https://script.spoken-tutorial.org/index.php?title=New_server_test_foss1/C2/new_server_tut_1/English&feed=atom&action=historyNew server test foss1/C2/new server tut 1/English - Revision history2024-03-29T13:03:18ZRevision history for this page on the wikiMediaWiki 1.23.17https://script.spoken-tutorial.org/index.php?title=New_server_test_foss1/C2/new_server_tut_1/English&diff=46933&oldid=prevKaushik Datta: Created page with "{|border=1 ||'''Visual Cue''' ||'''Narration''' |- || '''Slide Number 1 '''Title Slide''' || Welcome to this spoken tutorial on '''Binary Phase Envelope '''in '''DWSIM'''...."2019-04-10T11:30:20Z<p>Created page with "{|border=1 ||'''Visual Cue''' ||'''Narration''' |- || '''Slide Number 1 '''Title Slide''' || Welcome to this spoken tutorial on '''Binary Phase Envelope '''in '''DWSIM'''...."</p>
<p><b>New page</b></p><div>{|border=1<br />
||'''Visual Cue'''<br />
||'''Narration'''<br />
|- <br />
|| '''Slide Number 1<br />
'''Title Slide''' <br />
|| Welcome to this spoken tutorial on '''Binary Phase Envelope '''in '''DWSIM'''. <br />
<br />
|- <br />
|| '''Slide Number 2'''<br />
<br />
'''Learning Objective''' <br />
|| In this tutorial, we will learn to generate: <br />
<br />
* '''Txy''' plot at given '''pressure''' <br />
<br />
* '''xy''' plot for the obtained '''Txy''' data <br />
<br />
* '''Pxy''' plot at given '''temperature''' <br />
|- <br />
|| '''Slide Number 3'''<br />
<br />
'''System Requirements''' <br />
|| To record this tutorial, I am using <br />
<br />
* '''DWSIM 5.2 (Classic UI)''' and<br />
<br />
* '''Windows 10''' <br />
<br />
The process demonstrated in this tutorial is identical in other OS also, such as- <br />
<br />
* '''Linux''', <br />
<br />
* '''Mac OS X '''or <br />
<br />
* '''FOSSEE OS '''on '''ARM'''. <br />
<br />
|- <br />
|| '''Slide Number 4''' <br />
<br />
'''Pre-requisites''' <br />
|| To practice this tutorial, you should know to, <br />
<br />
<br />
* add components to a '''flowsheet''' <br />
<br />
* select '''thermodynamic '''packages<br />
<br />
* add '''material '''streams and specify their properties. <br />
<br />
|- <br />
|| '''Slide Number 5''' <br />
<br />
<br />
'''Prerequisite Tutorials and Files''' <br />
<br />
'''www.spoken-tutorial.org''' <br />
|| The pre-requisite tutorials are mentioned on our website.<br />
<br />
<br />
You can access these tutorials and all the associated files from this site. <br />
<br />
|- <br />
|| '''Slide Number 6''' <br />
<br />
<br />
'''Feed Conditions''' <br />
<br />
<br />
Mass Flow: 120 kmol/h <br />
<br />
Mole Fraction(Ethanol): 0.5 <br />
<br />
Mole Fraction(1-propanol): 0.5 <br />
<br />
Temperature: 30 degree C <br />
<br />
Pressure: 3.5 bar <br />
<br />
Property Package:''' '''Soave-Redlich-Kwong (SRK) <br />
|| In this tutorial, using '''DWSIM''', we will generate: <br />
<br />
<br />
<br />
1) '''Txy''' plot at a constant pressure of '''1.013 bar''' <br />
<br />
2) '''xy''' plot for the obtained '''Txy''' data <br />
<br />
3) '''Pxy''' plot at a constant temperature of '''75<sup>0</sup>C''' <br />
<br />
<br />
<br />
Here we give '''compounds, inlet stream conditions''' and '''property package'''. <br />
<br />
|- <br />
|| <br />
|| I have already opened '''DWSIM '''on my machine. <br />
<br />
|- <br />
|| File >>'''New Steady-state Simulation ''' <br />
|| Go to '''File '''menu and select '''New Steady-state Simulation.''' <br />
<br />
|- <br />
|| Point to '''Simulation Configuration Wizard '''window <br />
