Chemical Process CHEMCAD Simulation For Windows

1 V&M SYSTEMSCONSULTANCY : 886-2-88098037 Fax: 886-2-88098036 Chemical Process SimulationFinish your jobs in the shortest timeProcess designProcess improvingProcess integrationProcess debottleneckTrouble shootingThe Best Choice toImprove YourCompetitivenessRun Process simulationwithout Learning CurveFor WindowsCHEMCADV&M SYSTEMSCONSULTANCY : 886-2-88098037 Fax: 886-2-88098036 Batch distillation(1), Dynamic distillation(2), Batch Reactor(3), Dynamic Vessel(4), PID Controller(4), Surge tank(4), Flow control valve(4), valve, Recorder(4), Ramp controller(4), Time Delay(4), Time Switch(1)..Distillation, Absorption, Azeotropic distillation, Three Phase distillation, Electrolyte distillation, Reactive distillation,Flash, VLL Tower, Reactor,Heat Exchanger, Compressor, Pump Fire Heater, Controller, , Centrifugal filter, Cyclone, Hydrocyclone, Baghouse filter, Vacuum filter, Crusher, Grinder, Electrostatic Precipitator, Dryer, Washer, Sedimentation separator, Venturi WindowsThe most powerful and user friendly Chemical Process Simulation softwareFor WindowsCHEMCADUnit Operations andProcess SimulationUnit Operations andProcess Simulation (1) Require a CC-BATCH license (option)(2) Require a CC-DCOLUMN license (option)(3) Require a CC-ReACS license (option)(4) Require a CC-DCOLUMN or CC-ReACS license (option)V&M SYSTEMSCONSULTANCY : 886-2-88098037 Fax.

2 886-2-88098036 Physical Properties and ThermodynamicsPhysical Properties and ThermodynamicsPhysical properties databank for pure componentsElectrolytes databankVaper phase association, heat of solution databankDifferent K-values and/or enthalpiesfor different unit or BIPs for different unit provides the BIPs for activity coefficient model and electrolyte models. CHEMCAD has a complete library of thermodynamics options covering applications from refining to chemicals, to electrolytes. There are 38 K- models and 14 H-models, including: equation of state models (SRK, PR, APISRK, Grayson ), activity coefficient models(NRTL, UNIQUAC, Wilson, ), recently developed models(SAFT, ESD, MSRK, ), electrolyte models (NRTL and Pitzer), and lots of special WindowsCHEMCADCHEMCAD SUITE - PROGRAM FEATURESGENERAL FEATURES Graphical user interfaceCustomized reports and PFD sInteractive operationInterfaces to spreadsheets (Microsoft Excel) and AutoCAD (.)

3 DXF) User added unit operations, thermodynamics, components, and/or graphics symbolsIn-line C language interpreterUsers may add their own .DLLsExtensive online helpExtensive data checkingFlexible engineering unitsOLE, COM, and Visual Basic integrationENGINEERING DATA Physical properties databank for pure components (DIPPR)BIP database for activity coeffi cient equationsElectrolytes databaseVapor phase association databaseInterface to corporate and/or third party databasesTHERMODYNAMICS Vapor phase associationDifferent K-Value models and/or enthalpy models for different units or traysDifferent BIPs for different units or traysVapor-Liquid and Vapor-Liquid-Liquid equilibriumPhysical properties estimation of undefi ned components: group contribution methods available for pure and mixture properties estimationComposite heat curve pinch analysisDistillation curve assay analysisK-VALUE METHODS Equations of StateSoave-Redlich-KwongGrayson-Streed/C hao-SeaderPeng-RobinsonBenedict-Webb-Rub in-StarlingAPI Soave-Redlich-KwongModifi ed Soave-Redlich-Kwong (MSRK)Extended Soave-Redlich-Kwong (TSRK)Predictive Soave-Redlich-Kwong (PSRK)Elliott Suresh Donohoe (ESD)Statistical Associating Fluid Theory (SAFT)Peng-Robinson-Stryjek-Vara (PRSV) Empirical ESSO (Maxwell-Bonnell)Vapor Pressure (Ideal Solution)Henry s Gas Law Activity Coeffi cient MethodsUNIQUAC (UNIQUAC with the new group and surface parameters)UNIFAC/UNIQUAC (UNIQUAC with the old group and surface parameters)

