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    Heat and Power Technology, Stockholm, Sweden

    ASPEN ENGINEERING SUITEOVERVIEW

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    Heat and Power Technology, Stockholm, Sweden

    Software for integrated process engineering, including steady-stateand dynamic process simulation, equipment design, and costevaluation.

    General Overview

    Source: Aspen Technology, 2012

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    Heat and Power Technology, Stockholm, Sweden

    Aspen Plus Aspen Plus is a process modeling tool for conceptual design,

    optimization, and performance monitoring for diverse industries.Aspen Plus is a core element of AspenTechs Process Engineeringapplications.

    Given thermodynamic data, realistic operating conditions, andrigorous equipment models Its possible to simulate actual plantbehaviors, by using basic engineering relations such as mass

    and energy balances, and phase and chemical equilibrium Features Best-in-class physical properties methods and dataDiverse Model library : Simulation of a wide range of processesScalability for large and complex processesOnline deployment of models: real-time optimization/advancedprocess control applicationsWorkflow automation: Aspen Plus models can be linked to MicrosoftExcel using Aspen Simulation Workbook or Visual Basic

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    Heat and Power Technology, Stockholm, Sweden

    Aspen Plus

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    Heat and Power Technology, Stockholm, Sweden

    Example

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    Heat and Power Technology, Stockholm, Sweden

    Define Process Flow SheetCoal Drying Flowsheet

    WET-COAL

    NITROGEN

    DRY-REAC

    IN-DRIER

    DRY-FLSH

    EXHAUST

    DRY-COAL

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    Heat and Power Technology, Stockholm, Sweden

    Specify Chemical Components

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    Heat and Power Technology, Stockholm, Sweden

    Specify Thermodynamic Model

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    Heat and Power Technology, Stockholm, Sweden

    Specify Flow Rates conditions

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    Heat and Power Technology, Stockholm, Sweden

    Simulation Results

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    Heat and Power Technology, Stockholm, Sweden

    ASPEN CUSTOM MODELER

    OVERVIEW

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    Heat and Power Technology, Stockholm, Sweden

    FeaturesDesigned for process engineers : ACM uses a flow

    sheeting environment based on streams and equipment

    and includes built-in understanding of components andprocess thermodynamics.

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    Heat and Power Technology, Stockholm, Sweden

    FeaturesEquation oriented architecture : ACM language isdeclarative , you say what you want and leave it to ACM

    to find out how .- Solver for system of Algebraic Equations , based on Newton

    iterative procedure

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    Heat and Power Technology, Stockholm, Sweden

    Features- System of differential and algebraic equations

    Integration Algorithms- Implicit: Implicit Euler (fixed or variable step), gear- Explicit: Explicit Euler, Runge Kutta

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    Heat and Power Technology, Stockholm, Sweden

    Features Optimization and estimation tools enabling

    parameter fitting, data reconciliation, and steady-state

    and dynamic process optimization.

    Estimation example

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    Heat and Power Technology, Stockholm, Sweden

    FeaturesOptimization example

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    Heat and Power Technology, Stockholm, Sweden

    Features

    Flexible Task Language to define batch recipes,

    transition schemes, or to simulate process equipmentfailures or other disturbances

    Heating System example:

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    Heat and Power Technology, Stockholm, Sweden

    Features Export Equipments or process models

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    Heat and Power Technology, Stockholm, Sweden

    Model Example

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    Heat and Power Technology, Stockholm, Sweden

    Department of Energy Technology

    Stirling Engine Adiabatic Model + Losses

    Assumptions

    -Adiabatic expansion and compressionspaces

    - Sinusoidal volume variations

    -Ideal gas inside the engine

    - Heat Losses

    -Friction and Pressure drop losses

    - Non ideal Regenerator

    - Heat transfer model from the externalsource to the engine included.

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    Heat and Power Technology, Stockholm, Sweden

    Heater

    Regenerator

    Cooler

    StirlingS7

    S8

    S9

    Ideal Adiabatic LossesSolution Aspen- C++

    Pressure Losses

    Internal Conducction HeatExchangers

    Regenerator Losses

    Shuttle Effect Losses

    )(1 dQridQ

    JLd TcTd kpDd z

    dQ )(4.0 2

    2

    .

    2

    Ad V m fr

    P

    PmdQ

    T LkA

    dQ

    +

    Ths(source)Tks(source)

    Tho(heater)Tko(cooler)

    Teo=ThoTco= Tko

    Solve DifferentialEquations

    Calculate Tc, Te

    After 360(cycle)

    If TcTcoTeTeo

    Tco=TcTeo=Te

    Qheater Q cooler

    Qloss

    Th=Ths-Qhs/UATk=Tks-Qks/UA

    If ThThoTkTko

    Tho=ThTko=Tk

    Qheater Q cooler

    Qloss

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    Heat and Power Technology, Stockholm, Sweden

    THANKS