|| '''Simulation Configuration Wizard '''window appears. <br />
<br />
|- <br />
|| Click on '''Next'''. <br />
|| At the bottom, click on the '''Next '''button. <br />
<br />
|- <br />
|| Type '''Ethanol '''in the '''Search '''tab <br />
|| Now, in the '''Compounds Search '''tab, type '''Ethanol.''' <br />
<br />
|- <br />
|| '''ChemSep '''database >>'''Ethanol''' <br />
|| Select '''Ethanol '''from '''ChemSep '''database. <br />
<br />
|- <br />
|| '''Type 1-propanol '''in the '''Search '''tab <br />
|| Similarly, add '''1-propanol'''. <br />
<br />
|- <br />
|| Click on '''Next.''' <br />
|| At the bottom, click on the '''Next '''button. <br />
<br />
|- <br />
|| Point to''' Property Packages''' <br />
|| The '''Property Packages '''opens. <br />
<br />
|- <br />
|| '''Property Packages'''>>'''Available Property Package''' <br />
<br />
<br />
Double click on '''Soave-Redlich-Kwong (SRK)''' <br />
|| From '''Available Property Packages '''list, double-click on '''Soave-Redlich-Kwong (SRK).''' <br />
<br />
|- <br />
|| Click on '''Next.''' <br />
|| Then click on the '''Next '''button'''.''' <br />
<br />
|- <br />
|| Point to '''Flash Algorithm''' <br />
|| We are moved to a new window named '''Flash Algorithm'''. <br />
<br />
|- <br />
|| '''Default Flash Algorithm '''>>'''Nested Loops (VLE)''' <br />
|| From '''Default Flash Algorithm '''select '''Nested Loops(VLE)''' <br />
<br />
|- <br />
|| Click '''Next''' <br />
|| At the bottom, click on the '''Next '''button. <br />
<br />
|- <br />
|| Point to '''System of Units''' <br />
|| Next option is '''System of Units.''' <br />
<br />
|- <br />
|| '''System of Units >>C5''' <br />
|| Under '''System of Units''', select '''C5'''. <br />
<br />
|- <br />
|| Click on '''Finish''' <br />
|| At the bottom, click on '''Finish '''button. <br />
<br />
|- <br />
|| Click on maximize button. <br />
|| Let us maximize the '''simulation window''' for better visibility. <br />
<br />
|- <br />
|| <br />
|| Let’s insert a '''material stream''' for which we have to generate the '''Txy, xy '''and '''Pxy''' plots. <br />
<br />
|- <br />
|| Point to '''Flowsheet Objects.''' <br />
|| On the right hand side of the main '''simulation window''', go to '''Flowsheet Objects.''' <br />
<br />
|- <br />
|| In the '''Filter List '''tab(right panel), type '''Material Stream''' <br />
|| In the '''Filter List '''tab, type '''Material Stream.''' <br />
<br />
|- <br />
|| Click and drag '''Material Stream '''to the flowsheet <br />
|| From the displayed list, drag and drop a '''Material Stream '''to the '''Flowsheet'''. <br />
<br />
|- <br />
|| Click on '''MSTR-000''' <br />
|| Click on the '''Material Stream “MSTR-000” '''to view its properties. <br />
<br />
|- <br />
|| Type '''Feed''' <br />
|| Let’s change the name of this '''stream '''to '''Feed.''' <br />
<br />
|- <br />
|| Point to '''Feed stream '''properties. <br />
|| Now we will specify the '''Feed stream '''properties. <br />
<br />
|- <br />
|| Go to '''Input Data.''' <br />
<br />
'''Input Data>>Flash Spec>>Temperature and Pressure(TP)''' <br />
|| Go to '''Input Data.''' <br />
<br />
<br />
Select '''Flash Spec '''as '''Temperature and Pressure (TP), '''if not already selected. <br />
<br />
<br />
By default, '''Temperature and Pressure '''are already selected as '''Flash Spec.''' <br />
<br />
|- <br />
|| '''Input Data >>Temperature >>30 C''' <br />
<br />
Press '''Enter''' <br />
|| Change '''Temperature '''to '''30 deg C '''and press '''Enter.''' <br />
<br />
|- <br />
