Kaushik Datta at 06:52, 2 August 2019

2019-08-02T06:52:38Z

Kaushik Datta: Created page with "{|border=1 ||'''Visual Cue''' ||'''Narration''' |- || '''Slide Number 1''' ''' Title Slide''' || Welcome to this tutorial on Simulating a '''PFR '''using '''Heterogeneous Cata..."

2019-06-17T11:58:24Z

Created page with "{|border=1 ||'''Visual Cue''' ||'''Narration''' |- || '''Slide Number 1''' ''' Title Slide''' || Welcome to this tutorial on Simulating a '''PFR '''using '''Heterogeneous Cata..."

New page

{|border=1
||'''Visual Cue'''
||'''Narration'''
|-
|| '''Slide Number 1'''
''' Title Slide'''
|| Welcome to this tutorial on Simulating a '''PFR '''using '''Heterogeneous Catalytic Reaction '''in''' DWSIM.'''
|-
|| '''Slide Number 2'''
'''Learning Objective'''
|| In this tutorial, we will learn to:

* Define a '''Heterogeneous Catalytic''' reaction
* Define parameters for '''PFR '''required to simulate a '''Heterogeneous Catalytic Reaction'''
* Calculate '''Conversion''' and '''Residence time''' for '''Heterogeneous Catalytic Reaction''' in a '''PFR'''

|-
|| '''Slide Number 3'''
'''System Requirements'''
|| To record this tutorial, I am using

* '''DWSIM 5.7 Update 8 '''and
* '''Windows 10'''

The process demonstrated in this tutorial is identical in other OS also such as-* '''Ubuntu Linux''',
* '''Mac OS X''' or
* '''FOSSEE OS''' on '''ARM'''.

|-
|| '''Slide Number 4'''

'''Pre-requisites '''
|| To practice this tutorial, you should know to-

* add components to a '''flowsheet'''
* select '''thermodynamic''' packages
* add '''material''' and '''energy''' streams and specify their properties.

|-
|| '''Slide Number 5'''

'''Prerequisite Tutorials and Files'''

'''https:\\spoken-tutorial.org'''
|| The prerequisite tutorials are available on this website'''.'''

You can access these tutorials and all the associated files from this site.
|-
|| '''Slide Number 6 '''

'''Problem Statement'''

Reaction: '''CH4 + H2O ⇔ 3H2 + CO'''

'''Inlet Stream: '''

Mass Flow: 300 kg/h

Mole Fraction(CH4): 0.4975

Mole Fraction(H2O): 0.4975

Mole Fraction(H2): 0.005

Temperature: 730 degree C

Pressure: 1.01325 bar

'''Property Package: '''Peng Robinson(PR)

'''PFR Dimensions:'''

Volume: 1 m3, length: 1 m
|| We will develop a flowsheet to determine the exit composition from an Isothermal '''PFR '''with '''Heterogeneous Catalytic Reaction'''.

Here we give '''Inlet stream conditions''', '''Property package''' and '''Reactor Parameters.'''

|-
|| '''Slide Number 7'''

'''Catalyst Properties:'''

'''Loading: '''0.386 kg/m3

'''Particle Diameter:''' 0.002 m

'''Void Fraction:''' 0.4

'''Gas Constant: '''R = 8.314 J/mol-K
|| Next, we give the '''Catalyst properties and Gas constant.'''
|-
|| '''Slide Number 8'''

'''Reaction Rate and Coefficients:'''

R1 = [k1/PH22.5 {PCH4 PH2O - PH23 PCO / K1}] / DEN2

'''Reaction Rate '''

k1 = 4.22 * 10 15 exp (- 240100/RT)

K1 = exp (30.42 - 27106/T)

DEN = 1 + KCH4 PCH4 + KCO PCO + KH2 PH2 + KH2O PH2O/PH2

|| Now we give the '''reaction rate''' and its '''coefficients'''.

|-
|| '''Slide Number 9'''

'''Reaction Rate Coefficients'''

k1 = 6.65 * 10-4 exp (38280/RT)

k1 = 1.77 * 105 exp (- 88680/RT)

k1 = 6.12 * 10-9 exp (82920/RT)

k1 = 8.23 * 10-5 exp (70650/RT)

|| Here we give the '''reaction rate''' '''coefficients'''.
|-
||
|| Before we start the simulation, we will simplify the rate expression.
|-
||
|| We will substitute the coefficients in the rate for the numerator and denominator separately.

