
                Fuel            propane,     propane,      propane,          all         propane,
                                    oil          oil        diesel                       methanol
        Use for thermal        Heat, HW,    Heat, HW,    HW, LP steam    LP-HP steam   HW, LP* steam
            output            LP-HP steam    LP steam
         Power to Heat            0.5-2       0.4-0.7        0.5-1         0.1-0.3          1-2
             ratio
            Typical             0.5-250     0.03-0.25       0.01-5         0.5-250        0.005-2
        capacity (MWe)
I NTRODUCTION   T HERMODYNAMIC METHODS   O PTIMIZATION METHODS   C ARBON CONSTRAINED SCENARIO   S UMMARY



C OMBINED H EAT AND P OWER (CHP) PLANT
I NTRODUCTION   T HERMODYNAMIC METHODS   O PTIMIZATION METHODS   C ARBON CONSTRAINED SCENARIO   S UMMARY



C OMBINED H EAT AND P OWER (CHP) PLANT
I NTRODUCTION   T HERMODYNAMIC METHODS   O PTIMIZATION METHODS   C ARBON CONSTRAINED SCENARIO   S UMMARY



C OMBINED H EAT AND P OWER (CHP) PLANT
I NTRODUCTION     T HERMODYNAMIC METHODS   O PTIMIZATION METHODS   C ARBON CONSTRAINED SCENARIO   S UMMARY



OTHER COMPONENTS IN THE CHP SYSTEM




                Boilers for steam generation
                Waste heat boilers for steam generation
                Generators for conversion of power to electricity
                Electric motors as mechanical drivers (in addition to gas and
                steam turbines)
I NTRODUCTION    T HERMODYNAMIC METHODS   O PTIMIZATION METHODS   C ARBON CONSTRAINED SCENARIO   S UMMARY



O UTLINE
       1   I NTRODUCTION
                The topic
                Boundary conditions and components
                Process Synthesis Methods
       2   T HERMODYNAMIC METHODS
                Early work
                Targeting methodologies
       3   O PTIMIZATION METHODS
                Background
                Early work
                Recent Trends in synthesis
       4   C ARBON CONSTRAINED SCENARIO
                CCS
                Bio-energy
       5   S UMMARY
I NTRODUCTION   T HERMODYNAMIC METHODS   O PTIMIZATION METHODS   C ARBON CONSTRAINED SCENARIO   S UMMARY



P ROCESS S YNTHESIS


      Process synthesis is the systematic generation of alternative
      process flowsheets and selection of a design whose configuration
      and parameters optimize a given objective function.
I NTRODUCTION     T HERMODYNAMIC METHODS   O PTIMIZATION METHODS   C ARBON CONSTRAINED SCENARIO   S UMMARY


T HERMODYNAMIC METHODS
A   NOTE




                The two products from a CHP or utility system power and
                heat.
                First law analysis where heat and work are equivalent is not
                sufficient.
                Second law analysis required for consistent evaluation and
                consideration of both products in a systematic way.
                E XERGY BASED APPROACH TO THERMODYNAMIC ANALYSIS .
I NTRODUCTION    T HERMODYNAMIC METHODS   O PTIMIZATION METHODS   C ARBON CONSTRAINED SCENARIO   S UMMARY



O UTLINE
       1   I NTRODUCTION
                The topic
                Boundary conditions and components
                Process Synthesis Methods
       2   T HERMODYNAMIC METHODS
                Early work
                Targeting methodologies
       3   O PTIMIZATION METHODS
                Background
                Early work
                Recent Trends in synthesis
       4   C ARBON CONSTRAINED SCENARIO
                CCS
                Bio-energy
       5   S UMMARY
I NTRODUCTION     T HERMODYNAMIC METHODS   O PTIMIZATION METHODS   C ARBON CONSTRAINED SCENARIO   S UMMARY



T HERMODYNAMICS - BASED H EURISTIC METHODS

      N ISHIO AND J OHNSON (1979), N ISHIO ET. AL . (1980)
                Introduced a number of thermodynamic-based heuristics for
                reducing the loss of available energy in steam cycles.
                Developed Heuristics for preliminary selection of energy
                conservation and power generation technologies.
                     Two-step approach that differentiated between steam
                     dominant and power dominant cases.
                     Linear Program for allocation of drivers.

      C HOU AND S HIH (1987)
                Similar approach to Nishio et. al. (1982).
                Included gas turbine and combined gas-steam cycles.
                Five step procedure for designing the system starts with
                screening based on P/H ratio.
I NTRODUCTION     T HERMODYNAMIC METHODS   O PTIMIZATION METHODS   C ARBON CONSTRAINED SCENARIO   S UMMARY



T HERMODYNAMICS - BASED H EURISTIC METHODS

      N ISHIO AND J OHNSON (1979), N ISHIO ET. AL . (1980)
                Introduced a number of thermodynamic-based heuristics for
                reducing the loss of available energy in steam cycles.
                Developed Heuristics for preliminary selection of energy
                conservation and power generation technologies.
                     Two-step approach that differentiated between steam
                     dominant and power dominant cases.
                     Linear Program for allocation of drivers.

      C HOU AND S HIH (1987)
                Similar approach to Nishio et. al. (1982).
                Included gas turbine and combined gas-steam cycles.
                Five step procedure for designing the system starts with
                screening based on P/H ratio.
I NTRODUCTION    T HERMODYNAMIC METHODS   O PTIMIZATION METHODS   C ARBON CONSTRAINED SCENARIO   S UMMARY



O UTLINE
       1   I NTRODUCTION
                The topic
                Boundary conditions and components
                Process Synthesis Methods
       2   T HERMODYNAMIC METHODS
                Early work
                Targeting methodologies
       3   O PTIMIZATION METHODS
                Background
                Early work
                Recent Trends in synthesis
       4   C ARBON CONSTRAINED SCENARIO
                CCS
                Bio-energy
       5   S UMMARY
I NTRODUCTION     T HERMODYNAMIC METHODS   O PTIMIZATION METHODS   C ARBON CONSTRAINED SCENARIO   S UMMARY


TARGETS FOR COGENERATION
E XTENSION OF P INCH A NALYSIS

      D HOLE AND L INNHOFF (1993) AND L INNHOFF AND D HOLE
      (1993)
                Extended Pinch Analysis for total site wide targets for fuel,
                co-generation and emissions.
                Site Source-Sink Profiles (SSSP) for site level targeting.
                First systematic thermodynamic method for targeting
                co-generation.
                Only boilers and steam turbine systems are included.
                No detail design method proposed.
                Methodology extended in Raissi (1994) and developed the
                TH-shaftwork targeting model.
                The methodology extended by Bandyopadhyay et al. (2010)
                to generate Site level Grand Composite Curves (SGCC) to
                include indirect heat transfer.
I NTRODUCTION     T HERMODYNAMIC METHODS   O PTIMIZATION METHODS   C ARBON CONSTRAINED SCENARIO   S UMMARY


TARGETS FOR COGENERATION
E XTENSION OF P INCH A NALYSIS

      D HOLE AND L INNHOFF (1993) AND L INNHOFF AND D HOLE
      (1993)
                Extended Pinch Analysis for total site wide targets for fuel,
                co-generation and emissions.
                Site Source-Sink Profiles (SSSP) for site level targeting.
                First systematic thermodynamic method for targeting
                co-generation.
                Only boilers and steam turbine systems are included.
                No detail design method proposed.
                Methodology extended in Raissi (1994) and developed the
                TH-shaftwork targeting model.
                The methodology extended by Bandyopadhyay et al. (2010)
                to generate Site level Grand Composite Curves (SGCC) to
                include indirect heat transfer.
I NTRODUCTION     T HERMODYNAMIC METHODS   O PTIMIZATION METHODS   C ARBON CONSTRAINED SCENARIO   S UMMARY


TARGETS FOR COGENERATION
E XTENSION OF P INCH A NALYSIS

      D HOLE AND L INNHOFF (1993) AND L INNHOFF AND D HOLE
      (1993)
                Extended Pinch Analysis for total site wide targets for fuel,
                co-generation and emissions.
                Site Source-Sink Profiles (SSSP) for site level targeting.
                First systematic thermodynamic method for targeting
                co-generation.
                Only boilers and steam turbine systems are included.
                No detail design method proposed.
                Methodology extended in Raissi (1994) and developed the
                TH-shaftwork targeting model.
                The methodology extended by Bandyopadhyay et al. (2010)
                to generate Site level Grand Composite Curves (SGCC) to
                include indirect heat transfer.
I NTRODUCTION     T HERMODYNAMIC METHODS   O PTIMIZATION METHODS   C ARBON CONSTRAINED SCENARIO   S UMMARY


TARGETS FOR COGENERATION
E XTENSION OF P INCH A NALYSIS

      D HOLE AND L INNHOFF (1993) AND L INNHOFF AND D HOLE
      (1993)
                Extended Pinch Analysis for total site wide targets for fuel,
                co-generation and emissions.
                Site Source-Sink Profiles (SSSP) for site level targeting.
                First systematic thermodynamic method for targeting
                co-generation.
                Only boilers and steam turbine systems are included.
                No detail design method proposed.
                Methodology extended in Raissi (1994) and developed the
                TH-shaftwork targeting model.
                The methodology extended by Bandyopadhyay et al. (2010)
                to generate Site level Grand Composite Curves (SGCC) to
                include indirect heat transfer.
I NTRODUCTION     T HERMODYNAMIC METHODS   O PTIMIZATION METHODS   C ARBON CONSTRAINED SCENARIO   S UMMARY


TARGETS FOR COGENERATION
E XTENSION OF P INCH A NALYSIS

      D HOLE AND L INNHOFF (1993) AND L INNHOFF AND D HOLE
      (1993)
                Extended Pinch Analysis for total site wide targets for fuel,
                co-generation and emissions.
                Site Source-Sink Profiles (SSSP) for site level targeting.
                First systematic thermodynamic method for targeting
                co-generation.
                Only boilers and steam turbine systems are included.
                No detail design method proposed.
                Methodology extended in Raissi (1994) and developed the
                TH-shaftwork targeting model.
                The methodology extended by Bandyopadhyay et al. (2010)
                to generate Site level Grand Composite Curves (SGCC) to
                include indirect heat transfer.
I NTRODUCTION     T HERMODYNAMIC METHODS   O PTIMIZATION METHODS   C ARBON CONSTRAINED SCENARIO   S UMMARY


TARGETS FOR COGENERATION
E XTENSION OF P INCH A NALYSIS

      D HOLE AND L INNHOFF (1993) AND L INNHOFF AND D HOLE
      (1993)
                Extended Pinch Analysis for total site wide targets for fuel,
                co-generation and emissions.
                Site Source-Sink Profiles (SSSP) for site level targeting.
                First systematic thermodynamic method for targeting
                co-generation.
                Only boilers and steam turbine systems are included.
                No detail design method proposed.
                Methodology extended in Raissi (1994) and developed the
                TH-shaftwork targeting model.
                The methodology extended by Bandyopadhyay et al. (2010)
                to generate Site level Grand Composite Curves (SGCC) to
                include indirect heat transfer.
I NTRODUCTION     T HERMODYNAMIC METHODS   O PTIMIZATION METHODS   C ARBON CONSTRAINED SCENARIO   S UMMARY


TARGETS FOR COGENERATION
E XTENSION OF P INCH A NALYSIS

      D HOLE AND L INNHOFF (1993) AND L INNHOFF AND D HOLE
      (1993)
                Extended Pinch Analysis for total site wide targets for fuel,
                co-generation and emissions.
                Site Source-Sink Profiles (SSSP) for site level targeting.
                First systematic thermodynamic method for targeting
                co-generation.
                Only boilers and steam turbine systems are included.
                No detail design method proposed.
                Methodology extended in Raissi (1994) and developed the
                TH-shaftwork targeting model.
                The methodology extended by Bandyopadhyay et al. (2010)
                to generate Site level Grand Composite Curves (SGCC) to
                include indirect heat transfer.
I NTRODUCTION   T HERMODYNAMIC METHODS   O PTIMIZATION METHODS   C ARBON CONSTRAINED SCENARIO   S UMMARY