4 UNIFAC VLEUNIFAC LLEUPLM (UNIFAC for Polymers)WilsonT. K. WilsonHRNM Modifi ed WilsonVan LaarNon-Random Two Liquid (NRTL)MargulesGMAC (Chien-Null)Scatchard-Hildebrand (Regular Solution)Wilson Salt Special SystemsHydrocarbon-Water SolubilityAmines (VLE and LLE)Sour WaterTri-Ethylene-Glycol/Water DehydrationFlory-Huggins Method for Polymers User Supplied K-Values Polynomial K-valuesTabular K-valuesPartial Pressures of Aqueous MixturesUser SubroutineUser Specifi ed Activity Coeffi cients ENTHALPY METHODS Equations of StateRedlich-KwongSoave-Redlich-KwongPen g-RobinsonAPI Soave-Redlich-KwongLee-KeslerBenedict-We bb-Rubin-StarlingPeng-Robinson-Stryjek-V ara (PRSV) Chemical SystemsLatent HeatElectrolyteHeat of Mixing by Gamma Special SystemsSteam TableMixed ModelNo Enthalpy (Mass balance only)

5 User Added DataPolynomial Enthalpy ModelTabular H sHeat of Solution DataUser SubroutineELECTROLYTES Pitzer and mNRTL methods for strong and weak electrolytes including temperature dependent interaction parametersBinary and ternary interaction parameter databaseReaction equilibrium database including many common industrial systems; calculated from Gibbs free energy when data is absentExpert system assistance for setting up electrolyte chemistryREGRESSION Pure component physical property regressionMulticomponent VLE/LLE regression from user data, UNIFAC, or infi nite dilution dataRegression of electrolyte dataUTILITIES EPA WAR Algorithm for environmental and health impact studiesHydrate/Solid CO2 predictionTotal Organic Content/ Chemical Oxygen Demand calculationPlots TPXY, Binodal, Residue Curve MapSymbol Builder for custom graphic representationsCalculation of Relief Devices (DIERS)

6 Design and rating of relief valves and/or rupture disksBubbly, churn-turbulent, and homogeneous vessel modelsHEM, ERM, Henry-Fauske HNE, non-fl ashing liquid and single-phase vapor vent fl ow modelsAPI-520/52, API-2000, OSHA , and NFPA-30 fi re models, or specifi ed heat and outlet piping pressure drop calculationsComprehensive vessel and relief vent specifi cation capabilitiesAtmospheric and pressure vesselsCOMMON FEATURES V&M SYSTEMS CONSULTANCY LTD TEL: 886-2-8809-8037 FAX: 886-2-8809-8036 V&M SYSTEMS CONSULTANCY LTD TEL: 886-2-8809-8037 FAX: 886-2-8809-8036 CHEMCAD SUITE - PROGRAM FEATURESUNIT OPERATIONS CalculatorComponent separatorCompressorControllerDistillatio n Column (see detailed DISTILLATION section)DividerExcel UnitExpander/TurbineFired heaterFlashHeat exchangerLiquid-liquid extractorLNG Heat exchangerLoopMixerNodePhase GeneratorPipe simulatorPumpReactor (see detailed REACTORS section)RecorderStream referenceUser Added ModuleValveVesselSolids handling.

7 Baghouse fi lterCentrifugal fi lterCrusher/GrinderCrystallizerCycloneDr yerElectrostatic precipitatorHydrocycloneScreenSedimentat orVacuum fi lterVenturi scrubberWasherDISTILLATION Shortcut and rigorousMultiple column arrangementsFlexible specifi cationsSimultaneous Correction and Rigorous Inside Out algorithmsUp to 500 theoretical stagesThree phase distillationScrubbing and strippingMass transfer based distillation for packed and tray-ed columnsAutomatically calculates the component diffusivitiesRigorous calculation of the mass transfer coeffi cientUser editable database of packing data from packing manufacturersCalculation of ambient heat lossTray by tray tabular and plotted outputREACTIVE DISTILLATION Reactions may be equilibrium or kinetic equation basedReactions solved simultaneously with VLEF lexible rate form, including user addedPurity and temperature specifi cationsUp to 300 reactionsVapor and/or liquid reactions are permittedREACTORS StoichiometricEquilibrium Up to 300 simultaneous reactionsWater-gas shift dataMethanation dataGibbs free energy minimizationKinetic (PFR or CSTR)Unlimited simultaneous reactionsFlexible rate form, including user addedFLOWSHEET CONVERGENCE Sequential Modular convergence Speed up methods (Wegstein, Dominant Eigenvalue)Simultaneous Modular convergence for piping networks (when the Node unit operation is used)Optimization algorithm allows you to maximize or minimize a stream or unit operation variable (Objective Function)