|| '''Input Data >>Pressure >>3.5 bar''' <br />
<br />
Press '''Enter''' <br />
|| Change '''Pressure '''to '''3.5 bar '''and press '''Enter'''. <br />
<br />
|- <br />
|| '''Input Data >>Molar Flow >>120 kmol/h''' <br />
<br />
Press '''Enter''' <br />
|| Change '''Molar Flow '''to '''120 kmol/h '''and press '''Enter'''. <br />
<br />
|- <br />
|| Cursor on the window. <br />
|| Now let us specify the '''feed stream compositions'''. <br />
<br />
|- <br />
|| '''Composition >>Basis >>Mole Fractions''' <br />
|| Under '''Composition''', choose the '''Basis '''as '''Mole Fractions, '''if not already selected'''.''' <br />
<br />
<br />
By default, '''Mole Fractions '''will be selected as '''Basis.''' <br />
<br />
|- <br />
|| '''Ethanol: 0.5''' <br />
<br />
<br />
<br />
|| For '''Ethanol''', enter the '''Amount '''as '''0.5 '''and press '''Enter'''. <br />
<br />
|- <br />
|| '''1-propanol: 0.5''' <br />
|| Similarly, for '''1-propanol''', enter it as '''0.5 '''and press '''Enter'''. <br />
<br />
|- <br />
|| Point to the green tick mark. <br />
<br />
Click '''Accept Changes''' <br />
|| On the right side, click on this green tick to '''Accept Changes.''' <br />
<br />
|- <br />
|| Click on '''Utilities''' <br />
|| Now we will see how '''property package''' calculates '''phase equilibrium''' data of compounds. <br />
<br />
<br />
To do this, go to '''Utilities'''. <br />
<br />
|- <br />
|| Click on''' Add Utility''' <br />
|| Click on '''Add Utility.''' <br />
<br />
|- <br />
|| '''Object Type >> Material Streams''' <br />
|| In the '''Add Utility '''window under '''Object Type''', select '''Material Streams.''' <br />
<br />
|- <br />
|| '''Utility Type >> Binary Phase Envelope''' <br />
|| Under '''Utility Type''', select '''Binary Phase Envelope.''' <br />
<br />
|- <br />
|| '''Flowsheet Object >> Feed''' <br />
|| Under '''Flowsheet Object''', select '''Feed.''' <br />
<br />
|- <br />
|| Click on '''Add Utility''' <br />
|| At the bottom, click on the '''Add Utility''' button.<br />
<br />
|- <br />
|| Point to '''Binary Phase Envelope''' window <br />
|| '''Binary Phase Envelope''' window opens. <br />
<br />
|- <br />
|| Drag the phase envelope window. <br />
|| Let us adjust the '''phase envelope window''''''Bold text''' for better visibility. <br />
<br />
|- <br />
|| '''Name >> Txy-plot''' <br />
|| Enter '''Name''' as '''Txy-plot.''' <br />
<br />
|- <br />
|| Point to '''Diagram Settings.''' <br />
|| Go to '''Diagram Settings.''' <br />
<br />
|- <br />
|| Compound 1 >> Ethanol <br />
|| Select '''Ethanol''' as '''Compound 1''', if not already selected. <br />
<br />
<br />
By default, '''Ethanol''' is selected as '''Compound 1'''. <br />
<br />
|- <br />
|| Compound 2 >> 1-propanol <br />
|| Make sure that the other '''compound''' is selected as '''Compound 2'''. <br />
<br />
<br />
In this case, it is '''1-propanol''' which is '''Compound 2'''. <br />
<br />
|- <br />
|| '''Envelope type >> Txy''' <br />
|| Select '''Envelope type''' as '''Txy''', if not already selected. <br />
<br />
<br />
By default, '''Txy''' is selected as '''Envelope type'''. <br />
<br />
|- <br />
|| '''Txy Diagram Options >> VLE''' <br />
|| Select '''Txy Diagram Options''' as '''VLE''', if not already selected. <br />
<br />
<br />
By default, '''VLE''' is selected as '''Txy Diagram Options'''. <br />
<br />
|- <br />
|| X-Axis Basis >> Mole Fraction <br />
|| Select '''X-Axis Basis''' as '''Mole Fraction''', if not already selected. <br />
<br />
<br />
