Process Simulation using DWSIM
P. R. Naren
School of Chemical & Biotechnology
SASTRA University
E-mail: prnaren@scbt.sastra.edu
National Conference on Advances in Process Engineering
CAPE-2015
SASTRA University
Thanjavur, Tamilnadu 613 401 INDIA
10th October 2015
Progress Through Quality Education
Outline
• Process Simulation and Simulation Tools
• DWSIM
• Spoken Tutorials – IITB
• Tutorials on process simulation using DWSIM
10-Oct-15 Process Simulation using DWSIM
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Process Simulation
• Perform material and energy balance
• Performance of equipment for given design
• Sensitivity analysis
• What-If analysis
• Process synthesis and comparison
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DWSIM
• Process Simulator
• Steady State
• Thermodynamic Models
• Unit Operations
• Free & Open Source
• CAPE Open Complaint
http://dwsim.inforside.com.br/
https://en.wikipedia.org/wiki/DWSIM
http://dwsim.fossee.in/
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Daniel Medeiros
Process Engineer, Petrobras
FOSSEE Project
• Free and Open Source Software for Education
• FOSSEE on DWSIM: http://dwsim.fossee.in/
• Spoken Tutorials
 10 min short videos on DWSIM http://spoken-tutorial.org/
 Forum to post queries on videos
– Textbook Companion Project
 http://dwsim.fossee.in/Textbook_Companion_Project
 Code all solved examples of standard textbook
 Get paid ! Honorarium from IITB
– Lab Migration Project
 Convert process simulation lab to DWSIM
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Dr. Kannan Moudgalya
Chemical Engg., IITB
Tutorials
• Creation of material streams
• Creation of simple process flow sheet
• Thermodynamics
– Thermo physical properties of components
– VLE data of binary component system
• Process Units
– Mixer
– Simple heater
– Simple distillation column
– Flash column
– Equilibirum reactor
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Tutorial 1
Specification of Material Stream and Composition
• Objective
– Create material stream
– Specify composition
– Operating condition (Pressure, Temperature, State –
Thermodynamics)
• Spoken Tutorial
• Data
– Components: Benzene and Toluene
– Composition: Equimolar
– Thermodynamics: Raoults Law
– Pressure: 1 atm
– Temperature: 30oC
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Tutorial 2
Generation of Vapour Liquid Equilibrium (VLE) data
• Objective
– Generate binary component VLE (Pxy at T or Txy
at P, y vs. x)
• Data
– Components: Benzene and Toluene
– Pressure: 1 atm
Generate Txy, y vs. x
– Temperature: 50oC
Generate Pxy, y vs x
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Tutorial 3
Mixing of Two Liquid Streams
• Objective
– Mix two liquid streams and estimate the flow rate and composition of outlet
stream
• Data
– Inlet stream 1: 10 mol % Methanol solution at 20 kmol/hr
– Inlet stream 2: 80 mol % Methanol solution at 10 kmol/hr
– Both the streams are at 30oC and at 1 atm pressure
– The liquid streams can be considered as ideal
• Block
– Mixer
• Output
– Outlet molar flow rate
– Composition
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Tutorial 4
Heat duty through Simulation of Heater Block
• Objective
– Determine the heat duty required to heat a fluid to a desired temperature
• Data
– Fluid: Water
– Inlet mass flow rate: 50 kg/hr
– Inlet temperature: 25oC
– Outlet temperature: 90oC
– Pressure: 1 bar
• Block
– Heater
• Output
– Heat Duty
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Tutorial 5
Simulation of a Simple Distillation Column
• Objective
– Develop a simple process sheet to simulate distillation column
– Underwood Fenske Method
• Spoken Tutorial
• Output
– Minimum reflux
– Min. no. of stages
– Condenser duty
– Re-boiler duty
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Quantity Value
Components Benzene, Toluene