This will be helpful when we have to enter the reaction rate for '''Heterogeneous Catalytic reaction'''.
|-
||
|| In the rate expression, we will assign the variables for partial pressure of '''reactants''' and '''products'''.
|-
|| '''Slide Number 10'''

'''Reactants: R'''

'''PCH4: R1, PH2O: R2'''

'''Products: P'''

'''PH2: P1, PCO: P2'''
|| '''R''' corresponds to '''reactants.'''

Partial pressure of '''Methane(CH4)''' is '''R1''' and '''Water(H2O)''' is '''R2'''.

'''P''' corresponds to '''products'''.

So partial pressure of '''Hydrogen(H2)''' is '''P1''' and '''Carbon monoxide(CO)''' is '''P2'''.
|-
|| '''Slide Number 11'''

Numerator of R1 = k1/PH22.5 {PCH4 PH2O - PH23 PCO / K1}

Substituting for''' k'''1''', PH2, PCH4, PH3, PCO '''and''' K1, '''we get

4.22E+15*exp(-240100/(8.314*T))/P12.5*((R1*R2)-(P13*P2)/(exp(30.42-27106/T)))
|| The numerator term in the rate expression is this.

Substituting the values of '''k1''', '''K1''' and '''partial pressure''' terms, the numerator becomes like this.
|-
|| '''Slide Number 12'''

Denominator of R1 = [1 + KCH4 PCH4 + KCO PCO + KH2 PH2 + KH2O PH2O/PH2] 2

Substituting for '''KCH4''', '''PCH4''', '''KCO''', '''PCO''', '''KH2''', '''PH2''', '''KH2O''' and '''PH2O''', we get

(1+6.65E-4*exp(38280/(8.314*T))*R1+8.23E-5*exp(70650/(8.314*T))*P2+6.12E-9*exp(82900/(8.314*T))*P1+1.77E+5*exp(-88680/(8.314*T))*R2/P1)^2
|| The denominator term in the rate expression is this.

Substituting the values of '''KCH4''', '''KCO''', '''KH2''', '''KH2O''' and '''partial pressure''' terms, the denominator becomes like this.
|-
||
|| We have simplified the rate expression to be entered in '''DWSIM'''.

Now we will start the simulation.
|-
|| '''File''' >> '''New Steady-state Simulation '''
|| I have already opened '''DWSIM'''.

Go to '''File''' menu and select '''New Steady-state Simulation.'''
|-
|| Point to '''Simulation Configuration Wizard''' window
|| '''Simulation Configuration Wizard''' window appears.
|-
|| Click on '''Next '''button.
|| Click on '''Next '''button.
|-
||
|| First, we will add the compounds.
|-
|| Type '''Methane '''in the '''Search''' tab

'''ChemSep '''database >> '''Methane'''

Check the checkbox under column '''Added'''
|| In the '''Compounds Search '''tab, type '''Methane.'''

Select '''Methane '''from '''ChemSep '''database.

Check the checkbox under column '''Added'''.
|-
|| Type '''Water '''in the '''Search''' tab
|| Next, add '''Water''' from '''ChemSep '''database.
|-
|| Type '''Hydrogen '''in the '''Search''' tab
|| Then, add '''Hydrogen''' from '''ChemSep '''database.
|-
|| Type '''Carbon monoxide '''in the '''Search''' tab
|| Next, add '''Carbon monoxide''' from '''ChemSep '''database.
|-
|| Type '''Carbon dioxide '''in the '''Search''' tab
|| Next, add '''Carbon dioxide''' from '''ChemSep '''database.

