DWSIM/C2/Plug-Flow-Reactor/English

Visual Cue	Narration
Slide Number 1 Title Slide	Welcome to this spoken tutorial on Simulating a Plug Flow Reactor(PFR) in DWSIM.
Slide Number 2 Learning Objective	In this tutorial, we will learn to: Define a kinetic reaction Simulate a Plug Flow Reactor (PFR) Calculate Conversion and Residence time for a reaction in a PFR.
Slide Number 3 System Requirements	To record this tutorial, I am using DWSIM 4.3 and Windows 7 The process demonstrated in this tutorial is identical in other OS also, such as- Linux, Mac OS X or FOSSEE OS on ARM.
Slide Number 4 Pre-requisites	To practice this tutorial, you should know how to add components to a flowsheet how to select thermodynamic packages how to add material and energy streams and specify their properties.
Slide: Prerequisite Tutorials and Files	The prerequisite tutorials are mentioned on our website, spoken-tutorial.org You can access these tutorials and all the associated files from this site.
Slide Number 5 Reaction, Inlet Condition and Package. Reaction: N2 + 3 H2 ⇌ 2 NH3 Inlet Stream: Mass Flow: 3600 kg/h Mole Fraction(N2): 0.5 Mole Fraction(H2): 0.5 Temperature: 425 degree C Pressure: 200 bar Property Package: Peng Robinson(PR)	We will develop a flowsheet to determine the exit composition from an Isothermal PFR. Here we give reaction, property package and inlet stream conditions.
Slide Number 6 Reactor Parameters and Reaction Kinetics PFR Dimensions: Volume: 1 m3, length: 1.5 m Reaction rate: r A = KCan K = 0.004, n = 1	Next, we give Reactor Parameters and reaction kinetics.
File >> New Steady-state Simulation Point to Simulation Configuration Wizard window Click on Next.	I have already opened DWSIM on my machine. Go to File menu and select New Steady-state Simulation. Simulation Configuration Wizard window appears. At the bottom, click on Next.
Type Nitrogen in the Search tab ChemSep database >> Nitrogen Type Hydrogen in the Search tab Type Ammonia in the Search tab Click on Next.	First, we will add the compounds. In the Compounds Search tab, type Nitrogen. Select Nitrogen from ChemSep database. Similarly, add Hydrogen from ChemSep database. Next, add Ammonia from ChemSep database. Now, all the compounds are added. Click on Next.
Point to Property Packages Property Packages >> Available Property Package Double click on Peng-Robinson (PR) Click on Next.	Now comes Property Packages. From Available Property Packages, double-click on Peng-Robinson (PR). Then click on Next.
Point to Flash Algorithm Default Flash Algorithm >> Nested Loops (VLE) Click Next	We are moved to Flash Algorithm. From Default Flash Algorithm select Nested Loops(VLE) Click on Next.
Point to System of Units System of Units >> C5 Click on Finish	Next option is System of Units. So we select C5. This has the desired system of units according to our problem statement. Then click on Finish.
	Let us maximize the simulation window.
Point to Object Palette Go to Streams Section Click and drag Material Stream to the flowsheet	Now let’s insert a feed stream that enters the PFR. On the right hand side of main simulation window, go to Object Palette. From Streams section, drag and drop a Material Stream to the Flowsheet.
Click on MSTR-000	Click on Material Stream “MSTR-000” to view its properties.
Type Feed	Let’s change the name of this stream to Feed.
Input Data>> Flash Spec>> Temperature and Pressure(TP)	Now we will specify the Feed stream properties. Under Input Data, select Flash Spec as Temperature and Pressure (TP), if not already selected. By default, Temperature and Pressure are already selected as Flash Spec. So let’s not change it.
Input Data >> Temperature >> 425 C Press Enter	Change Temperature to 425 degC and press Enter to accept the new value.
Input Data >> Pressure >> 200 bar Press Enter	Change Pressure to 200 bar and press Enter.
Input Data >> Mass Flow >> 3600 kg/h Press Enter	Change Mass Flow to 3600 kg/h and press Enter.
	Now let us specify the feed stream compositions.
Composition >> Basis >> Mole Fractions	Under Composition, choose the Basis as Mole Fractions, if not already selected. By default, Mole Fractions is already selected as Basis. So, let’s not change it.
Nitrogen: 0.5 Hydrogen: 0.5 Ammonia: 0	Now for Nitrogen, enter the Amount as 0.5 and press Enter. Similarly, for Hydrogen, enter it as 0.5 and press Enter. For Ammonia, enter 0 and press Enter.