Thermodynamics Ideal – Raoult’s Law
Feed
Molar flow rate
Mol fraction
State
100 kmol/hr
xF = 0.4
Saturated Liquid at P = 1 bar
Reflux 2
Product Bottoms: xB = 0.05
Distillate: xD = 0.95
Tutorial 6
Simulation of a Simple Process Flow Sheet – Mixer and Flash
Column
• Objective
– Develop process sheet with Mixer and Flash Column
 Mix two streams
 Outlet from mixer is sent to flash column
 Estimate the vapour and liquid outlet
• Spoken Tutorial
• Output
– Vapour composition
– Liquid composition
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Tutorial 7
Simulation of Equilibirum Reactor
• Objective
– Simulate equilibrium reactor to estimate conversion for reversible reaction
(known stoichiometry)
• Data
– Reversible reaction – Water Gas Shift
– Operating temperature: 900 K, Operating pressure: 1 atm
– Inlet flow rate: 100 kmol/hr
– Composition: stoichiometric ratio of CO and H2O
• Block
– Equilibrium Reactor
• Output
– Equilibrium conversion in terms of base component
– Enthalpy of reaction
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       2 2g g 2 g g
CO H O CO H 
To Sum Up
• DWSIM – Effective and promising open source
process simulation tool
• Complement learning process through simulation of
difference process scenarios
10-Oct-15 Process Simulation using DWSIM
14
Gratitude
• Prof Kannan Moudgalya, IITB
– M. Neelesh Chandran, Chemical Engg., SASTRA
– C. S. Vighnesh, Chemical Engg., SASTRA
• CAPE-2015 and IIChE Student Chapter
– For this wonderful opportunity
– PR Team for their registration drive !!
– Technical and Infra support team
• Audience
10-Oct-15 Process Simulation using DWSIM
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THANK YOU
A person who never made a mistake never tried
anything new
- Albert Einstein
- 1879 -1955
Entities must not be
multiplied beyond necessity
- William of Ockham
- 12th A.D.
10-Oct-15 Process Simulation using DWSIM
16

Process Simulation using DWSIM

  • 1.
    Process Simulation usingDWSIM P. R. Naren School of Chemical & Biotechnology SASTRA University E-mail: prnaren@scbt.sastra.edu National Conference on Advances in Process Engineering CAPE-2015 SASTRA University Thanjavur, Tamilnadu 613 401 INDIA 10th October 2015 Progress Through Quality Education
  • 2.
    Outline • Process Simulationand Simulation Tools • DWSIM • Spoken Tutorials – IITB • Tutorials on process simulation using DWSIM 10-Oct-15 Process Simulation using DWSIM 2
  • 3.
    Process Simulation • Performmaterial and energy balance • Performance of equipment for given design • Sensitivity analysis • What-If analysis • Process synthesis and comparison 10-Oct-15 Process Simulation using DWSIM 3
  • 4.
    DWSIM • Process Simulator •Steady State • Thermodynamic Models • Unit Operations • Free & Open Source • CAPE Open Complaint http://dwsim.inforside.com.br/ https://en.wikipedia.org/wiki/DWSIM http://dwsim.fossee.in/ 10-Oct-15 Process Simulation using DWSIM 4 Daniel Medeiros Process Engineer, Petrobras
  • 5.
    FOSSEE Project • Freeand Open Source Software for Education • FOSSEE on DWSIM: http://dwsim.fossee.in/ • Spoken Tutorials  10 min short videos on DWSIM http://spoken-tutorial.org/  Forum to post queries on videos – Textbook Companion Project  http://dwsim.fossee.in/Textbook_Companion_Project  Code all solved examples of standard textbook  Get paid ! Honorarium from IITB – Lab Migration Project  Convert process simulation lab to DWSIM 10-Oct-15 Process Simulation using DWSIM 5 Dr. Kannan Moudgalya Chemical Engg., IITB
  • 6.
    Tutorials • Creation ofmaterial streams • Creation of simple process flow sheet • Thermodynamics – Thermo physical properties of components – VLE data of binary component system • Process Units – Mixer – Simple heater – Simple distillation column – Flash column – Equilibirum reactor 10-Oct-15 Process Simulation using DWSIM 6
  • 7.