TARGETS FOR COGENERATION
D HOLE AND L INNHOFF (1993)
I NTRODUCTION   T HERMODYNAMIC METHODS   O PTIMIZATION METHODS   C ARBON CONSTRAINED SCENARIO   S UMMARY


TARGETS FOR COGENERATION
D HOLE AND L INNHOFF (1993)
I NTRODUCTION   T HERMODYNAMIC METHODS   O PTIMIZATION METHODS   C ARBON CONSTRAINED SCENARIO   S UMMARY


TARGETS FOR COGENERATION
D HOLE AND L INNHOFF (1993)
I NTRODUCTION   T HERMODYNAMIC METHODS   O PTIMIZATION METHODS   C ARBON CONSTRAINED SCENARIO   S UMMARY


TARGETS FOR COGENERATION
D HOLE AND L INNHOFF (1993)
I NTRODUCTION     T HERMODYNAMIC METHODS   O PTIMIZATION METHODS   C ARBON CONSTRAINED SCENARIO   S UMMARY


TARGETS FOR COGENERATION
E XTRACTABLE POWER SURPLUS COMPOSITE CURVE


      E L -H ALWAGI ET AL . (2009)
                Targets for cogeneration given a set of combustible wastes
                and byproducts, heating cooling demands, non-heating steam
                demands.
                Using standard mass and heat integration procedures to
                identify process steam requirement and generation potential.
                New concept of extractable energy
                                                   ˙
                                                   e = ηH
                Extractable power surplus composite curve targets for
                cogeneration potential.
                Only boilers and steam turbine systems are included.
                No detail design method proposed.
I NTRODUCTION     T HERMODYNAMIC METHODS   O PTIMIZATION METHODS   C ARBON CONSTRAINED SCENARIO   S UMMARY


TARGETS FOR COGENERATION
E XTRACTABLE POWER SURPLUS COMPOSITE CURVE


      E L -H ALWAGI ET AL . (2009)
                Targets for cogeneration given a set of combustible wastes
                and byproducts, heating cooling demands, non-heating steam
                demands.
                Using standard mass and heat integration procedures to
                identify process steam requirement and generation potential.
                New concept of extractable energy
                                                   ˙
                                                   e = ηH
                Extractable power surplus composite curve targets for
                cogeneration potential.
                Only boilers and steam turbine systems are included.
                No detail design method proposed.
I NTRODUCTION     T HERMODYNAMIC METHODS   O PTIMIZATION METHODS   C ARBON CONSTRAINED SCENARIO   S UMMARY


TARGETS FOR COGENERATION
E XTRACTABLE POWER SURPLUS COMPOSITE CURVE


      E L -H ALWAGI ET AL . (2009)
                Targets for cogeneration given a set of combustible wastes
                and byproducts, heating cooling demands, non-heating steam
                demands.
                Using standard mass and heat integration procedures to
                identify process steam requirement and generation potential.
                New concept of extractable energy
                                                   ˙
                                                   e = ηH
                Extractable power surplus composite curve targets for
                cogeneration potential.
                Only boilers and steam turbine systems are included.
                No detail design method proposed.
I NTRODUCTION     T HERMODYNAMIC METHODS   O PTIMIZATION METHODS   C ARBON CONSTRAINED SCENARIO   S UMMARY


TARGETS FOR COGENERATION
E XTRACTABLE POWER SURPLUS COMPOSITE CURVE


      E L -H ALWAGI ET AL . (2009)
                Targets for cogeneration given a set of combustible wastes
                and byproducts, heating cooling demands, non-heating steam
                demands.
                Using standard mass and heat integration procedures to
                identify process steam requirement and generation potential.
                New concept of extractable energy
                                                   ˙
                                                   e = ηH
                Extractable power surplus composite curve targets for
                cogeneration potential.
                Only boilers and steam turbine systems are included.
                No detail design method proposed.
I NTRODUCTION     T HERMODYNAMIC METHODS   O PTIMIZATION METHODS   C ARBON CONSTRAINED SCENARIO   S UMMARY


TARGETS FOR COGENERATION
E XTRACTABLE POWER SURPLUS COMPOSITE CURVE


      E L -H ALWAGI ET AL . (2009)
                Targets for cogeneration given a set of combustible wastes
                and byproducts, heating cooling demands, non-heating steam
                demands.
                Using standard mass and heat integration procedures to
                identify process steam requirement and generation potential.
                New concept of extractable energy
                                                   ˙
                                                   e = ηH
                Extractable power surplus composite curve targets for
                cogeneration potential.
                Only boilers and steam turbine systems are included.
                No detail design method proposed.
I NTRODUCTION     T HERMODYNAMIC METHODS   O PTIMIZATION METHODS   C ARBON CONSTRAINED SCENARIO   S UMMARY


TARGETS FOR COGENERATION
E XTRACTABLE POWER SURPLUS COMPOSITE CURVE


      E L -H ALWAGI ET AL . (2009)
                Targets for cogeneration given a set of combustible wastes
                and byproducts, heating cooling demands, non-heating steam
                demands.
                Using standard mass and heat integration procedures to
                identify process steam requirement and generation potential.
                New concept of extractable energy
                                                   ˙
                                                   e = ηH
                Extractable power surplus composite curve targets for
                cogeneration potential.
                Only boilers and steam turbine systems are included.
                No detail design method proposed.
I NTRODUCTION   T HERMODYNAMIC METHODS   O PTIMIZATION METHODS   C ARBON CONSTRAINED SCENARIO   S UMMARY


TARGETS FOR COGENERATION
E L -H ALWAGI ET AL . (2009)
I NTRODUCTION   T HERMODYNAMIC METHODS   O PTIMIZATION METHODS   C ARBON CONSTRAINED SCENARIO   S UMMARY


TARGETS FOR COGENERATION
E L -H ALWAGI ET AL . (2009)
I NTRODUCTION   T HERMODYNAMIC METHODS   O PTIMIZATION METHODS   C ARBON CONSTRAINED SCENARIO   S UMMARY


TARGETS FOR COGENERATION
E L -H ALWAGI ET AL . (2009)
I NTRODUCTION   T HERMODYNAMIC METHODS   O PTIMIZATION METHODS   C ARBON CONSTRAINED SCENARIO   S UMMARY


TARGETS FOR COGENERATION
E L -H ALWAGI ET AL . (2009)
I NTRODUCTION    T HERMODYNAMIC METHODS   O PTIMIZATION METHODS   C ARBON CONSTRAINED SCENARIO   S UMMARY



O UTLINE
       1   I NTRODUCTION
                The topic
                Boundary conditions and components
                Process Synthesis Methods
       2   T HERMODYNAMIC METHODS
                Early work
                Targeting methodologies
       3   O PTIMIZATION METHODS
                Background
                Early work
                Recent Trends in synthesis
       4   C ARBON CONSTRAINED SCENARIO
                CCS
                Bio-energy
       5   S UMMARY
I NTRODUCTION   T HERMODYNAMIC METHODS   O PTIMIZATION METHODS   C ARBON CONSTRAINED SCENARIO   S UMMARY



O PTIMIZATION DESIGN SPACE




                                                                    El-Sayed Y.M. (2003)
I NTRODUCTION   T HERMODYNAMIC METHODS   O PTIMIZATION METHODS   C ARBON CONSTRAINED SCENARIO   S UMMARY



O PTIMIZATION DESIGN SPACE




                                                                    El-Sayed Y.M. (2003)
I NTRODUCTION   T HERMODYNAMIC METHODS   O PTIMIZATION METHODS   C ARBON CONSTRAINED SCENARIO   S UMMARY



O PTIMIZATION DESIGN SPACE




                                                                    El-Sayed Y.M. (2003)
I NTRODUCTION   T HERMODYNAMIC METHODS   O PTIMIZATION METHODS   C ARBON CONSTRAINED SCENARIO   S UMMARY



O PTIMIZATION DESIGN SPACE




                                                                    El-Sayed Y.M. (2003)
I NTRODUCTION    T HERMODYNAMIC METHODS   O PTIMIZATION METHODS   C ARBON CONSTRAINED SCENARIO   S UMMARY



A PPROACHES TO OPTIMIZATION OF CHP SYSTEMS



      Two broad approaches to the use of optimization in the design of
      CHP or utility systems
        1 Process Systems Engineering

                    Superstrucrure based approach
                    Evolution of structural changes
         2      Thermodynamic/Thermoeconomic
                    Parametric optimization
                    Suitable for optimizing a base case rather than synthesizing a
                    new design
I NTRODUCTION    T HERMODYNAMIC METHODS   O PTIMIZATION METHODS   C ARBON CONSTRAINED SCENARIO   S UMMARY



A PPROACHES TO OPTIMIZATION OF CHP SYSTEMS



      Two broad approaches to the use of optimization in the design of
      CHP or utility systems
        1 Process Systems Engineering

                    Superstrucrure based approach
                    Evolution of structural changes
         2      Thermodynamic/Thermoeconomic
                    Parametric optimization
                    Suitable for optimizing a base case rather than synthesizing a
                    new design
I NTRODUCTION   T HERMODYNAMIC METHODS   O PTIMIZATION METHODS   C ARBON CONSTRAINED SCENARIO   S UMMARY


O PTIMIZATION FRAMEWORK
G ENERIC SUPERSTRUCTURE
I NTRODUCTION   T HERMODYNAMIC METHODS   O PTIMIZATION METHODS   C ARBON CONSTRAINED SCENARIO   S UMMARY


O PTIMIZATION FRAMEWORK
G ENERIC SUPERSTRUCTURE
I NTRODUCTION   T HERMODYNAMIC METHODS   O PTIMIZATION METHODS   C ARBON CONSTRAINED SCENARIO   S UMMARY


O PTIMIZATION FRAMEWORK
G ENERIC SUPERSTRUCTURE
I NTRODUCTION     T HERMODYNAMIC METHODS   O PTIMIZATION METHODS   C ARBON CONSTRAINED SCENARIO   S UMMARY



O PTIMIZATION FRAMEWORK



      Given a set of steam and power demands:
                configure the CHP or utility plant;
                assign values of the operating pressures and temperatures of
                the steam;
                set the type and capacities of boilers, and all stream flowrates;
                and assign drivers to
                optimize the objective.
I NTRODUCTION     T HERMODYNAMIC METHODS   O PTIMIZATION METHODS   C ARBON CONSTRAINED SCENARIO   S UMMARY



O PTIMIZATION FRAMEWORK



      Given a set of steam and power demands:
                configure the CHP or utility plant;
                assign values of the operating pressures and temperatures of
                the steam;
                set the type and capacities of boilers, and all stream flowrates;
                and assign drivers to
                optimize the objective.
I NTRODUCTION     T HERMODYNAMIC METHODS   O PTIMIZATION METHODS   C ARBON CONSTRAINED SCENARIO   S UMMARY



O PTIMIZATION FRAMEWORK



      Given a set of steam and power demands:
                configure the CHP or utility plant;
                assign values of the operating pressures and temperatures of
                the steam;
                set the type and capacities of boilers, and all stream flowrates;
                and assign drivers to
                optimize the objective.
I NTRODUCTION     T HERMODYNAMIC METHODS   O PTIMIZATION METHODS   C ARBON CONSTRAINED SCENARIO   S UMMARY



O PTIMIZATION FRAMEWORK



      Given a set of steam and power demands:
                configure the CHP or utility plant;
                assign values of the operating pressures and temperatures of
                the steam;
                set the type and capacities of boilers, and all stream flowrates;
                and assign drivers to
                optimize the objective.
I NTRODUCTION     T HERMODYNAMIC METHODS   O PTIMIZATION METHODS   C ARBON CONSTRAINED SCENARIO   S UMMARY