Now, all the compounds are added.
|-
|| Click on '''Next.'''
|| Click on '''Next '''button'''.'''
|-
|| Point to '''Property Packages'''
|| Next is '''Property Packages.'''
|-
|| '''Property Packages''' >> '''Available Property Package'''

Double click on '''Peng-Robinson (PR)'''
|| From '''Available Property Package''' list, double click on '''Peng-Robinson (PR) '''option.
|-
|| Click on '''Next.'''
|| Then click on the '''Next '''button.
|-
|| Point to '''System of Units'''
|| Next option is '''System of Units.'''
|-
|| '''System of Units >> C5'''
|| Under '''System of Units, '''we will select '''C5'''.
|-
|| Click on''' Finish'''
|| Then at the bottom, click on the '''Finish '''button.
|-
|| Click on '''Maximize''' button
|| Let us maximize the simulation window.
|-
|| Cursor on the simulation window.
|| Now insert a feed stream that enters the '''Reactor'''.
|-
|| Point to '''Streams.'''
|| At the bottom of the main simulation window, go to '''Streams.'''
|-
|| Click and drag '''Material Stream '''to the flowsheet
|| From the displayed list, drag and drop '''Material Stream '''to the '''Flowsheet'''.
|-
|| Click '''MSTR-000'''
|| Click on the material stream named '''MSTR-000.'''
|-
|| Type '''Feed'''
|| Let’s change the name of this '''stream''' to '''Feed.'''
|-
||
|| Now we will specify the Feed''' stream''' properties.
|-
|| '''Stream Conditions >> Flash Spec >> Temperature and Pressure (TP)'''
|| Go to '''Input Data.'''

Under '''Stream Conditions tab''', select '''Flash Spec''' as '''Temperature and Pressure (TP),''' if not already selected.
|-
|| Point to the default temperature and pressure.
|| By default, '''Temperature '''and''' Pressure '''are already selected as '''Flash Spec.'''
|-
|| '''Stream Conditions >>Temperature >> 730 C'''

Press '''Enter'''
|| Change '''Temperature''' to '''730 degree C''' and press '''Enter.'''
|-
|| '''Stream Conditions >> Pressure >> 1.01325 bar'''

Press '''Enter'''
|| Change '''Pressure''' to '''1.01325 bar''' and press '''Enter.'''
|-
|| '''Stream Conditions >> Mass Flow >> 300 kg/h'''

Press '''Enter'''
|| Change '''Mass Flow''' to '''300 kg/h''' and press '''Enter.'''
|-
|| '''Input Data '''>>''' Compound Amounts'''
|| Now let us specify the '''Feed stream compositions.'''

For this click on '''Compound Amounts''' tab under '''Input Data.'''
|-
|| '''Basis >> Mole Fractions'''
|| Choose the '''Basis''' as '''Mole Fractions''', if not already selected.

By default, '''Mole Fractions''' is already selected as the '''Basis.'''
|-
|| '''Methane: 0.4975'''
|| Now for '''Methane''', enter the '''Amount''' as '''0.4975''' and press '''Enter.'''
|-
|| '''Water: 0.4975'''
|| For '''Water, '''enter '''0.4975''' and press '''Enter'''.
|-
|| '''Hydrogen: 0.005'''
|| For '''Hydrogen, '''enter '''0.005''' and press '''Enter'''.
|-
|| '''Carbon monoxide: 0'''
|| For '''Carbon monoxide, '''enter '''0''' and press '''Enter'''.
|-
|| '''Carbon dioxide: 0'''
|| For '''Carbon dioxide''',''' '''enter '''0''' and press '''Enter'''.
|-
|| Click '''Accept Changes '''button
|| On the right, click on the '''Accept Changes''' button.
|-
||
|| Now we will define the '''Heterogeneous Catalytic Reaction.'''
|-
|| '''Edit>> Simulation Settings'''

Click '''Reactions'''
|| Under '''Edit''', Click on '''Simulation Settings.'''

Click on the tab '''Reactions.'''
|-
|| '''Chemical Reactions >> Add Reaction'''
|| Under '''Chemical Reactions''' tab, click on the green coloured '''Add Reaction''' button.
|-
|| Click on '''Heterogeneous Catalytic'''
|| Click on '''Heterogeneous Catalytic.'''
|-
|| Point to '''Heterogeneous Catalytic Reaction'''
|| '''Heterogeneous Catalytic Reaction '''window opens.
|-
|| '''Identification >> Name''' '''>> Steam Reforming'''
|| Under '''Identification,''' enter the '''Name''' as '''Steam Reforming.'''
|-
|| '''Description >> Catalytic Reaction for Steam Reforming'''
|| Next, enter the '''Description '''as,

“'''Catalytic Reaction for Steam Reforming'''”
|-
|| Point to '''Components and Stoichiometry'''
|| Next part is a table of '''Components and Stoichiometry.'''
|-
|| 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 '''Heat of Formation'''
|| Third column corresponds to its '''Heat of Formation.'''
|-
|| Point to '''Include'''
|| Next column is '''Include.'''