Click Accept Changes	On the right, click on this green tick to Accept Changes.
	Now we will define the Kinetic Reaction.
Tools >> Reactions Manager Point to Chemical Reactions Manager	Under Tools, click on Reactions Manager. Chemical Reactions Manager window opens.
Chemical Reactions >> Add Reaction	Under Chemical Reactions tab, click on the green coloured Add Reaction button.
Click on Kinetic	Then click on Kinetic.
Point to Add New Kinetic Reactions	Add New Kinetic Reactions window opens.
Identification >> Name >> Ammonia Synthesis	First part is Identification. Under Identification, enter the Name as Ammonia Synthesis.
Description >> Irreversible reaction for synthesis of Ammonia from Nitrogen and Hydrogen	Next, enter the Description. “Irreversible reaction for synthesis of Ammonia from Nitrogen and Hydrogen”
Point to Components, Stoichiometry and Reaction Orders	Next part is a table of Components, Stoichiometry and Reaction Orders.
Point to Name field	First column Name, shows the available components here.
Point to Molar Weight	Second column corresponds to its Molar Weight.
Point to Include	Next column is Include. It indicates the components which will take part in the reaction. Under Include, check all the check boxes against all the components’ names.
Point to BC Check Nitrogen check box	Fourth column is BC. It indicates the base component of the reaction. Under BC, check the Nitrogen check box as Nitrogen is the base component.
Point to Stoich. Coeff Stoich. Coeff >> Nitrogen: -1, Hydrogen: -3, Ammonia: 2	Next column is Stoich. Coeff. (stoichiometric coefficients) Under Stoic Coeff column, enter: -1 for Nitrogen, -3 for Hydrogen, and for Ammonia 2 Then press Enter. Negative sign is to indicate the components as Reactants.
Point to Stoichiometry field	In the Stoichiometry field, we can see it is showing OK. So the reaction is balanced after entering the stoichiometric coefficients.
Point to Equation field	Here the Equation field shows the reaction equation.
Point to DO DO >> Nitrogen: 1	Next column is DO, which indicates direct/forward reaction order. We are considering the reaction to be First order with respect to Nitrogen. So we will enter 1 in the DO column against Nitrogen. And then press Enter.
Point to RO	Next column is RO which indicates reverse reaction order. Since we are considering an irreversible reaction, we will not enter anything here.
Point to Kinetic Reactions Parameters	Then comes Kinetic Reactions Parameters.
Basis >> Molar Concentrations	Our rate is in terms of molar concentration. So, we will select Basis as Molar Concentrations.
Fase >> Vapor	Select Fase as Vapor.
Point to Tmin and Tmax	Next is Tmin and Tmax. It gives temperature range within which rate expression is assumed to be valid.
Tmin (K) >> 700 Tmax (K) >> 2000	So, enter Tmin (K) as 500 and Tmax (K) as 2000.
Point to Direct and Reverse Reactions Velocity Constant Direct Reaction: A >> 0.004	Now go to Direct and Reverse Reactions Velocity Constant. In Direct Reaction, enter A as 0.004
Click OK Close Chemical Reactions Manager window.	Click OK and close the Chemical Reactions Manager window.
Go to Object Palette>>Unit Operations Click and drag Plug-Flow Reactor (PFR) to the flowsheet	Now let us insert a Plug-Flow Reactor (PFR) into the flowsheet. Go to Object Palette. Under Unit Operations, click on Plug-Flow Reactor (PFR) Click on it and drag it to the flowsheet. Let us now arrange it as required.
Click and drag Material Stream to the flowsheet	We will insert one Output Stream. To do so, drag one Material Stream. Let us once again arrange it. As this is an output stream, we will leave it unspecified.
Type Product	We will change the name of this stream to Product.
Click and drag Energy Stream to the flowsheet	Next, we will insert one Energy Stream.
Type Energy.	And name this stream as Energy.
Click Plug-Flow Reactor (PFR)	We are now ready to specify the Plug-Flow Reactor. Click on it. On the left, we can see a tab displaying properties related to the PFR. This tab is called Property Editor Window.
Go to Connections Click on drop down arrow against Inlet Stream Select Feed.	Under Connections, click on the drop-down against Inlet Stream. And select Feed.
Click on drop down arrow against Outlet Stream Select Product.	Next, click on the drop-down against Outlet Stream and select Product.