O PTIMIZATION FRAMEWORK



      Given a set of steam and power demands:
                configure the CHP or utility plant;
                assign values of the operating pressures and temperatures of
                the steam;
                set the type and capacities of boilers, and all stream flowrates;
                and assign drivers to
                optimize the objective.
I NTRODUCTION    T HERMODYNAMIC METHODS   O PTIMIZATION METHODS   C ARBON CONSTRAINED SCENARIO   S UMMARY



O UTLINE
       1   I NTRODUCTION
                The topic
                Boundary conditions and components
                Process Synthesis Methods
       2   T HERMODYNAMIC METHODS
                Early work
                Targeting methodologies
       3   O PTIMIZATION METHODS
                Background
                Early work
                Recent Trends in synthesis
       4   C ARBON CONSTRAINED SCENARIO
                CCS
                Bio-energy
       5   S UMMARY
I NTRODUCTION     T HERMODYNAMIC METHODS   O PTIMIZATION METHODS   C ARBON CONSTRAINED SCENARIO   S UMMARY



M ATH PROGRAMMING APPROACHES

      PAPOULIAS AND G ROSSMANN (1983)
                Incorporates an extensive superstructure and model includes
                driver allocation.
                Linearized the inherent MINLP problem.
                     Linear equation derived for each unit when operating
                     parameters have fixed values.
                     Binary variables identify the existence of each operating
                     condition for each unit.
                     Non-linear cost linearized using a fixed charge approximation
                     or piece-wise linear function.
                The optimization criterion used was minimization of annual
                cost.
                Proved the strength of mathematical programming methods to
                synthesize utility systems compared to heuristic methods.
I NTRODUCTION   T HERMODYNAMIC METHODS   O PTIMIZATION METHODS   C ARBON CONSTRAINED SCENARIO   S UMMARY


M ATH PROGRAMMING APPROACHES
PAPOULIAS AND G ROSSMANN (1983)
I NTRODUCTION     T HERMODYNAMIC METHODS   O PTIMIZATION METHODS   C ARBON CONSTRAINED SCENARIO   S UMMARY



M ATH PROGRAMMING APPROACHES




      P ETROULAS AND R EKLAITIS (1983)
                Decomposed the problem into
                  1   Steam header selection and
                  2   Driver selection
                The overall objective was to minimize a linear combination of
                objective costs.
                No gas turbines and capital costs were considered.
I NTRODUCTION     T HERMODYNAMIC METHODS   O PTIMIZATION METHODS   C ARBON CONSTRAINED SCENARIO   S UMMARY



M ATH PROGRAMMING APPROACHES



      C OLMENARES AND S EIDER (1989)
                Developed an NLP model for synthesis of utility system
                Superstructure consists of cascade of Rankine cycles at
                different temperature levels.
                The overall objective was to minimize cost of the utility system.
                No gas turbines and electric motors were included in the
                superstructure.
I NTRODUCTION     T HERMODYNAMIC METHODS   O PTIMIZATION METHODS   C ARBON CONSTRAINED SCENARIO   S UMMARY



M ETAHEURISTIC APPROACHES



      M AIA ET AL . (1995)
                Simulated annealing approach for synthesis of utility system
                Superstructure is similar to Papoulias and Grossmann (1983).
                First attempt to include discrete equipement sizes in
                synthesis.
                Limitation of only one mechanical demand per drive.
                Costs and efficiency are obtained through continuous
                correlations.
I NTRODUCTION    T HERMODYNAMIC METHODS   O PTIMIZATION METHODS   C ARBON CONSTRAINED SCENARIO   S UMMARY



O UTLINE
       1   I NTRODUCTION
                The topic
                Boundary conditions and components
                Process Synthesis Methods
       2   T HERMODYNAMIC METHODS
                Early work
                Targeting methodologies
       3   O PTIMIZATION METHODS
                Background
                Early work
                Recent Trends in synthesis
       4   C ARBON CONSTRAINED SCENARIO
                CCS
                Bio-energy
       5   S UMMARY
I NTRODUCTION     T HERMODYNAMIC METHODS   O PTIMIZATION METHODS   C ARBON CONSTRAINED SCENARIO   S UMMARY


R ECENT TRENDS IN OPTIMAL SYNTHESIS OF UTILITY
SYSTEMS




      MINLP MODELS
                Bruno et al. (1998) extended the MILP model of Papoulias
                and Grossmann (1983) to develop an MINLP formulation.

      D ETAIL PROCESS UNIT MODELS
                Varbanov et al. (2004) developed detailed hardware models
                that were linearized and solved as a succession of MILPs.
I NTRODUCTION     T HERMODYNAMIC METHODS   O PTIMIZATION METHODS   C ARBON CONSTRAINED SCENARIO   S UMMARY


R ECENT TRENDS IN OPTIMAL SYNTHESIS OF UTILITY
SYSTEMS




      MINLP MODELS
                Bruno et al. (1998) extended the MILP model of Papoulias
                and Grossmann (1983) to develop an MINLP formulation.

      D ETAIL PROCESS UNIT MODELS
                Varbanov et al. (2004) developed detailed hardware models
                that were linearized and solved as a succession of MILPs.
I NTRODUCTION      T HERMODYNAMIC METHODS   O PTIMIZATION METHODS   C ARBON CONSTRAINED SCENARIO   S UMMARY



R ECENT TRENDS

      M ULTIPERIOD MODELS
                Iyer and Grossmann (1998) extended the Papoulias and Grossmann (1983)
                model to include mutiperiod operation.
                Maia and Qassim (1997) extended the work by Maia et al.(1995) to include
                multiperiod operation.
                Oliviera and Matos (2003) included environmental aspects when extending
                the work by Iyer and Grossmann (1998) and Maia and Qassim (1997).
                Frangopoulos and Dimopoulos (2004) used thermoeconomic optimization
                of multiperiod co-generation systems with a limited superstructure.
                Aguilar et al. (2005) proposed a MILP formulation of multi-period utility
                systems.
                Chen and Lin (2011) develop a steam distribution network for integration
                with chemical processes by adapting the transhipment model for flexible
                operation.
I NTRODUCTION     T HERMODYNAMIC METHODS   O PTIMIZATION METHODS   C ARBON CONSTRAINED SCENARIO   S UMMARY



R ECENT TRENDS


      I NCORPORATING OTHER CONSIDERATIONS SUCH AS
      AVAILABILITY ETC .
                Frangopoulos and Dimopoulos (2004) used thermoeconomic
                optimization of multiperiod co-generation systems and include
                availability costs in calculating the NPV.
                Aguilar et al. (2005) do not explicity include availability but
                including the degree of equipment redundancy during
                optimization phase.
                Del Nogal et al. (2010) present an rich superstructure and
                MILP formulation to synthesize utility systems including
                availability considerations.
I NTRODUCTION    T HERMODYNAMIC METHODS   O PTIMIZATION METHODS   C ARBON CONSTRAINED SCENARIO   S UMMARY



O UTLINE
       1   I NTRODUCTION
                The topic
                Boundary conditions and components
                Process Synthesis Methods
       2   T HERMODYNAMIC METHODS
                Early work
                Targeting methodologies
       3   O PTIMIZATION METHODS
                Background
                Early work
                Recent Trends in synthesis
       4   C ARBON CONSTRAINED SCENARIO
                CCS
                Bio-energy
       5   S UMMARY
I NTRODUCTION     T HERMODYNAMIC METHODS   O PTIMIZATION METHODS   C ARBON CONSTRAINED SCENARIO   S UMMARY


P OWER AND STEAM PLANTS IN A CARBON
CONSTRAINED SCENARIO




      C ARBON C APTURE AND S TORAGE
                Fossil fuel based utility plants would require CCS.
                Inclusion of CCS would mean addition of a chemical process
                facility in the utility system.
                Tight integration required between the different components to
                reduce efficiency penalty.
I NTRODUCTION   T HERMODYNAMIC METHODS   O PTIMIZATION METHODS   C ARBON CONSTRAINED SCENARIO   S UMMARY


C ARBON CONSTRAINED SCENARIO
C ARBON C APTURE AND S TORAGE

      M ARTELLI ET AL . (2011) AND M ARTELLI ET AL . (2012)
      Two step optimization procedure for optimal design of heat
      recovery steam generator including external heat addition and
      extraction.
I NTRODUCTION   T HERMODYNAMIC METHODS   O PTIMIZATION METHODS   C ARBON CONSTRAINED SCENARIO   S UMMARY


C ARBON CONSTRAINED SCENARIO
C ARBON C APTURE AND S TORAGE




      L IU ET AL . (2009, 2010)
      A MINLP framework for the synthesis of optimum poly-generation
      plants using coal as fuel.
I NTRODUCTION   T HERMODYNAMIC METHODS   O PTIMIZATION METHODS   C ARBON CONSTRAINED SCENARIO   S UMMARY


C ARBON CONSTRAINED SCENARIO
C ARBON C APTURE AND S TORAGE



      A NANTHARAMAN AND B ERSTAD (2011)
      A MILP framework for generation of optimal integration schemes
      for post-combustion CO2 capture unit with NGCC power plant.
I NTRODUCTION   T HERMODYNAMIC METHODS   O PTIMIZATION METHODS   C ARBON CONSTRAINED SCENARIO   S UMMARY


C ARBON CONSTRAINED SCENARIO
C ARBON C APTURE AND S TORAGE


      A NANTHARAMAN AND B ERSTAD (2011)
      A MILP framework for generation of optimal integration schemes
      for post-combustion CO2 capture unit with NGCC power plant.
I NTRODUCTION   T HERMODYNAMIC METHODS   O PTIMIZATION METHODS   C ARBON CONSTRAINED SCENARIO   S UMMARY


C ARBON CONSTRAINED SCENARIO
C ARBON C APTURE AND S TORAGE


      J OHNSEN , E. (2011)
      A MINLP framework for generation of optimal synthesis of an
      air-blown Integrated Reforming Combined Cycle power plant using
      meta-models.
I NTRODUCTION   T HERMODYNAMIC METHODS   O PTIMIZATION METHODS   C ARBON CONSTRAINED SCENARIO   S UMMARY


C ARBON CONSTRAINED SCENARIO
C ARBON C APTURE AND S TORAGE


      J OHNSEN , E. (2011)
      A MINLP framework for generation of optimal synthesis of an
      air-blown Integrated Reforming Combined Cycle power plant using
      meta-models.
I NTRODUCTION    T HERMODYNAMIC METHODS   O PTIMIZATION METHODS   C ARBON CONSTRAINED SCENARIO   S UMMARY



O UTLINE
       1   I NTRODUCTION
                The topic
                Boundary conditions and components
                Process Synthesis Methods
       2   T HERMODYNAMIC METHODS
                Early work
                Targeting methodologies
       3   O PTIMIZATION METHODS
                Background
                Early work
                Recent Trends in synthesis
       4   C ARBON CONSTRAINED SCENARIO
                CCS
                Bio-energy
       5   S UMMARY
I NTRODUCTION     T HERMODYNAMIC METHODS   O PTIMIZATION METHODS   C ARBON CONSTRAINED SCENARIO   S UMMARY


P OWER AND STEAM PLANTS IN A CARBON
CONSTRAINED SCENARIO



      B IO - ENERGY
                CHP plants fired with biomass, MSW etc.
                The superstructure involved for biomass based CHP will be
                extensive:
                     Selection of biomass
                     Preparation of fuel
                     Fuel/energy conversion system
                     Integration with gas turbine systems
                No significant development in the systematic approach to the
                design of biomass based CHP systems.
I NTRODUCTION      T HERMODYNAMIC METHODS   O PTIMIZATION METHODS   C ARBON CONSTRAINED SCENARIO   S UMMARY