8 Given certain independent variables and and Parametric analysis with reportingUnlimited size of fl owsheet (unlimited number of streams and unit operations)EQUIPMENT SIZING Rigorous equipment sizing routines for:Trays (Sieve, Bubble cap, Valve)Packing (Random & Structured)PipesPressure VesselsOrifi cesControl ValvesThree Phase VesselsRelief Devices (DIERS)Spec (specifi cation) sheets in Microsoft Excel with pre-built templates for:Baghouse fi lterCompressorFired HeaterHeat Exchanger (including TEMA sheet)PumpDistillation columnTankValveEQUIPMENT COST ESTIMATION Calculates purchase and installed cost of major pieces of plant equipmentCC-STEADY STATE V&M SYSTEMS CONSULTANCY LTD TEL: 886-2-8809-8037 FAX: 886-2-8809-8036 V&M SYSTEMS CONSULTANCY LTD TEL: 886-2-8809-8037 FAX.

9 886-2-8809-8036 CHEMCAD SUITE - PROGRAM FEATURESGENERAL FEATURES Full dynamic fl owsheeting for operability, training, startup/shutdownGraphical plotting of time dependent resultsOnline, real-time display of results during calculationCalculation interruptFull integration into the CHEMCAD Suite and fl owsheetsINTERACTIVE DYNAMIC Simulation Additional mode of operation allowing user interactivity while the Simulation is runningOpen/close valvesChange setpointsIntroduce upsetsMode for connectivity to operator training systemsCONTROL VALVES Equal percentage or linear valuesValve coeffi cient (Cv)RangeabilityCritical fl ow factorValve position functionCONTROLLER PID (proportional integral derivative) action can be specifi edController set points can be purity, temperature, pressure, level, fl ow, or any other fl owsheet variableController limits may be set:With or without upper or lower limitsRelative to the set pointAt a specifi ed valueCascade and split range controllers can be usedSensor functions can be specifi edRAMP Control Time/Value table Random Disturbance Sine WaveDIERS ANALYSIS FACILITY Practical, comprehensive, fi eld tested DIERS (Design Institute for Emergency Relief Systems) analysisThis can be used to simulate emergency relief situations on a dynamic basisThe DIERS results are included in the heat and material balance of the dynamic vesselOUTPUTTime history reports and plots for.

10 All unit operation parameters including control valve position and controller outputAll stream parametersBATCH REACTOR (CC-REACS) FEATURES Chemical DESIGNU nlimited number of speciesUnlimited number of simultaneous reactionsChoice of Arrhenius, Langmuir-Hinshelwood, or user added rate equation formsRegression of kinetic Process dataREACTOR DESIGNM ultiple Coils and jacketsService or Process side heat exchangers and electric heatersHeat transfer rate calculation; includes calculation of Process and service side fi lm coeffi cientsVapor and liquid draws permittedBatch, semi-batch or continuous operationVessel pressurization calculatedAUXILLIARY EQUIPMENTO ther unit operations may be used with the batch reactor to fl exibly model the Process , including: dynamic vessel, heat exchanger, mixer, divider, separator, valve, pump, SYSTEM User specifi ed PID loopsMultiple ramp or step changes in setpointControl of reactor or jacket temperature differentialLevel controllersPressure controllersCascade controlHeat-cool-chill system with safety interlocksSplit range controllersKINETIC DATA REGRESSIONCan regress any combination of concentration, temperature volume and/