Under '''Include''', check the check boxes against '''Methane''', '''Water''', '''Hydrogen''' and '''Carbon monoxide'''.
|-
||
|| '''Carbon dioxide''' doesn’t take part in this reaction.

We will keep it unchecked.
|-
|| Point to '''BC'''

Check '''Methane''' check box
|| Fourth column is '''BC.'''

Under '''BC''', check the '''Methane''' check box as '''Methane '''is the base component.
|-
|| Point to '''Stoich. Coeff'''
|| Next column is '''Stoich. Coeff. (stoichiometric coefficients)'''
|-
||

'''Stoich. Coeff >> Methane: -1,

'''Water: -1'''

'''Hydrogen: 3,'''

'''Carbon monoxide: 1,'''

'''Carbon dioxide: 0''''''
|| Under '''Stoic Coeff''' column, enter

'''-1''' for '''Methane'''

'''-1''' for '''Water'''

'''3 '''for''' Hydrogen'''

'''1''' for '''Carbon monoxide'''

'''0''' for '''Carbon dioxide'''

Then press Enter.
|-
|| Point to '''Stoichiometry '''field
|| In the '''Stoichiometry '''field, we can see it is showing '''OK'''.
|-
|| Point to '''Equation '''field
|| Here''' '''the '''Equation '''field shows the reaction equation'''.'''
|-
|| Point to '''Heterogeneous Kinetic Reaction Parameters'''
|| Next part is '''Heterogeneous Kinetic Reaction Parameters.'''
|-
|| '''Basis >> Partial Pressures'''
|| Select '''Basis''' as '''Partial Pressures.'''
|-
|| '''Phase >> Vapor'''
|| Select '''Phase''' as '''Vapor.'''
|-
|| Leave '''Tmin''' and '''Tmax''' unchanged.
|| We will leave '''Tmin''' and '''Tmax''' field as unchanged.
|-
||
|| Now we will specify the reaction rate.
|-
|| Point to '''Reaction Rate(Base Component)'''
|| Go to '''Reaction Rate (Base Component) = Numerator/Denominator.'''
|-
|| Point to '''Numerator''' and '''Denominator''' field.
|| The reaction rate is to be entered separately as '''Numerator''' and '''Denominator.'''

We have already simplified the '''Numerator''' and '''Denominator''' part separately.
|-
|| Point to '''Numerator'''

'''Type '''

'''4.22E+15*exp(-240100/(8.314*T))/P1^2.5*((R1*R2)-(P1^3*P2)/(exp(30.42-27106/T)))'''
|| We will enter the '''Numerator''' part first.

Type the equation as shown here.
|-
|| Point to '''Denominator'''

'''Type'''

'''(1+6.65E-4*exp(38280/(8.314*T))*R1+8.23E-5*exp(70650/(8.314*T))*P2+6.12E-9*exp(82900/(8.314*T))*P1+1.77E+5*exp(-88680/(8.314*T))*R2/P1)^2'''
|| Now we will enter the '''Denominator''' part.

Type the equation as shown here.
|-
||
|| Now we will specify the units for '''Amount''' and '''Velocity'''.
|-
|| '''Amount Unit >> atm'''
|| Select '''Amount Unit''' as '''atm''' from the dropdown.

The '''Reaction Rate '''is expressed in terms of '''Partial Pressure, '''whose unit is '''atm.'''
|-
|| '''Velocity Unit >> kmol/[kg.h]'''
|| From the drop-down select '''Velocity Unit''' as '''kmol/[kg.h].'''