By default, '''Mole Fraction''' is selected as '''X-Axis Basis''' <br />
<br />
|- <br />
|| Pressure >> 1.013 bar <br />
|| Enter '''Pressure''' as '''1.013 bar.''' <br />
<br />
|- <br />
|| <br />
|| Here we are going to plot a '''Txy''' diagram. <br />
<br />
<br />
So let us not worry about the '''pressure''' value. <br />
<br />
|- <br />
|| Point to '''Soave-Redlich-Kwong (SRK)''' <br />
|| Make sure that the '''property package''' is selected as '''Soave-Redlich-Kwong (SRK)''' <br />
<br />
|- <br />
|| Click on '''Calculate '''button at the bottom. <br />
|| Now click on '''Calculate''' button at the bottom. <br />
<br />
|- <br />
|| Point to '''Txy''' diagram <br />
<br />
<br />
Point to '''X-axis''' <br />
<br />
<br />
Point to '''Y-axis''' <br />
|| The diagram generated is a '''Txy''' diagram or '''Constant Pressure Phase Diagram'''. <br />
<br />
<br />
'''X-axis''' indicates the '''mole fraction''' of '''Ethanol'''.<br />
<br />
'''Y -axis''' indicates the temperature range for which the '''VLE '''is generated. <br />
<br />
|- <br />
|| Point to '''Bubble Point Curve''' <br />
|| The lower line of the '''envelope''' represents '''Bubble Point''' '''Curve.''' <br />
<br />
|- <br />
|| Point to lower line Ethanol mole fraction value <br />
<br />
<br />
Point to '''bubble point temperature''' value <br />
|| Hover the mouse to the lower line at '''Ethanol mole fraction''''''Bold text''' of '''0.5.''' <br />
<br />
<br />
We can see the '''bubble point temperature '''to be '''86.2853 deg C.''' <br />
<br />
|- <br />
|| Point to the subcooled region. <br />
|| For any mixture composition below this line, is '''subcooled liquid'''. <br />
<br />
|- <br />
|| Point to '''Dew Point''' '''Curve''' <br />
|| The upper line of the '''envelope''' represents '''Dew Point Curve.''' <br />
<br />
|- <br />
|| Point to upper line '''Ethanol mole fraction''' value <br />
<br />
<br />
Point to dew point temperature value <br />
|| Hover the mouse to the upper line at '''Ethanol mole fraction''' of '''0.5.''' <br />
<br />
<br />
We can see the '''dew point temperature '''to be '''89.5881 deg C''' <br />
<br />
|- <br />
|| Point to the '''superheated vapour '''region. <br />
|| For any mixture composition above this line, the mixture is '''superheated vapour'''. <br />
<br />
|- <br />
|| Point to '''VLE region''' <br />
<br />
<br />
<br />
|| The area enclosed between these two lines is the '''VLE region.''' <br />
<br />
<br />
Here both vapor and liquid phases exist in '''equilibrium'''. <br />
<br />
|- <br />
|| Point to '''Results''' section >> click on''' Table''' <br />
<br />
<br />
point to the values. <br />
|| We can see the '''bubble points''' and '''dew points''' at every composition. <br />
<br />
<br />
For this, go to '''Results''' section and click on '''Table'''. <br />
<br />
<br />
Here we can see the corresponding '''mole fractions''' and '''temperatures '''values. <br />
<br />
|- <br />
|| <br />
|| Let us now generate the '''xy''' plot for data obtained in the above '''Txy''' diagram. <br />
<br />
|- <br />
|| Close this window<br />
|| Close this window. <br />
<br />
|- <br />
|| '''Utilities >> Add Utility''' <br />
|| Go to '''Utilities''' and click on '''Add Utility.''' <br />
<br />
|- <br />
|| '''Object Type >> Material Streams''' <br />
|| In the '''Add Utility '''window, under '''Object Type''', select '''Material Streams.''' <br />
<br />
|- <br />
|| '''Utility Type >> Binary Phase Envelope''' <br />
|| Under '''Utility Type''', select '''Binary Phase Envelope.''' <br />