S UMMARY

                Synthesis of combined heat and power plants or utility plants is a mature
                area of research.
                Thermodynamic based targeting methods for co-generation have been
                developed.
                No thermodynamic based systematic synthesis methodology in the
                literature.
                Mathematical programming methods where an exhaustive superstructure is
                used to synthesize utility networks dominate literature.
                Most of these models are formulated as MILPs.
                Recent developments include multiperiod optimization models and
                incorporating availability consideration in the design phase.
                In a carbon constrained scenario, novel methods to synthsize power and
                steam systems with CCS need to be developed further.
                Systematic methods for the optimal synthesis of biomass based CHP
                needs development.
I NTRODUCTION      T HERMODYNAMIC METHODS   O PTIMIZATION METHODS   C ARBON CONSTRAINED SCENARIO   S UMMARY



S UMMARY

                Synthesis of combined heat and power plants or utility plants is a mature
                area of research.
                Thermodynamic based targeting methods for co-generation have been
                developed.
                No thermodynamic based systematic synthesis methodology in the
                literature.
                Mathematical programming methods where an exhaustive superstructure is
                used to synthesize utility networks dominate literature.
                Most of these models are formulated as MILPs.
                Recent developments include multiperiod optimization models and
                incorporating availability consideration in the design phase.
                In a carbon constrained scenario, novel methods to synthsize power and
                steam systems with CCS need to be developed further.
                Systematic methods for the optimal synthesis of biomass based CHP
                needs development.
I NTRODUCTION      T HERMODYNAMIC METHODS   O PTIMIZATION METHODS   C ARBON CONSTRAINED SCENARIO   S UMMARY



S UMMARY

                Synthesis of combined heat and power plants or utility plants is a mature
                area of research.
                Thermodynamic based targeting methods for co-generation have been
                developed.
                No thermodynamic based systematic synthesis methodology in the
                literature.
                Mathematical programming methods where an exhaustive superstructure is
                used to synthesize utility networks dominate literature.
                Most of these models are formulated as MILPs.
                Recent developments include multiperiod optimization models and
                incorporating availability consideration in the design phase.
                In a carbon constrained scenario, novel methods to synthsize power and
                steam systems with CCS need to be developed further.
                Systematic methods for the optimal synthesis of biomass based CHP
                needs development.
I NTRODUCTION      T HERMODYNAMIC METHODS   O PTIMIZATION METHODS   C ARBON CONSTRAINED SCENARIO   S UMMARY



S UMMARY

                Synthesis of combined heat and power plants or utility plants is a mature
                area of research.
                Thermodynamic based targeting methods for co-generation have been
                developed.
                No thermodynamic based systematic synthesis methodology in the
                literature.
                Mathematical programming methods where an exhaustive superstructure is
                used to synthesize utility networks dominate literature.
                Most of these models are formulated as MILPs.
                Recent developments include multiperiod optimization models and
                incorporating availability consideration in the design phase.
                In a carbon constrained scenario, novel methods to synthsize power and
                steam systems with CCS need to be developed further.
                Systematic methods for the optimal synthesis of biomass based CHP
                needs development.
I NTRODUCTION      T HERMODYNAMIC METHODS   O PTIMIZATION METHODS   C ARBON CONSTRAINED SCENARIO   S UMMARY



S UMMARY

                Synthesis of combined heat and power plants or utility plants is a mature
                area of research.
                Thermodynamic based targeting methods for co-generation have been
                developed.
                No thermodynamic based systematic synthesis methodology in the
                literature.
                Mathematical programming methods where an exhaustive superstructure is
                used to synthesize utility networks dominate literature.
                Most of these models are formulated as MILPs.
                Recent developments include multiperiod optimization models and
                incorporating availability consideration in the design phase.
                In a carbon constrained scenario, novel methods to synthsize power and
                steam systems with CCS need to be developed further.
                Systematic methods for the optimal synthesis of biomass based CHP
                needs development.
I NTRODUCTION      T HERMODYNAMIC METHODS   O PTIMIZATION METHODS   C ARBON CONSTRAINED SCENARIO   S UMMARY



S UMMARY

                Synthesis of combined heat and power plants or utility plants is a mature
                area of research.
                Thermodynamic based targeting methods for co-generation have been
                developed.
                No thermodynamic based systematic synthesis methodology in the
                literature.
                Mathematical programming methods where an exhaustive superstructure is
                used to synthesize utility networks dominate literature.
                Most of these models are formulated as MILPs.
                Recent developments include multiperiod optimization models and
                incorporating availability consideration in the design phase.
                In a carbon constrained scenario, novel methods to synthsize power and
                steam systems with CCS need to be developed further.
                Systematic methods for the optimal synthesis of biomass based CHP
                needs development.
I NTRODUCTION      T HERMODYNAMIC METHODS   O PTIMIZATION METHODS   C ARBON CONSTRAINED SCENARIO   S UMMARY



S UMMARY

                Synthesis of combined heat and power plants or utility plants is a mature
                area of research.
                Thermodynamic based targeting methods for co-generation have been
                developed.
                No thermodynamic based systematic synthesis methodology in the
                literature.
                Mathematical programming methods where an exhaustive superstructure is
                used to synthesize utility networks dominate literature.
                Most of these models are formulated as MILPs.
                Recent developments include multiperiod optimization models and
                incorporating availability consideration in the design phase.
                In a carbon constrained scenario, novel methods to synthsize power and
                steam systems with CCS need to be developed further.
                Systematic methods for the optimal synthesis of biomass based CHP
                needs development.
I NTRODUCTION      T HERMODYNAMIC METHODS   O PTIMIZATION METHODS   C ARBON CONSTRAINED SCENARIO   S UMMARY



S UMMARY

                Synthesis of combined heat and power plants or utility plants is a mature
                area of research.
                Thermodynamic based targeting methods for co-generation have been
                developed.
                No thermodynamic based systematic synthesis methodology in the
                literature.
                Mathematical programming methods where an exhaustive superstructure is
                used to synthesize utility networks dominate literature.
                Most of these models are formulated as MILPs.
                Recent developments include multiperiod optimization models and
                incorporating availability consideration in the design phase.
                In a carbon constrained scenario, novel methods to synthsize power and
                steam systems with CCS need to be developed further.
                Systematic methods for the optimal synthesis of biomass based CHP
                needs development.
I NTRODUCTION    T HERMODYNAMIC METHODS               O PTIMIZATION METHODS       C ARBON CONSTRAINED SCENARIO               S UMMARY



R EFERENCES I

            O Aguilar, S Perry, J Kim, and R Smith.
            Design and Optimization of Flexible Utility Systems Subject to Variable ConditionsPart 1: Modelling Framework.
            Chemical Engineering Research and Design, 85(8):1136–1148, 2007.

            J Bruno, F Fernandez, F Castells, and I.E. Grossmann.
            A Rigorous MINLP Model for the Optimal Synthesis and Operation of Utility Plants.
            Chemical Engineering Research and Design, 76(3):246–258, March 1998.

            C.T. Chang and J.R. Hwang.
            A multiobjective programming approach to waste minimization in the utility systems of chemical processes.
            Chemical Engineering Science, 51(16):3951–3965, August 1996.

            C.L. Chen and C.Y. Lin.
            A flexible structural and operational design of steam systems.
            Applied Thermal Engineering, 31(13):2084–2093, September 2011.

            C.C. Chou and Y.S. Shih.
            A thermodynamic approach to the design and synthesis of plant utility systems.
            Industrial & Engineering Chemistry Research, 26(6):1100–1108, June 1987.

            T.R. Colmenares and W.D. Seider.
            Synthesis of utility systems integrated with chemical processes.
            Industrial & Engineering Chemistry Research, 28(1):84–93, January 1989.

            F.L. Del Nogal, J.K. Kim, S. Perry, and R. Smith.
            Synthesis of mechanical driver and power generation configurations, Part 1: Optimization framework.
            AIChE Journal, pages NA–NA, 2010.
I NTRODUCTION    T HERMODYNAMIC METHODS               O PTIMIZATION METHODS         C ARBON CONSTRAINED SCENARIO            S UMMARY



R EFERENCES II

            V.R. Dhole and B. Linnhoff.
            Total site targets for fuel, co-generation, emissions, and cooling.
            Computers & Chemical Engineering, 17:S101–S109, 1993.

            M. El-Halwagi, D. Harell, and H. Dennis Spriggs.
            Targeting cogeneration and waste utilization through process integration.
            Applied Energy, 86(6):880–887, June 2009.

            C.A. Frangopoulos and G.G. Dimopoulos.
            Effect of reliability considerations on the optimal synthesis, design and operation of a cogeneration system.
            Energy, 29(3):309–329, March 2004.

            R.R. Iyer and I.E. Grossmann.
            Optimal multiperiod operational planning for utility systems.
            Computers & Chemical Engineering, 21(8):787–800, 1997.

            J. Klemeš, V.R. Dhole, K. Raissi, S.J. Perry, and L. Puigjaner.
            Targeting and design methodology for reduction of fuel, power and CO2 on total sites.
            Applied Thermal Engineering, 17(8-10):993–1003, August 1997.

            B. Linnhoff and V.R. Dhole.
            Targeting for CO2 emissions for Total Sites.
            Chemical Engineering & Technology, 16(4):252–259, August 1993.

            P. Liu, M.C. Georgiadis, and E.N. Pistikopoulos.
            Advances in Energy Systems Engineering.
            Industrial & Engineering Chemistry Research, page 100917092426020, September 2010.
I NTRODUCTION    T HERMODYNAMIC METHODS             O PTIMIZATION METHODS           C ARBON CONSTRAINED SCENARIO        S UMMARY



R EFERENCES III

            P. Liu, E. Pistikopoulos, and Z. Li.
            A mixed-integer optimization approach for polygeneration energy systems design.
            Computers & Chemical Engineering, 33(3):759–768, March 2009.

            F. Marechal and B. Kalitventzeff.
            Process integration : Selection optimal utility system .
            Computers & Chemical Engineering, 22(Suppl):S149–156, 1998.

            S.P Mavromatis and A.C Kokossis.
            Hardware composites: A new conceptual tool for the analysis and optimisation of steam turbine networks in
            chemical process industries.
            Chemical Engineering Science, 53(7):1405–1434, March 1998.

            L.O. Maia, L. Vidal de Carvalho, and R.Y. Qassim.
            Synthesis of utility systems by simulated annealing.
            Computers & Chemical Engineering, 19(4):481–488, April 1995.

            M. Nishio, J. Itoh, K. Shiroko, and T. Umeda.
            A Thermodynamic Approach to Steam-Power System Design.
            Industrial & Engineering Chemistry Process Design and Development, 19(2):306–312, April 1980.

            M. Nishio and A.I. Johnson.
            Stratergy for energy system expansion.
            Chemical Engineering Progress, 73:75, 1979.

            S. Papoulias and I.E. Grossmann.
            A structural optimization approach in process synthesisâI Utility systems.
            Computers & Chemical Engineering, 7(6):695–706, 1983.
I NTRODUCTION    T HERMODYNAMIC METHODS               O PTIMIZATION METHODS             C ARBON CONSTRAINED SCENARIO   S UMMARY



R EFERENCES IV


            T. Petroulas and G. V. Reklaitis.
            Computer-aided synthesis and design of plant utility systems.
            AIChE Journal, 30(1):69–78, January 1984.

            V Papandreou and Z Shang.
            A multi-criteria optimisation approach for the design of sustainable utility systems.
            Computers & Chemical Engineering, 32(7):1589–1602, July 2008.

            Z. Shang and A. Kokossis.
            A systematic approach to the synthesis and design of flexible site utility systems.
            Chemical Engineering Science, 60(16):4431–4451, August 2005.

            P. Varbanov, S. Doyle, and R. Smith.
            Modelling and Optimization of Utility Systems.
            Chemical Engineering Research and Design, 82(5):561–578, May 2004.

            P. Varbanov, S. Perry, J. Klemeš, and R. Smith.
            Synthesis of industrial utility systems: cost-effective de-carbonisation.
            Applied Thermal Engineering, 25(7):985–1001, May 2005.