Click on the drop down against Energy Stream Select Energy.	Then click on the drop-down against Energy Stream and select Energy.
Hover mouse at Calculation Parameters	Now go to the next section, Calculation Parameters.
Reaction Set >> Default Set	Here, the first option is Reaction Set. By default, it is Default Set. Since we have only one reaction, we leave it as it is.
Click drop down against Calculation Mode Select Isothermic	Next, click on the drop-down against Calculation Mode. Select Isothermic.
Reactor Volume >> 1 m3 Press Enter	Then click on the field against Reactor Volume and enter 1 m3. Then press Enter.
Reactor Length >> 1.5 m Press Enter	Click on the field against Reactor length and enter it as 1.5 m. Then press Enter.
	Now we will run the simulation.
Click Solve Flowsheet	So, from the toolbar click on Solve Flowsheet button.
Click Plug-Flow Reactor	When the calculations are completed, click on PFR in the Flowsheet.
Hover mouse at Results	From the Property Editor Window of PFR locate Results section.
Results >> General	Under General tab, check Residence time. It is 0.013 h.
Results >> Conversions	Under Conversions tab, check conversion for both the reacting compounds. For Nitrogen, the conversion is 17.91% and for Hydrogen, it is 53.73%.
Insert >> Master Property Table	Now we will check the material balances. Go to Insert menu and select Master Property Table.
Double click on Master Property Table Point to Configure Master Property Table	Double click on the Master Property Table to edit it. Configure Master Property Table window opens.
Type Results - Plug Flow Reactor	Enter Name as Results - Plug Flow Reactor
Type Material Stream	Enter Object Type as Material Stream. By default, Material Stream is already selected. So we will not change it.
Object >> Feed and Product	Under Properties to display, select Object as Feed and Product.
Configure Master Property Table>> Property	Under Property, scroll down to see all the parameters. Now select the properties as: Temperature Pressure Mass Flow Molar Flow Vapor Phase Volumetric Fraction Molar Flow (Mixture) / Nitrogen Mass Flow (Mixture) / Nitrogen Molar Flow (Mixture) / Hydrogen Mass Flow (Mixture) / Hydrogen Molar Flow (Mixture) / Ammonia Mass Flow (Mixture) / Ammonia
	Close this window. Move the Master Property Table for better visibility. Here we can see the corresponding results for Product and Feed.
	Let us summarize.
Slide Number 7 Summary	In this tutorial, we have learnt to Define a kinetic reaction Simulate a Plug-Flow Reactor (PFR) Calculate Conversion and Residence time for a reaction in a PFR
Slide Number 8 Assignment Compounds: Ethylene oxide, Water & Ethylene glycol C2H4O + H2O ⇌ C2H6O2 Property Package: Raoult's Law Inlet stream: Mass Flow: 1000kg/h Mole Fraction(C2H4O): 0.2 Mole Fraction(H2O): 0.8 Temperature: 55 degree C Pressure: 1 bar PFR Dimensions: Volume: 1 m3, Length: 1.2 m Reaction rate: r A = KCan, K = 0.005 1/s, n = 1	As an assignment, Repeat this simulation with different compounds and thermodynamics. Different feed conditions Different PFR dimensions and reaction kinetics
Slide Number 9 About the Spoken Tutorial Project	Watch the video available at following link. http://spoken-tutorial.org/ It summarizes the Spoken Tutorial project.
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Slide Number 11 Forum Slide Do you have questions in this Spoken Tutorial? Please visit this site Choose the minute and second where you have the question. Explain your question briefly. Someone from the FOSSEE team will answer them.	Please post your times queries in this forum.
Slide Number 12 TextBook Companion Project	The FOSSEE team coordinates coding of solved examples of popular books. We give honorarium and certificates for those who do this. For more details, please visit this site.
Slide Number 13 Lab Migration Project	The FOSSEE team helps migrate commercial simulator labs to DWSIM. We give honorarium and certificates for those who do this. For more details, please visit this site
Slide Number 14 DWSIM Flowsheeting Project	The FOSSEE team coordinates conversion of existing flow sheets into DWSIM. We give honorarium and certificates for those who do this. For more details, please visit this site.
Slide Number 15 Acknowledgements	Spoken Tutorial and FOSSEE projects are funded by NMEICT, MHRD, Government of India.
Slide Number 16 Thanks	This tutorial is contributed by Kaushik Datta and Priyam Nayak. Thanks for joining.

Contributors and Content Editors

Kaushik Datta, Nancyvarkey