This is the unit for the '''Reaction Rate'''.
|-
|| Click '''OK'''
|| Click''' '''on '''OK''' button.
|-
|| Click on '''Flowsheet'''
|| Now go back to '''Flowsheet''' area.
|-
||
|| We will use a '''Plug Flow Reactor''' for the simulation.
|-
|| Cursor to''' Reactors''' tab
|| At the bottom of the main simulation window, go to '''Reactors '''tab.
|-
|| Click and drag '''Plug-Flow Reactor(PFR)''' to the flowsheet
|| Drag and drop '''Plug-Flow Reactor(PFR)''' to the flowsheet area.
|-
||
|| Let us arrange it as required.
|-
||
|| And then let us insert one '''Output Stream'''.
|-
|| Click and drag '''Material Stream''' to the flowsheet
|| To do that let us drag one '''Material Stream.'''
|-
||
|| Let us once again arrange it in the flowsheet.
|-
||
|| Leave that stream as unspecified.
|-
|| Type '''Product'''
|| We will change the name of this stream to '''Product.'''
|-
|| Click and drag '''Energy Stream''' to the flowsheet
|| Let us now insert one '''Energy Stream.'''
|-
|| Type '''Energy.'''
|| Name this stream as '''Energy.'''
|-
||Click '''Plug-Flow Reactor (PFR)'''
|| We are now ready to specify the '''Plug-Flow Reactor.'''

So let’s click on it.
|-
|| Point to the tab on the left.
|| On the left, we can see a tab displaying properties related to the '''PFR.'''
|-
|| Go to a'''Connections'''

Click on drop down arrow against '''Inlet Stream'''

Select''' Feed.'''
|| Under '''Connections,''' click on the drop down against '''Inlet Stream.'''

Select '''Feed.'''
|-
|| Click on drop down arrow against '''Outlet Stream'''

Select''' Product.'''
|| Click on the drop down against '''Outlet Stream''' and select '''Product.'''
|-
|| Click on the drop down against '''Energy Stream'''

Select''' Energy.'''
|| Click on the drop down against '''Energy Stream''' and select '''Energy.'''
|-
|| Hover mouse at '''Calculation Parameters'''
|| Now, Go to '''Calculation Parameters.'''
|-
|| '''Reaction Set''' >> '''Default Set'''
|| In this section, 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'''
|| Click on the drop down against '''Calculation Mode.'''

Select '''Isothermic.'''
|-
|| '''Reactor Volume''' >> 1''' m3'''

Press '''Enter'''
|| Click on the field against '''Reactor Volume''' and enter 1''' m3.'''

Then press '''Enter.'''
|-
|| '''Reactor Length''' >> '''1 m'''

Press '''Enter'''
|| Click on the field against '''Reactor length''' and enter it as '''1 m.'''

Then press '''Enter.'''
|-
|| '''Catalyst Loading''' >> '''0.386 kg/m3'''

Press '''Enter'''
|| Click on the field against '''Catalyst Loading''' and enter it as '''0.386 kg/m3.'''

Then press '''Enter.'''
|-
|| '''Catalyst Particle Diameter''' >> 2''' mm'''

Press '''Enter'''
|| Click on the field against '''Catalyst Particle Diameter''' and enter it as 2''' mm.'''

Then press '''Enter.'''
|-
|| '''Catalyst Void Fraction''' >> '''0.4'''

Press '''Enter'''
|| Click on the field against '''Catalyst Void Fraction''' and enter it as '''0.4.'''

Then press '''Enter.'''
|-
||
|| Wait for a few seconds.

The flowsheet is getting simulated.
|-
||
|| Once again, we will run the simulation.
|-
|| Click '''Solve Flowsheet'''
|| To do this, click on '''Solve Flowsheet''' button.
|-
|| Click '''Plug-Flow Reactor'''
|| When calculations are completed, click on '''PFR''' in the Flowsheet.
|-
|| Hover mouse at '''Results'''
|| Locate '''Results''' section.
|-
|| '''Results >> General'''
|| Under '''General''' tab, Check '''Residence time.'''

It is '''0.00068 h.'''
|-
|| '''Results >> Conversions'''
|| Under '''Conversions''' tab, check conversion for both the reacting compounds.

For '''Methane,''' the conversion is '''80.67%''' and for '''Water,''' it is '''80.67%.'''
|-
|| '''Insert >> Master Property Table'''
|| To check the material balances, go to '''Insert''' option from the toolbar.