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Optimal synthesis of steam and power plants

  • 1. I NTRODUCTION T HERMODYNAMIC METHODS O PTIMIZATION METHODS C ARBON CONSTRAINED SCENARIO S UMMARY O PTIMAL SYNTHESIS OF STEAM AND POWER PLANTS Rahul Anantharaman Department of Energy & Process Engineering Norwegian University of Science and Technology PhD Trial Lecture Trondheim, 06.12.2011
  • 2. I NTRODUCTION T HERMODYNAMIC METHODS O PTIMIZATION METHODS C ARBON CONSTRAINED SCENARIO S UMMARY O UTLINE 1 I NTRODUCTION The topic Boundary conditions and components Process Synthesis Methods 2 T HERMODYNAMIC METHODS Early work Targeting methodologies 3 O PTIMIZATION METHODS Background Early work Recent Trends in synthesis 4 C ARBON CONSTRAINED SCENARIO CCS Bio-energy 5 S UMMARY
  • 3. I NTRODUCTION T HERMODYNAMIC METHODS O PTIMIZATION METHODS C ARBON CONSTRAINED SCENARIO S UMMARY O UTLINE 1 I NTRODUCTION The topic Boundary conditions and components Process Synthesis Methods 2 T HERMODYNAMIC METHODS Early work Targeting methodologies 3 O PTIMIZATION METHODS Background Early work Recent Trends in synthesis 4 C ARBON CONSTRAINED SCENARIO CCS Bio-energy 5 S UMMARY
  • 4. I NTRODUCTION T HERMODYNAMIC METHODS O PTIMIZATION METHODS C ARBON CONSTRAINED SCENARIO S UMMARY T HE TOPIC AND MY INTEPRETATION Optimal Synthesis of Steam and Power Plants
  • 5. I NTRODUCTION T HERMODYNAMIC METHODS O PTIMIZATION METHODS C ARBON CONSTRAINED SCENARIO S UMMARY T HE TOPIC AND MY INTEPRETATION Optimal Synthesis of Steam and Power Plants
  • 6. I NTRODUCTION T HERMODYNAMIC METHODS O PTIMIZATION METHODS C ARBON CONSTRAINED SCENARIO S UMMARY T HE TOPIC AND MY INTEPRETATION Optimal Synthesis of Steam and Power Plants
  • 7. I NTRODUCTION T HERMODYNAMIC METHODS O PTIMIZATION METHODS C ARBON CONSTRAINED SCENARIO S UMMARY T HE TOPIC AND MY INTEPRETATION Optimal Synthesis of Steam and Power Plants
  • 8. I NTRODUCTION T HERMODYNAMIC METHODS O PTIMIZATION METHODS C ARBON CONSTRAINED SCENARIO S UMMARY T HE TOPIC AND MY INTEPRETATION Optimal Synthesis of Steam and Power Plants
  • 9. I NTRODUCTION T HERMODYNAMIC METHODS O PTIMIZATION METHODS C ARBON CONSTRAINED SCENARIO S UMMARY O UTLINE 1 I NTRODUCTION The topic Boundary conditions and components Process Synthesis Methods 2 T HERMODYNAMIC METHODS Early work Targeting methodologies 3 O PTIMIZATION METHODS Background Early work Recent Trends in synthesis 4 C ARBON CONSTRAINED SCENARIO CCS Bio-energy 5 S UMMARY
  • 10. I NTRODUCTION T HERMODYNAMIC METHODS O PTIMIZATION METHODS C ARBON CONSTRAINED SCENARIO S UMMARY C OMBINED H EAT AND P OWER (CHP) PLANT
  • 11. I NTRODUCTION T HERMODYNAMIC METHODS O PTIMIZATION METHODS C ARBON CONSTRAINED SCENARIO S UMMARY C OMBINED H EAT AND P OWER (CHP) PLANT
  • 12. I NTRODUCTION T HERMODYNAMIC METHODS O PTIMIZATION METHODS C ARBON CONSTRAINED SCENARIO S UMMARY P RIME MOVER T YPICAL CHARACTERISTICS Gas Micro- Reciprocating Steam Fuel turbine turbine engine turbine cell NG, biogas NG, biogas NG, biogas H2 , NG, Fuel propane, propane, propane, all propane, oil oil diesel methanol Use for thermal Heat, HW, Heat, HW, HW, LP steam LP-HP steam HW, LP* steam output LP-HP steam LP steam Power to Heat 0.5-2 0.4-0.7 0.5-1 0.1-0.3 1-2 ratio Typical 0.5-250 0.03-0.25 0.01-5 0.5-250 0.005-2 capacity (MWe)
  • 13. I NTRODUCTION T HERMODYNAMIC METHODS O PTIMIZATION METHODS C ARBON CONSTRAINED SCENARIO S UMMARY C OMBINED H EAT AND P OWER (CHP) PLANT
  • 14. I NTRODUCTION T HERMODYNAMIC METHODS O PTIMIZATION METHODS C ARBON CONSTRAINED SCENARIO S UMMARY C OMBINED H EAT AND P OWER (CHP) PLANT
  • 15. I NTRODUCTION T HERMODYNAMIC METHODS O PTIMIZATION METHODS C ARBON CONSTRAINED SCENARIO S UMMARY C OMBINED H EAT AND P OWER (CHP) PLANT
  • 16. I NTRODUCTION T HERMODYNAMIC METHODS O PTIMIZATION METHODS C ARBON CONSTRAINED SCENARIO S UMMARY OTHER COMPONENTS IN THE CHP SYSTEM Boilers for steam generation Waste heat boilers for steam generation Generators for conversion of power to electricity Electric motors as mechanical drivers (in addition to gas and steam turbines)
  • 17. I NTRODUCTION T HERMODYNAMIC METHODS O PTIMIZATION METHODS C ARBON CONSTRAINED SCENARIO S UMMARY O UTLINE 1 I NTRODUCTION The topic Boundary conditions and components Process Synthesis Methods 2 T HERMODYNAMIC METHODS Early work Targeting methodologies 3 O PTIMIZATION METHODS Background Early work Recent Trends in synthesis 4 C ARBON CONSTRAINED SCENARIO CCS Bio-energy 5 S UMMARY
  • 18. I NTRODUCTION T HERMODYNAMIC METHODS O PTIMIZATION METHODS C ARBON CONSTRAINED SCENARIO S UMMARY P ROCESS S YNTHESIS Process synthesis is the systematic generation of alternative process flowsheets and selection of a design whose configuration and parameters optimize a given objective function.
  • 19. I NTRODUCTION T HERMODYNAMIC METHODS O PTIMIZATION METHODS C ARBON CONSTRAINED SCENARIO S UMMARY T HERMODYNAMIC METHODS A NOTE The two products from a CHP or utility system power and heat. First law analysis where heat and work are equivalent is not sufficient. Second law analysis required for consistent evaluation and consideration of both products in a systematic way. E XERGY BASED APPROACH TO THERMODYNAMIC ANALYSIS .
  • 20. I NTRODUCTION T HERMODYNAMIC METHODS O PTIMIZATION METHODS C ARBON CONSTRAINED SCENARIO S UMMARY O UTLINE 1 I NTRODUCTION The topic Boundary conditions and components Process Synthesis Methods 2 T HERMODYNAMIC METHODS Early work Targeting methodologies 3 O PTIMIZATION METHODS Background Early work Recent Trends in synthesis 4 C ARBON CONSTRAINED SCENARIO CCS Bio-energy 5 S UMMARY
  • 21. I NTRODUCTION T HERMODYNAMIC METHODS O PTIMIZATION METHODS C ARBON CONSTRAINED SCENARIO S UMMARY T HERMODYNAMICS - BASED H EURISTIC METHODS N ISHIO AND J OHNSON (1979), N ISHIO ET. AL . (1980) Introduced a number of thermodynamic-based heuristics for reducing the loss of available energy in steam cycles. Developed Heuristics for preliminary selection of energy conservation and power generation technologies. Two-step approach that differentiated between steam dominant and power dominant cases. Linear Program for allocation of drivers. C HOU AND S HIH (1987) Similar approach to Nishio et. al. (1982). Included gas turbine and combined gas-steam cycles. Five step procedure for designing the system starts with screening based on P/H ratio.
  • 22. I NTRODUCTION T HERMODYNAMIC METHODS O PTIMIZATION METHODS C ARBON CONSTRAINED SCENARIO S UMMARY T HERMODYNAMICS - BASED H EURISTIC METHODS N ISHIO AND J OHNSON (1979), N ISHIO ET. AL . (1980) Introduced a number of thermodynamic-based heuristics for reducing the loss of available energy in steam cycles. Developed Heuristics for preliminary selection of energy conservation and power generation technologies. Two-step approach that differentiated between steam dominant and power dominant cases. Linear Program for allocation of drivers. C HOU AND S HIH (1987) Similar approach to Nishio et. al. (1982). Included gas turbine and combined gas-steam cycles. Five step procedure for designing the system starts with screening based on P/H ratio.
  • 23. I NTRODUCTION T HERMODYNAMIC METHODS O PTIMIZATION METHODS C ARBON CONSTRAINED SCENARIO S UMMARY O UTLINE 1 I NTRODUCTION The topic Boundary conditions and components Process Synthesis Methods 2 T HERMODYNAMIC METHODS Early work Targeting methodologies 3 O PTIMIZATION METHODS Background Early work Recent Trends in synthesis 4 C ARBON CONSTRAINED SCENARIO CCS Bio-energy 5 S UMMARY
  • 24. I NTRODUCTION T HERMODYNAMIC METHODS O PTIMIZATION METHODS C ARBON CONSTRAINED SCENARIO S UMMARY TARGETS FOR COGENERATION E XTENSION OF P INCH A NALYSIS D HOLE AND L INNHOFF (1993) AND L INNHOFF AND D HOLE (1993) Extended Pinch Analysis for total site wide targets for fuel, co-generation and emissions. Site Source-Sink Profiles (SSSP) for site level targeting. First systematic thermodynamic method for targeting co-generation. Only boilers and steam turbine systems are included. No detail design method proposed. Methodology extended in Raissi (1994) and developed the TH-shaftwork targeting model. The methodology extended by Bandyopadhyay et al. (2010) to generate Site level Grand Composite Curves (SGCC) to include indirect heat transfer.
  • 25. I NTRODUCTION T HERMODYNAMIC METHODS O PTIMIZATION METHODS C ARBON CONSTRAINED SCENARIO S UMMARY TARGETS FOR COGENERATION E XTENSION OF P INCH A NALYSIS D HOLE AND L INNHOFF (1993) AND L INNHOFF AND D HOLE (1993) Extended Pinch Analysis for total site wide targets for fuel, co-generation and emissions. Site Source-Sink Profiles (SSSP) for site level targeting. First systematic thermodynamic method for targeting co-generation. Only boilers and steam turbine systems are included. No detail design method proposed. Methodology extended in Raissi (1994) and developed the TH-shaftwork targeting model. The methodology extended by Bandyopadhyay et al. (2010) to generate Site level Grand Composite Curves (SGCC) to include indirect heat transfer.
  • 26. I NTRODUCTION T HERMODYNAMIC METHODS O PTIMIZATION METHODS C ARBON CONSTRAINED SCENARIO S UMMARY TARGETS FOR COGENERATION E XTENSION OF P INCH A NALYSIS D HOLE AND L INNHOFF (1993) AND L INNHOFF AND D HOLE (1993) Extended Pinch Analysis for total site wide targets for fuel, co-generation and emissions. Site Source-Sink Profiles (SSSP) for site level targeting. First systematic thermodynamic method for targeting co-generation. Only boilers and steam turbine systems are included. No detail design method proposed. Methodology extended in Raissi (1994) and developed the TH-shaftwork targeting model. The methodology extended by Bandyopadhyay et al. (2010) to generate Site level Grand Composite Curves (SGCC) to include indirect heat transfer.
  • 27. I NTRODUCTION T HERMODYNAMIC METHODS O PTIMIZATION METHODS C ARBON CONSTRAINED SCENARIO S UMMARY TARGETS FOR COGENERATION E XTENSION OF P INCH A NALYSIS D HOLE AND L INNHOFF (1993) AND L INNHOFF AND D HOLE (1993) Extended Pinch Analysis for total site wide targets for fuel, co-generation and emissions. Site Source-Sink Profiles (SSSP) for site level targeting. First systematic thermodynamic method for targeting co-generation. Only boilers and steam turbine systems are included. No detail design method proposed. Methodology extended in Raissi (1994) and developed the TH-shaftwork targeting model. The methodology extended by Bandyopadhyay et al. (2010) to generate Site level Grand Composite Curves (SGCC) to include indirect heat transfer.
