boiler steam cycle aspenplusv8

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    SteamCycleSimulationAspenPlusv8.6

    Create

    new

    simulation

    file

    StartAllProgramsAspenTech ProcessModelingV8.6AspenPlusAspen

    PlusV8.6 New GasProcessing Gas

    ProcessingwithMetricUnits Create

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    DefinetheComponents&thePropertyModels

    Specifycomponents,fluidpropertypackages,&crudeoilassays

    ComponentLists

    Add ComponentList2

    Find

    Add

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    ComponentID

    Alias

    Enter

    Rename

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    Close

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    File

    SaveAs AspenPlusBackup

    Setup&SolvetheFlowsheet

    WorkingUnits

    Simulation

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    Home

    UnitSets

    SICBAR

    Edit

    Mass

    Flow

    Flow

    related

    Heat

    Heatrelated

    SteamCycle

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    ModelPalette Heater

    PressureChangers Compr ICON3 Pump

    ModelPalette Material

    o

    o

    o

    o

    o

    ModelPalette Heat

    o

    o

    ModelPalette Work

    o

    o

    ModelPalette View ModelPalette

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    CONDNSAT

    Temperature Vapor

    Fraction FlashType

    Temperature

    Vapor

    Fraction

    Composition

    H2O

    MoleFrac

    Pump

    Model

    DischargePressure

    Pump DriverEfficiencies

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    Turbine

    Model

    Isentropic MechanicalEfficiencies

    DischargePressure

    Convergence

    Valid

    phases VaporLiquid

    FreeWater

    FlashType

    Vaporfraction

    FlashType Pressure

    Home Run

    StreamResults

    MainFlowsheet Modify Temperature Pressure VaporFraction

    StreamResults

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    Heat/Work Pressure

    Vaporfraction OK

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    ModelPalette Manipulators Calculator ICON1

    Import

    variable

    Export

    variable

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    Calculate

    Fortran

    CALCULATOR

    PENGROB

    STEAMTA

    FreeWater STEAMTA

    STEAMTA

    BlockOptions Simulation Block

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    Options Propertymethod STEAMTA STMTRBN

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    Fuel&CombustionSystem

    ModelPalette Valve Compressor2 RGibbs

    Heater3

    ModelPalette Material

    o

    o

    o

    o

    o

    o

    ModelPalette Heat

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    o

    ModelPalette Work

    o

    Temperature Pressure

    FlashType

    Temperature

    Pressure.

    Mole

    Frac

    Temperature Pressure

    FlashType

    Temperature Pressure.

    MoleFrac

    Outletpressure

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    Compressor Model

    Type Isentropic

    Isentropic

    MechanicalEfficiencies

    RGibbs

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    AIR2

    CALCULATOR

    ModelPalette Manipulators Calculator ICON1

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    Importvariable

    Export

    variable

    Calculate

    Fortran

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    excessstoich

    n fn

    y

    ModelPalette Manipulators Calculator ICON1

    Exportvariable

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    Import

    variables

    Import

    variable

    Importvariables

    Importvariables

    Calculate

    Fortran

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    Setup

    Simulation

    ReportOptions

    MoleFlowbasis

    Fractionbasis

    Mole

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    TyingtheTwoSystemsTogether

    Reconnect ReconnectDestination inlet

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    Spec

    Spec

    Target

    Tolerance

    Vary

    StreamVar Type

    Upper

    Lower

    Stepsize Maximum

    stepsize

    not MassFlow Type

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    AdditionalStream&UnitAnalyses

    Setup

    Report

    Options

    Stream

    PropertySets

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    Availablepropertysets

    > Selected

    propertysets Close

    Results

    Boilerefficiency.

    Q

    m

    Steamcyclethermalefficiency.

    W WQ

    Overallefficiency.

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    blowerW W W

    m

    MaterialTable HeatTable Work

    Table

    Streams ResultsSummary

    Material CopyAll

    MaterialTable Paste

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    Heat

    Copy HeatTable

    Paste

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    Work

    Copy HeatTable

    Paste

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    Models ResultsSummary

    Heater

    SendtoExcel OnetableperExcelworksheet

    Addtablestoexistingworkbook Browse

    ExporttablestoExcel OK Open

    ExcelFile

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    Summary

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