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 '''Stream Wise Results – Heterogeneous Catalytic Reaction'''
|| Enter the '''Name''' as '''Stream Wise Results – Heterogeneous Catalytic Reaction.'''
|-
|| 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''', select the properties as

'''Temperature'''

'''Pressure'''

'''Mass Flow'''

'''Molar Flow'''

'''Mass Flow (Mixture) / Methane'''

'''Molar Flow (Mixture) / Methane'''

'''Mass Flow (Mixture) / Water'''

'''Molar Flow (Mixture) / Water'''

'''Mass Flow (Mixture) / Hydrogen'''

'''Molar Flow (Mixture) / Hydrogen'''

'''Mass Flow (Mixture) / Carbon monoxide'''

'''Molar Flow (Mixture) /Carbon monoxide'''

'''Mass Flow (Mixture) / Carbon dioxide'''

'''Molar Flow (Mixture) / Carbon dioxide'''
|-
|| Close this window.
|| Close this window.
|-
|| Point to the results.
|| Move the '''Master Property Table '''for better visibility.

Here we can see the corresponding results for '''Product''' and''' Feed.'''
|-
||
|| Let us summarize.
|-
|| '''Slide Number 13'''

'''Summary'''
|| In this tutorial, we have learnt to

* Define a '''Heterogeneous Catalytic''' reaction
* Define parameters for '''PFR '''required to simulate a '''Heterogeneous Catalytic''' reaction
* Find out '''Conversion''' and '''Residence time''' for '''Heterogeneous Catalytic '''reaction in a '''PFR'''

|-
|| '''Slide Number 14'''

'''Assignment'''

'''Water Gas Shift Reaction:'''

CO + H2O ⇔ H2 + CO2

R2 = [k2/PH2 {PCO PH2O - PH2 PCO2 / K2}] / DEN2

k2 = 1.96 * 10 6 exp (- 67130/RT)

K2 = exp (-3.798 + 4160/T)

||As an assignment,

Add two more Heterogeneous Catalytic Reactions for the existing PFR system.

'''Feed Stream''' conditions and '''Plug-Flow Reactor''' parameters remain unchanged.
|-
|| '''Slide Number 15'''

'''Assignment'''

'''Overall Reaction:'''

CH4 + 2H2O ⇔ 4H2 + CO2

R3 = [k3/PH23.5 {PCH4 PH2O2 - PH24 PCO2 / K3}] / DEN2

k3 = 1.02 * 10 15 exp (- 243900/RT)

K3 = exp (34.218 - 31266/T)

|| Here we give the reaction rates and its coefficients.
|-
|| '''Slide Number 16'''

'''About the Spoken Tutorial Project'''
|| Watch the video available at following link.

'''http://spoken-tutorial.org/ '''

It summarizes the Spoken Tutorial project.
|-
|| '''Slide Number 17'''

'''Spoken Tutorial Workshops'''
|| The Spoken Tutorial Project Team* Conducts workshops using spoken tutorials
* Gives certificates to those who pass an online test
* For more details, please write to contact@spoken-tutorial.org

|-
|| '''Slide Number 18'''

'''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 19'''

'''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 20'''

'''Acknowledgements'''
|| '''Spoken Tutorial''' and '''FOSSEE''' projects are funded by '''NMEICT, MHRD''', Government of India.
|-
|| '''Slide Number 21'''

'''Thanks'''
|| This tutorial is contributed by Kaushik Datta and Priyam Nayak.

Thanks for joining.
|-
|}

DWSIM/C3/Heterogeneous-Catalytic-Reaction/English - Revision history

Nancyvarkey at 06:02, 6 August 2019

Kaushik Datta at 06:52, 2 August 2019

Kaushik Datta at 06:39, 2 August 2019

Kaushik Datta: Created page with "{|border=1 ||'''Visual Cue''' ||'''Narration''' |- || '''Slide Number 1''' ''' Title Slide''' || Welcome to this tutorial on Simulating a '''PFR '''using '''Heterogeneous Cata..."

@@ Line 624: / Line 624: @@
 For '''Methane,''' the conversion is '''80.67%''' and for '''Water,''' it is '''80.67%.'''
 |-
 ||