  • 28. I NTRODUCTION T HERMODYNAMIC METHODS O PTIMIZATION METHODS C ARBON CONSTRAINED SCENARIO S UMMARY TARGETS FOR COGENERATION E XTENSION OF P INCH A NALYSIS D HOLE AND L INNHOFF (1993) AND L INNHOFF AND D HOLE (1993) Extended Pinch Analysis for total site wide targets for fuel, co-generation and emissions. Site Source-Sink Profiles (SSSP) for site level targeting. First systematic thermodynamic method for targeting co-generation. Only boilers and steam turbine systems are included. No detail design method proposed. Methodology extended in Raissi (1994) and developed the TH-shaftwork targeting model. The methodology extended by Bandyopadhyay et al. (2010) to generate Site level Grand Composite Curves (SGCC) to include indirect heat transfer.
  • 29. I NTRODUCTION T HERMODYNAMIC METHODS O PTIMIZATION METHODS C ARBON CONSTRAINED SCENARIO S UMMARY TARGETS FOR COGENERATION E XTENSION OF P INCH A NALYSIS D HOLE AND L INNHOFF (1993) AND L INNHOFF AND D HOLE (1993) Extended Pinch Analysis for total site wide targets for fuel, co-generation and emissions. Site Source-Sink Profiles (SSSP) for site level targeting. First systematic thermodynamic method for targeting co-generation. Only boilers and steam turbine systems are included. No detail design method proposed. Methodology extended in Raissi (1994) and developed the TH-shaftwork targeting model. The methodology extended by Bandyopadhyay et al. (2010) to generate Site level Grand Composite Curves (SGCC) to include indirect heat transfer.
  • 30. I NTRODUCTION T HERMODYNAMIC METHODS O PTIMIZATION METHODS C ARBON CONSTRAINED SCENARIO S UMMARY TARGETS FOR COGENERATION E XTENSION OF P INCH A NALYSIS D HOLE AND L INNHOFF (1993) AND L INNHOFF AND D HOLE (1993) Extended Pinch Analysis for total site wide targets for fuel, co-generation and emissions. Site Source-Sink Profiles (SSSP) for site level targeting. First systematic thermodynamic method for targeting co-generation. Only boilers and steam turbine systems are included. No detail design method proposed. Methodology extended in Raissi (1994) and developed the TH-shaftwork targeting model. The methodology extended by Bandyopadhyay et al. (2010) to generate Site level Grand Composite Curves (SGCC) to include indirect heat transfer.
  • 31. I NTRODUCTION T HERMODYNAMIC METHODS O PTIMIZATION METHODS C ARBON CONSTRAINED SCENARIO S UMMARY TARGETS FOR COGENERATION D HOLE AND L INNHOFF (1993)
  • 32. I NTRODUCTION T HERMODYNAMIC METHODS O PTIMIZATION METHODS C ARBON CONSTRAINED SCENARIO S UMMARY TARGETS FOR COGENERATION D HOLE AND L INNHOFF (1993)
  • 33. I NTRODUCTION T HERMODYNAMIC METHODS O PTIMIZATION METHODS C ARBON CONSTRAINED SCENARIO S UMMARY TARGETS FOR COGENERATION D HOLE AND L INNHOFF (1993)
  • 34. I NTRODUCTION T HERMODYNAMIC METHODS O PTIMIZATION METHODS C ARBON CONSTRAINED SCENARIO S UMMARY TARGETS FOR COGENERATION D HOLE AND L INNHOFF (1993)
  • 35. I NTRODUCTION T HERMODYNAMIC METHODS O PTIMIZATION METHODS C ARBON CONSTRAINED SCENARIO S UMMARY TARGETS FOR COGENERATION E XTRACTABLE POWER SURPLUS COMPOSITE CURVE E L -H ALWAGI ET AL . (2009) Targets for cogeneration given a set of combustible wastes and byproducts, heating cooling demands, non-heating steam demands. Using standard mass and heat integration procedures to identify process steam requirement and generation potential. New concept of extractable energy ˙ e = ηH Extractable power surplus composite curve targets for cogeneration potential. Only boilers and steam turbine systems are included. No detail design method proposed.
  • 36. I NTRODUCTION T HERMODYNAMIC METHODS O PTIMIZATION METHODS C ARBON CONSTRAINED SCENARIO S UMMARY TARGETS FOR COGENERATION E XTRACTABLE POWER SURPLUS COMPOSITE CURVE E L -H ALWAGI ET AL . (2009) Targets for cogeneration given a set of combustible wastes and byproducts, heating cooling demands, non-heating steam demands. Using standard mass and heat integration procedures to identify process steam requirement and generation potential. New concept of extractable energy ˙ e = ηH Extractable power surplus composite curve targets for cogeneration potential. Only boilers and steam turbine systems are included. No detail design method proposed.
  • 37. I NTRODUCTION T HERMODYNAMIC METHODS O PTIMIZATION METHODS C ARBON CONSTRAINED SCENARIO S UMMARY TARGETS FOR COGENERATION E XTRACTABLE POWER SURPLUS COMPOSITE CURVE E L -H ALWAGI ET AL . (2009) Targets for cogeneration given a set of combustible wastes and byproducts, heating cooling demands, non-heating steam demands. Using standard mass and heat integration procedures to identify process steam requirement and generation potential. New concept of extractable energy ˙ e = ηH Extractable power surplus composite curve targets for cogeneration potential. Only boilers and steam turbine systems are included. No detail design method proposed.
  • 38. I NTRODUCTION T HERMODYNAMIC METHODS O PTIMIZATION METHODS C ARBON CONSTRAINED SCENARIO S UMMARY TARGETS FOR COGENERATION E XTRACTABLE POWER SURPLUS COMPOSITE CURVE E L -H ALWAGI ET AL . (2009) Targets for cogeneration given a set of combustible wastes and byproducts, heating cooling demands, non-heating steam demands. Using standard mass and heat integration procedures to identify process steam requirement and generation potential. New concept of extractable energy ˙ e = ηH Extractable power surplus composite curve targets for cogeneration potential. Only boilers and steam turbine systems are included. No detail design method proposed.
  • 39. I NTRODUCTION T HERMODYNAMIC METHODS O PTIMIZATION METHODS C ARBON CONSTRAINED SCENARIO S UMMARY TARGETS FOR COGENERATION E XTRACTABLE POWER SURPLUS COMPOSITE CURVE E L -H ALWAGI ET AL . (2009) Targets for cogeneration given a set of combustible wastes and byproducts, heating cooling demands, non-heating steam demands. Using standard mass and heat integration procedures to identify process steam requirement and generation potential. New concept of extractable energy ˙ e = ηH Extractable power surplus composite curve targets for cogeneration potential. Only boilers and steam turbine systems are included. No detail design method proposed.
  • 40. I NTRODUCTION T HERMODYNAMIC METHODS O PTIMIZATION METHODS C ARBON CONSTRAINED SCENARIO S UMMARY TARGETS FOR COGENERATION E XTRACTABLE POWER SURPLUS COMPOSITE CURVE E L -H ALWAGI ET AL . (2009) Targets for cogeneration given a set of combustible wastes and byproducts, heating cooling demands, non-heating steam demands. Using standard mass and heat integration procedures to identify process steam requirement and generation potential. New concept of extractable energy ˙ e = ηH Extractable power surplus composite curve targets for cogeneration potential. Only boilers and steam turbine systems are included. No detail design method proposed.
  • 41. I NTRODUCTION T HERMODYNAMIC METHODS O PTIMIZATION METHODS C ARBON CONSTRAINED SCENARIO S UMMARY TARGETS FOR COGENERATION E L -H ALWAGI ET AL . (2009)
  • 42. I NTRODUCTION T HERMODYNAMIC METHODS O PTIMIZATION METHODS C ARBON CONSTRAINED SCENARIO S UMMARY TARGETS FOR COGENERATION E L -H ALWAGI ET AL . (2009)
  • 43. I NTRODUCTION T HERMODYNAMIC METHODS O PTIMIZATION METHODS C ARBON CONSTRAINED SCENARIO S UMMARY TARGETS FOR COGENERATION E L -H ALWAGI ET AL . (2009)
  • 44. I NTRODUCTION T HERMODYNAMIC METHODS O PTIMIZATION METHODS C ARBON CONSTRAINED SCENARIO S UMMARY TARGETS FOR COGENERATION E L -H ALWAGI ET AL . (2009)
  • 45. I NTRODUCTION T HERMODYNAMIC METHODS O PTIMIZATION METHODS C ARBON CONSTRAINED SCENARIO S UMMARY O UTLINE 1 I NTRODUCTION The topic Boundary conditions and components Process Synthesis Methods 2 T HERMODYNAMIC METHODS Early work Targeting methodologies 3 O PTIMIZATION METHODS Background Early work Recent Trends in synthesis 4 C ARBON CONSTRAINED SCENARIO CCS Bio-energy 5 S UMMARY
  • 46. I NTRODUCTION T HERMODYNAMIC METHODS O PTIMIZATION METHODS C ARBON CONSTRAINED SCENARIO S UMMARY O PTIMIZATION DESIGN SPACE El-Sayed Y.M. (2003)
  • 47. I NTRODUCTION T HERMODYNAMIC METHODS O PTIMIZATION METHODS C ARBON CONSTRAINED SCENARIO S UMMARY O PTIMIZATION DESIGN SPACE El-Sayed Y.M. (2003)
  • 48. I NTRODUCTION T HERMODYNAMIC METHODS O PTIMIZATION METHODS C ARBON CONSTRAINED SCENARIO S UMMARY O PTIMIZATION DESIGN SPACE El-Sayed Y.M. (2003)
  • 49. I NTRODUCTION T HERMODYNAMIC METHODS O PTIMIZATION METHODS C ARBON CONSTRAINED SCENARIO S UMMARY O PTIMIZATION DESIGN SPACE El-Sayed Y.M. (2003)
  • 50. I NTRODUCTION T HERMODYNAMIC METHODS O PTIMIZATION METHODS C ARBON CONSTRAINED SCENARIO S UMMARY A PPROACHES TO OPTIMIZATION OF CHP SYSTEMS Two broad approaches to the use of optimization in the design of CHP or utility systems 1 Process Systems Engineering Superstrucrure based approach Evolution of structural changes 2 Thermodynamic/Thermoeconomic Parametric optimization Suitable for optimizing a base case rather than synthesizing a new design
  • 51. I NTRODUCTION T HERMODYNAMIC METHODS O PTIMIZATION METHODS C ARBON CONSTRAINED SCENARIO S UMMARY A PPROACHES TO OPTIMIZATION OF CHP SYSTEMS Two broad approaches to the use of optimization in the design of CHP or utility systems 1 Process Systems Engineering Superstrucrure based approach Evolution of structural changes 2 Thermodynamic/Thermoeconomic Parametric optimization Suitable for optimizing a base case rather than synthesizing a new design
  • 52. I NTRODUCTION T HERMODYNAMIC METHODS O PTIMIZATION METHODS C ARBON CONSTRAINED SCENARIO S UMMARY O PTIMIZATION FRAMEWORK G ENERIC SUPERSTRUCTURE
  • 53. I NTRODUCTION T HERMODYNAMIC METHODS O PTIMIZATION METHODS C ARBON CONSTRAINED SCENARIO S UMMARY O PTIMIZATION FRAMEWORK G ENERIC SUPERSTRUCTURE
  • 54. I NTRODUCTION T HERMODYNAMIC METHODS O PTIMIZATION METHODS C ARBON CONSTRAINED SCENARIO S UMMARY O PTIMIZATION FRAMEWORK G ENERIC SUPERSTRUCTURE
  • 55. I NTRODUCTION T HERMODYNAMIC METHODS O PTIMIZATION METHODS C ARBON CONSTRAINED SCENARIO S UMMARY O PTIMIZATION FRAMEWORK Given a set of steam and power demands: configure the CHP or utility plant; assign values of the operating pressures and temperatures of the steam; set the type and capacities of boilers, and all stream flowrates; and assign drivers to optimize the objective.
  • 56. I NTRODUCTION T HERMODYNAMIC METHODS O PTIMIZATION METHODS C ARBON CONSTRAINED SCENARIO S UMMARY O PTIMIZATION FRAMEWORK Given a set of steam and power demands: configure the CHP or utility plant; assign values of the operating pressures and temperatures of the steam; set the type and capacities of boilers, and all stream flowrates; and assign drivers to optimize the objective.
  • 57. I NTRODUCTION T HERMODYNAMIC METHODS O PTIMIZATION METHODS C ARBON CONSTRAINED SCENARIO S UMMARY O PTIMIZATION FRAMEWORK Given a set of steam and power demands: configure the CHP or utility plant; assign values of the operating pressures and temperatures of the steam; set the type and capacities of boilers, and all stream flowrates; and assign drivers to optimize the objective.