    Tutorial 1 Specification ofMaterial Stream and Composition • Objective – Create material stream – Specify composition – Operating condition (Pressure, Temperature, State – Thermodynamics) • Spoken Tutorial • Data – Components: Benzene and Toluene – Composition: Equimolar – Thermodynamics: Raoults Law – Pressure: 1 atm – Temperature: 30oC 10-Oct-15 Process Simulation using DWSIM 7
  • 8.
    Tutorial 2 Generation ofVapour Liquid Equilibrium (VLE) data • Objective – Generate binary component VLE (Pxy at T or Txy at P, y vs. x) • Data – Components: Benzene and Toluene – Pressure: 1 atm Generate Txy, y vs. x – Temperature: 50oC Generate Pxy, y vs x 10-Oct-15 Process Simulation using DWSIM 8
  • 9.
    Tutorial 3 Mixing ofTwo Liquid Streams • Objective – Mix two liquid streams and estimate the flow rate and composition of outlet stream • Data – Inlet stream 1: 10 mol % Methanol solution at 20 kmol/hr – Inlet stream 2: 80 mol % Methanol solution at 10 kmol/hr – Both the streams are at 30oC and at 1 atm pressure – The liquid streams can be considered as ideal • Block – Mixer • Output – Outlet molar flow rate – Composition 10-Oct-15 Process Simulation using DWSIM 9
  • 10.
    Tutorial 4 Heat dutythrough Simulation of Heater Block • Objective – Determine the heat duty required to heat a fluid to a desired temperature • Data – Fluid: Water – Inlet mass flow rate: 50 kg/hr – Inlet temperature: 25oC – Outlet temperature: 90oC – Pressure: 1 bar • Block – Heater • Output – Heat Duty 10-Oct-15 Process Simulation using DWSIM 10
  • 11.
    Tutorial 5 Simulation ofa Simple Distillation Column • Objective – Develop a simple process sheet to simulate distillation column – Underwood Fenske Method • Spoken Tutorial • Output – Minimum reflux – Min. no. of stages – Condenser duty – Re-boiler duty 10-Oct-15 Process Simulation using DWSIM 11 Quantity Value Components Benzene, Toluene Thermodynamics Ideal – Raoult’s Law Feed Molar flow rate Mol fraction State 100 kmol/hr xF = 0.4 Saturated Liquid at P = 1 bar Reflux 2 Product Bottoms: xB = 0.05 Distillate: xD = 0.95
  • 12.
    Tutorial 6 Simulation ofa Simple Process Flow Sheet – Mixer and Flash Column • Objective – Develop process sheet with Mixer and Flash Column  Mix two streams  Outlet from mixer is sent to flash column  Estimate the vapour and liquid outlet • Spoken Tutorial • Output – Vapour composition – Liquid composition 10-Oct-15 Process Simulation using DWSIM 12
  • 13.
    Tutorial 7 Simulation ofEquilibirum Reactor • Objective – Simulate equilibrium reactor to estimate conversion for reversible reaction (known stoichiometry) • Data – Reversible reaction – Water Gas Shift – Operating temperature: 900 K, Operating pressure: 1 atm – Inlet flow rate: 100 kmol/hr – Composition: stoichiometric ratio of CO and H2O • Block – Equilibrium Reactor • Output – Equilibrium conversion in terms of base component – Enthalpy of reaction 10-Oct-15 Process Simulation using DWSIM 13        2 2g g 2 g g CO H O CO H 
  • 14.
    To Sum Up •DWSIM – Effective and promising open source process simulation tool • Complement learning process through simulation of difference process scenarios 10-Oct-15 Process Simulation using DWSIM 14
  • 15.
    Gratitude • Prof KannanMoudgalya, IITB – M. Neelesh Chandran, Chemical Engg., SASTRA – C. S. Vighnesh, Chemical Engg., SASTRA • CAPE-2015 and IIChE Student Chapter – For this wonderful opportunity – PR Team for their registration drive !! – Technical and Infra support team • Audience 10-Oct-15 Process Simulation using DWSIM 15
  • 16.
    THANK YOU A personwho never made a mistake never tried anything new - Albert Einstein - 1879 -1955 Entities must not be multiplied beyond necessity - William of Ockham - 12th A.D. 10-Oct-15 Process Simulation using DWSIM 16