  • 58. I NTRODUCTION T HERMODYNAMIC METHODS O PTIMIZATION METHODS C ARBON CONSTRAINED SCENARIO S UMMARY O PTIMIZATION FRAMEWORK Given a set of steam and power demands: configure the CHP or utility plant; assign values of the operating pressures and temperatures of the steam; set the type and capacities of boilers, and all stream flowrates; and assign drivers to optimize the objective.
  • 59. I NTRODUCTION T HERMODYNAMIC METHODS O PTIMIZATION METHODS C ARBON CONSTRAINED SCENARIO S UMMARY O PTIMIZATION FRAMEWORK Given a set of steam and power demands: configure the CHP or utility plant; assign values of the operating pressures and temperatures of the steam; set the type and capacities of boilers, and all stream flowrates; and assign drivers to optimize the objective.
  • 60. I NTRODUCTION T HERMODYNAMIC METHODS O PTIMIZATION METHODS C ARBON CONSTRAINED SCENARIO S UMMARY O UTLINE 1 I NTRODUCTION The topic Boundary conditions and components Process Synthesis Methods 2 T HERMODYNAMIC METHODS Early work Targeting methodologies 3 O PTIMIZATION METHODS Background Early work Recent Trends in synthesis 4 C ARBON CONSTRAINED SCENARIO CCS Bio-energy 5 S UMMARY
  • 61. I NTRODUCTION T HERMODYNAMIC METHODS O PTIMIZATION METHODS C ARBON CONSTRAINED SCENARIO S UMMARY M ATH PROGRAMMING APPROACHES PAPOULIAS AND G ROSSMANN (1983) Incorporates an extensive superstructure and model includes driver allocation. Linearized the inherent MINLP problem. Linear equation derived for each unit when operating parameters have fixed values. Binary variables identify the existence of each operating condition for each unit. Non-linear cost linearized using a fixed charge approximation or piece-wise linear function. The optimization criterion used was minimization of annual cost. Proved the strength of mathematical programming methods to synthesize utility systems compared to heuristic methods.
  • 62. I NTRODUCTION T HERMODYNAMIC METHODS O PTIMIZATION METHODS C ARBON CONSTRAINED SCENARIO S UMMARY M ATH PROGRAMMING APPROACHES PAPOULIAS AND G ROSSMANN (1983)
  • 63. I NTRODUCTION T HERMODYNAMIC METHODS O PTIMIZATION METHODS C ARBON CONSTRAINED SCENARIO S UMMARY M ATH PROGRAMMING APPROACHES P ETROULAS AND R EKLAITIS (1983) Decomposed the problem into 1 Steam header selection and 2 Driver selection The overall objective was to minimize a linear combination of objective costs. No gas turbines and capital costs were considered.
  • 64. I NTRODUCTION T HERMODYNAMIC METHODS O PTIMIZATION METHODS C ARBON CONSTRAINED SCENARIO S UMMARY M ATH PROGRAMMING APPROACHES C OLMENARES AND S EIDER (1989) Developed an NLP model for synthesis of utility system Superstructure consists of cascade of Rankine cycles at different temperature levels. The overall objective was to minimize cost of the utility system. No gas turbines and electric motors were included in the superstructure.
  • 65. I NTRODUCTION T HERMODYNAMIC METHODS O PTIMIZATION METHODS C ARBON CONSTRAINED SCENARIO S UMMARY M ETAHEURISTIC APPROACHES M AIA ET AL . (1995) Simulated annealing approach for synthesis of utility system Superstructure is similar to Papoulias and Grossmann (1983). First attempt to include discrete equipement sizes in synthesis. Limitation of only one mechanical demand per drive. Costs and efficiency are obtained through continuous correlations.
  • 66. I NTRODUCTION T HERMODYNAMIC METHODS O PTIMIZATION METHODS C ARBON CONSTRAINED SCENARIO S UMMARY O UTLINE 1 I NTRODUCTION The topic Boundary conditions and components Process Synthesis Methods 2 T HERMODYNAMIC METHODS Early work Targeting methodologies 3 O PTIMIZATION METHODS Background Early work Recent Trends in synthesis 4 C ARBON CONSTRAINED SCENARIO CCS Bio-energy 5 S UMMARY
  • 67. I NTRODUCTION T HERMODYNAMIC METHODS O PTIMIZATION METHODS C ARBON CONSTRAINED SCENARIO S UMMARY R ECENT TRENDS IN OPTIMAL SYNTHESIS OF UTILITY SYSTEMS MINLP MODELS Bruno et al. (1998) extended the MILP model of Papoulias and Grossmann (1983) to develop an MINLP formulation. D ETAIL PROCESS UNIT MODELS Varbanov et al. (2004) developed detailed hardware models that were linearized and solved as a succession of MILPs.
  • 68. I NTRODUCTION T HERMODYNAMIC METHODS O PTIMIZATION METHODS C ARBON CONSTRAINED SCENARIO S UMMARY R ECENT TRENDS IN OPTIMAL SYNTHESIS OF UTILITY SYSTEMS MINLP MODELS Bruno et al. (1998) extended the MILP model of Papoulias and Grossmann (1983) to develop an MINLP formulation. D ETAIL PROCESS UNIT MODELS Varbanov et al. (2004) developed detailed hardware models that were linearized and solved as a succession of MILPs.
  • 69. I NTRODUCTION T HERMODYNAMIC METHODS O PTIMIZATION METHODS C ARBON CONSTRAINED SCENARIO S UMMARY R ECENT TRENDS M ULTIPERIOD MODELS Iyer and Grossmann (1998) extended the Papoulias and Grossmann (1983) model to include mutiperiod operation. Maia and Qassim (1997) extended the work by Maia et al.(1995) to include multiperiod operation. Oliviera and Matos (2003) included environmental aspects when extending the work by Iyer and Grossmann (1998) and Maia and Qassim (1997). Frangopoulos and Dimopoulos (2004) used thermoeconomic optimization of multiperiod co-generation systems with a limited superstructure. Aguilar et al. (2005) proposed a MILP formulation of multi-period utility systems. Chen and Lin (2011) develop a steam distribution network for integration with chemical processes by adapting the transhipment model for flexible operation.
  • 70. I NTRODUCTION T HERMODYNAMIC METHODS O PTIMIZATION METHODS C ARBON CONSTRAINED SCENARIO S UMMARY R ECENT TRENDS I NCORPORATING OTHER CONSIDERATIONS SUCH AS AVAILABILITY ETC . Frangopoulos and Dimopoulos (2004) used thermoeconomic optimization of multiperiod co-generation systems and include availability costs in calculating the NPV. Aguilar et al. (2005) do not explicity include availability but including the degree of equipment redundancy during optimization phase. Del Nogal et al. (2010) present an rich superstructure and MILP formulation to synthesize utility systems including availability considerations.
  • 71. I NTRODUCTION T HERMODYNAMIC METHODS O PTIMIZATION METHODS C ARBON CONSTRAINED SCENARIO S UMMARY O UTLINE 1 I NTRODUCTION The topic Boundary conditions and components Process Synthesis Methods 2 T HERMODYNAMIC METHODS Early work Targeting methodologies 3 O PTIMIZATION METHODS Background Early work Recent Trends in synthesis 4 C ARBON CONSTRAINED SCENARIO CCS Bio-energy 5 S UMMARY
  • 72. I NTRODUCTION T HERMODYNAMIC METHODS O PTIMIZATION METHODS C ARBON CONSTRAINED SCENARIO S UMMARY P OWER AND STEAM PLANTS IN A CARBON CONSTRAINED SCENARIO C ARBON C APTURE AND S TORAGE Fossil fuel based utility plants would require CCS. Inclusion of CCS would mean addition of a chemical process facility in the utility system. Tight integration required between the different components to reduce efficiency penalty.
  • 73. I NTRODUCTION T HERMODYNAMIC METHODS O PTIMIZATION METHODS C ARBON CONSTRAINED SCENARIO S UMMARY C ARBON CONSTRAINED SCENARIO C ARBON C APTURE AND S TORAGE M ARTELLI ET AL . (2011) AND M ARTELLI ET AL . (2012) Two step optimization procedure for optimal design of heat recovery steam generator including external heat addition and extraction.
  • 74. I NTRODUCTION T HERMODYNAMIC METHODS O PTIMIZATION METHODS C ARBON CONSTRAINED SCENARIO S UMMARY C ARBON CONSTRAINED SCENARIO C ARBON C APTURE AND S TORAGE L IU ET AL . (2009, 2010) A MINLP framework for the synthesis of optimum poly-generation plants using coal as fuel.
  • 75. I NTRODUCTION T HERMODYNAMIC METHODS O PTIMIZATION METHODS C ARBON CONSTRAINED SCENARIO S UMMARY C ARBON CONSTRAINED SCENARIO C ARBON C APTURE AND S TORAGE A NANTHARAMAN AND B ERSTAD (2011) A MILP framework for generation of optimal integration schemes for post-combustion CO2 capture unit with NGCC power plant.
  • 76. I NTRODUCTION T HERMODYNAMIC METHODS O PTIMIZATION METHODS C ARBON CONSTRAINED SCENARIO S UMMARY C ARBON CONSTRAINED SCENARIO C ARBON C APTURE AND S TORAGE A NANTHARAMAN AND B ERSTAD (2011) A MILP framework for generation of optimal integration schemes for post-combustion CO2 capture unit with NGCC power plant.
  • 77. I NTRODUCTION T HERMODYNAMIC METHODS O PTIMIZATION METHODS C ARBON CONSTRAINED SCENARIO S UMMARY C ARBON CONSTRAINED SCENARIO C ARBON C APTURE AND S TORAGE J OHNSEN , E. (2011) A MINLP framework for generation of optimal synthesis of an air-blown Integrated Reforming Combined Cycle power plant using meta-models.
  • 78. I NTRODUCTION T HERMODYNAMIC METHODS O PTIMIZATION METHODS C ARBON CONSTRAINED SCENARIO S UMMARY C ARBON CONSTRAINED SCENARIO C ARBON C APTURE AND S TORAGE J OHNSEN , E. (2011) A MINLP framework for generation of optimal synthesis of an air-blown Integrated Reforming Combined Cycle power plant using meta-models.
  • 79. I NTRODUCTION T HERMODYNAMIC METHODS O PTIMIZATION METHODS C ARBON CONSTRAINED SCENARIO S UMMARY O UTLINE 1 I NTRODUCTION The topic Boundary conditions and components Process Synthesis Methods 2 T HERMODYNAMIC METHODS Early work Targeting methodologies 3 O PTIMIZATION METHODS Background Early work Recent Trends in synthesis 4 C ARBON CONSTRAINED SCENARIO CCS Bio-energy 5 S UMMARY
  • 80. I NTRODUCTION T HERMODYNAMIC METHODS O PTIMIZATION METHODS C ARBON CONSTRAINED SCENARIO S UMMARY P OWER AND STEAM PLANTS IN A CARBON CONSTRAINED SCENARIO B IO - ENERGY CHP plants fired with biomass, MSW etc. The superstructure involved for biomass based CHP will be extensive: Selection of biomass Preparation of fuel Fuel/energy conversion system Integration with gas turbine systems No significant development in the systematic approach to the design of biomass based CHP systems.
  • 81. I NTRODUCTION T HERMODYNAMIC METHODS O PTIMIZATION METHODS C ARBON CONSTRAINED SCENARIO S UMMARY S UMMARY Synthesis of combined heat and power plants or utility plants is a mature area of research. Thermodynamic based targeting methods for co-generation have been developed. No thermodynamic based systematic synthesis methodology in the literature. Mathematical programming methods where an exhaustive superstructure is used to synthesize utility networks dominate literature. Most of these models are formulated as MILPs. Recent developments include multiperiod optimization models and incorporating availability consideration in the design phase. In a carbon constrained scenario, novel methods to synthsize power and steam systems with CCS need to be developed further. Systematic methods for the optimal synthesis of biomass based CHP needs development.
  • 82. I NTRODUCTION T HERMODYNAMIC METHODS O PTIMIZATION METHODS C ARBON CONSTRAINED SCENARIO S UMMARY S UMMARY Synthesis of combined heat and power plants or utility plants is a mature area of research. Thermodynamic based targeting methods for co-generation have been developed. No thermodynamic based systematic synthesis methodology in the literature. Mathematical programming methods where an exhaustive superstructure is used to synthesize utility networks dominate literature. Most of these models are formulated as MILPs. Recent developments include multiperiod optimization models and incorporating availability consideration in the design phase. In a carbon constrained scenario, novel methods to synthsize power and steam systems with CCS need to be developed further. Systematic methods for the optimal synthesis of biomass based CHP needs development.
  • 83. I NTRODUCTION T HERMODYNAMIC METHODS O PTIMIZATION METHODS C ARBON CONSTRAINED SCENARIO S UMMARY S UMMARY Synthesis of combined heat and power plants or utility plants is a mature area of research. Thermodynamic based targeting methods for co-generation have been developed. No thermodynamic based systematic synthesis methodology in the literature. Mathematical programming methods where an exhaustive superstructure is used to synthesize utility networks dominate literature. Most of these models are formulated as MILPs. Recent developments include multiperiod optimization models and incorporating availability consideration in the design phase. In a carbon constrained scenario, novel methods to synthsize power and steam systems with CCS need to be developed further. Systematic methods for the optimal synthesis of biomass based CHP needs development.
  • 84. I NTRODUCTION T HERMODYNAMIC METHODS O PTIMIZATION METHODS C ARBON CONSTRAINED SCENARIO S UMMARY S UMMARY Synthesis of combined heat and power plants or utility plants is a mature area of research. Thermodynamic based targeting methods for co-generation have been developed. No thermodynamic based systematic synthesis methodology in the literature. Mathematical programming methods where an exhaustive superstructure is used to synthesize utility networks dominate literature. Most of these models are formulated as MILPs. Recent developments include multiperiod optimization models and incorporating availability consideration in the design phase. In a carbon constrained scenario, novel methods to synthsize power and steam systems with CCS need to be developed further. Systematic methods for the optimal synthesis of biomass based CHP needs development.
  • 85. I NTRODUCTION T HERMODYNAMIC METHODS O PTIMIZATION METHODS C ARBON CONSTRAINED SCENARIO S UMMARY S UMMARY Synthesis of combined heat and power plants or utility plants is a mature area of research. Thermodynamic based targeting methods for co-generation have been developed. No thermodynamic based systematic synthesis methodology in the literature. Mathematical programming methods where an exhaustive superstructure is used to synthesize utility networks dominate literature. Most of these models are formulated as MILPs. Recent developments include multiperiod optimization models and incorporating availability consideration in the design phase. In a carbon constrained scenario, novel methods to synthsize power and steam systems with CCS need to be developed further. Systematic methods for the optimal synthesis of biomass based CHP needs development.
  • 86. I NTRODUCTION T HERMODYNAMIC METHODS O PTIMIZATION METHODS C ARBON CONSTRAINED SCENARIO S UMMARY S UMMARY Synthesis of combined heat and power plants or utility plants is a mature area of research. Thermodynamic based targeting methods for co-generation have been developed. No thermodynamic based systematic synthesis methodology in the literature. Mathematical programming methods where an exhaustive superstructure is used to synthesize utility networks dominate literature. Most of these models are formulated as MILPs. Recent developments include multiperiod optimization models and incorporating availability consideration in the design phase. In a carbon constrained scenario, novel methods to synthsize power and steam systems with CCS need to be developed further. Systematic methods for the optimal synthesis of biomass based CHP needs development.
  • 87. I NTRODUCTION T HERMODYNAMIC METHODS O PTIMIZATION METHODS C ARBON CONSTRAINED SCENARIO S UMMARY S UMMARY Synthesis of combined heat and power plants or utility plants is a mature area of research. Thermodynamic based targeting methods for co-generation have been developed. No thermodynamic based systematic synthesis methodology in the literature. Mathematical programming methods where an exhaustive superstructure is used to synthesize utility networks dominate literature. Most of these models are formulated as MILPs. Recent developments include multiperiod optimization models and incorporating availability consideration in the design phase. In a carbon constrained scenario, novel methods to synthsize power and steam systems with CCS need to be developed further. Systematic methods for the optimal synthesis of biomass based CHP needs development.
  • 88. I NTRODUCTION T HERMODYNAMIC METHODS O PTIMIZATION METHODS C ARBON CONSTRAINED SCENARIO S UMMARY S UMMARY Synthesis of combined heat and power plants or utility plants is a mature area of research. Thermodynamic based targeting methods for co-generation have been developed. No thermodynamic based systematic synthesis methodology in the literature. Mathematical programming methods where an exhaustive superstructure is used to synthesize utility networks dominate literature. Most of these models are formulated as MILPs. Recent developments include multiperiod optimization models and incorporating availability consideration in the design phase. In a carbon constrained scenario, novel methods to synthsize power and steam systems with CCS need to be developed further. Systematic methods for the optimal synthesis of biomass based CHP needs development.
  • 89. I NTRODUCTION T HERMODYNAMIC METHODS O PTIMIZATION METHODS C ARBON CONSTRAINED SCENARIO S UMMARY R EFERENCES I O Aguilar, S Perry, J Kim, and R Smith. Design and Optimization of Flexible Utility Systems Subject to Variable ConditionsPart 1: Modelling Framework. Chemical Engineering Research and Design, 85(8):1136–1148, 2007. J Bruno, F Fernandez, F Castells, and I.E. Grossmann. A Rigorous MINLP Model for the Optimal Synthesis and Operation of Utility Plants. Chemical Engineering Research and Design, 76(3):246–258, March 1998. C.T. Chang and J.R. Hwang. A multiobjective programming approach to waste minimization in the utility systems of chemical processes. Chemical Engineering Science, 51(16):3951–3965, August 1996. C.L. Chen and C.Y. Lin. A flexible structural and operational design of steam systems. Applied Thermal Engineering, 31(13):2084–2093, September 2011. C.C. Chou and Y.S. Shih. A thermodynamic approach to the design and synthesis of plant utility systems. Industrial & Engineering Chemistry Research, 26(6):1100–1108, June 1987. T.R. Colmenares and W.D. Seider. Synthesis of utility systems integrated with chemical processes. Industrial & Engineering Chemistry Research, 28(1):84–93, January 1989. F.L. Del Nogal, J.K. Kim, S. Perry, and R. Smith. Synthesis of mechanical driver and power generation configurations, Part 1: Optimization framework. AIChE Journal, pages NA–NA, 2010.
  • 90. I NTRODUCTION T HERMODYNAMIC METHODS O PTIMIZATION METHODS C ARBON CONSTRAINED SCENARIO S UMMARY R EFERENCES II V.R. Dhole and B. Linnhoff. Total site targets for fuel, co-generation, emissions, and cooling. Computers & Chemical Engineering, 17:S101–S109, 1993. M. El-Halwagi, D. Harell, and H. Dennis Spriggs. Targeting cogeneration and waste utilization through process integration. Applied Energy, 86(6):880–887, June 2009. C.A. Frangopoulos and G.G. Dimopoulos. Effect of reliability considerations on the optimal synthesis, design and operation of a cogeneration system. Energy, 29(3):309–329, March 2004. R.R. Iyer and I.E. Grossmann. Optimal multiperiod operational planning for utility systems. Computers & Chemical Engineering, 21(8):787–800, 1997. J. Klemeš, V.R. Dhole, K. Raissi, S.J. Perry, and L. Puigjaner. Targeting and design methodology for reduction of fuel, power and CO2 on total sites. Applied Thermal Engineering, 17(8-10):993–1003, August 1997. B. Linnhoff and V.R. Dhole. Targeting for CO2 emissions for Total Sites. Chemical Engineering & Technology, 16(4):252–259, August 1993. P. Liu, M.C. Georgiadis, and E.N. Pistikopoulos. Advances in Energy Systems Engineering. Industrial & Engineering Chemistry Research, page 100917092426020, September 2010.
  • 91. I NTRODUCTION T HERMODYNAMIC METHODS O PTIMIZATION METHODS C ARBON CONSTRAINED SCENARIO S UMMARY R EFERENCES III P. Liu, E. Pistikopoulos, and Z. Li. A mixed-integer optimization approach for polygeneration energy systems design. Computers & Chemical Engineering, 33(3):759–768, March 2009. F. Marechal and B. Kalitventzeff. Process integration : Selection optimal utility system . Computers & Chemical Engineering, 22(Suppl):S149–156, 1998. S.P Mavromatis and A.C Kokossis. Hardware composites: A new conceptual tool for the analysis and optimisation of steam turbine networks in chemical process industries. Chemical Engineering Science, 53(7):1405–1434, March 1998. L.O. Maia, L. Vidal de Carvalho, and R.Y. Qassim. Synthesis of utility systems by simulated annealing. Computers & Chemical Engineering, 19(4):481–488, April 1995. M. Nishio, J. Itoh, K. Shiroko, and T. Umeda. A Thermodynamic Approach to Steam-Power System Design. Industrial & Engineering Chemistry Process Design and Development, 19(2):306–312, April 1980. M. Nishio and A.I. Johnson. Stratergy for energy system expansion. Chemical Engineering Progress, 73:75, 1979. S. Papoulias and I.E. Grossmann. A structural optimization approach in process synthesisâI Utility systems. Computers & Chemical Engineering, 7(6):695–706, 1983.
  • 92. I NTRODUCTION T HERMODYNAMIC METHODS O PTIMIZATION METHODS C ARBON CONSTRAINED SCENARIO S UMMARY R EFERENCES IV T. Petroulas and G. V. Reklaitis. Computer-aided synthesis and design of plant utility systems. AIChE Journal, 30(1):69–78, January 1984. V Papandreou and Z Shang. A multi-criteria optimisation approach for the design of sustainable utility systems. Computers & Chemical Engineering, 32(7):1589–1602, July 2008. Z. Shang and A. Kokossis. A systematic approach to the synthesis and design of flexible site utility systems. Chemical Engineering Science, 60(16):4431–4451, August 2005. P. Varbanov, S. Doyle, and R. Smith. Modelling and Optimization of Utility Systems. Chemical Engineering Research and Design, 82(5):561–578, May 2004. P. Varbanov, S. Perry, J. Klemeš, and R. Smith. Synthesis of industrial utility systems: cost-effective de-carbonisation. Applied Thermal Engineering, 25(7):985–1001, May 2005.