<br />
|- <br />
|| '''Flowsheet Object >> Feed''' <br />
|| Under '''Flowsheet Object''', select '''Feed.''' <br />
<br />
|- <br />
|| At the bottom, click on the '''Add Utility''' button.<br />
|| At the bottom, click on the '''Add Utility''' button.<br />
<br />
|- <br />
|| Point to '''Binary Phase Envelope '''window <br />
|| Once again, '''Binary Phase Envelope''' window opens. <br />
<br />
|- <br />
|| <br />
|| Let us adjust the window for better visibility. <br />
<br />
|- <br />
|| '''Name >> xy-plot''' <br />
|| Enter '''Name''' as '''xy-plot.''' <br />
<br />
|- <br />
|| Go to '''Diagram Settings.''' <br />
|| Go to '''Diagram Settings.''' <br />
<br />
|- <br />
|| <br />
|| Let the '''Compound''' settings be the default settings. <br />
<br />
|- <br />
|| '''Envelope type >> (T)xy''' <br />
|| Select '''Envelope type''' as '''(T)xy.''' <br />
<br />
|- <br />
|| X-Axis Basis >> Mole Fraction <br />
|| Select '''X-Axis Basis''' as '''Mole Fraction''', if not already selected. <br />
<br />
<br />
By default, '''Mole Fraction''' is selected as '''X-Axis Basis.''' <br />
<br />
|- <br />
|| '''Pressure >> 1.013 bar''' <br />
|| Enter '''Pressure''' as '''1.013 bar.''' <br />
<br />
|- <br />
|| Click on '''Calculate '''button at the bottom. <br />
|| Now click on '''Calculate '''button at the bottom. <br />
<br />
|- <br />
|| Point to '''xy''' diagram <br />
<br />
<br />
Point to '''X-axis''' <br />
<br />
<br />
Point to '''Y-axis''' <br />
|| The diagram is generated is called '''xy diagram.''' <br />
<br />
<br />
'''X-axis''' indicates the '''mole fraction '''of '''Ethanol''' in liquid phase. <br />
<br />
<br />
'''Y -axis''' indicates the '''mole fraction''' of '''Ethanol''' in vapour phase. <br />
<br />
|- <br />
|| Point to '''Equilibrium Curve''' <br />
|| The upper curve is called '''Equilibrium Curve.''' <br />
<br />
|- <br />
|| Point to upper line Ethanol mole fraction value <br />
<br />
<br />
Point to vapour phase mole fraction of Ethanol value <br />
|| Hover the mouse to the upper line at '''Ethanol mole fraction '''of '''0.6.''' <br />
<br />
<br />
We can see the vapour phase '''mole fraction''' of '''Ethanol''' to be '''0.7539.''' <br />
<br />
|- <br />
|| <br />
|| Let us generate the '''Pxy''' plot now. <br />
<br />
|- <br />
|| Close this window.<br />
|| Close this window.<br />
|- <br />
|| '''Utilities >> Add Utility''' <br />
|| Go to '''Utilities''' and click on '''Add Utility.''' <br />
<br />
|- <br />
|| '''Object Type >> Material Streams''' <br />
|| In the '''Add Utility '''window, under '''Object Type''', select '''Material Streams.''' <br />
<br />
|- <br />
|| '''Utility Type >> Binary Phase Envelope''' <br />
|| Under '''Utility Type''', select '''Binary Phase Envelope.''' <br />
<br />
|- <br />
|| '''Flowsheet Object >> Feed''' <br />
|| Under '''Flowsheet Object''', select '''Feed.''' <br />
<br />
|- <br />
|| At the bottom, click on the '''Add Utility''' button.<br />
|| At the bottom, click on the '''Add Utility''' button.<br />
<br />
|- <br />
|| Point to the window. <br />
|| Once again, '''Binary Phase Envelope''' window opens. <br />
<br />
|- <br />
|| Drag the window to adjust. <br />
|| Let us adjust the window for better visibility. <br />
<br />
|- <br />
|| '''Name >> Pxy-plot''' <br />
|| Enter '''Name''' as '''Pxy-plot.''' <br />
<br />
|- <br />
|| Go to '''Diagram Settings''' <br />
|| Go to '''Diagram Settings.''' <br />
<br />
|- <br />
|| <br />
|| Let the '''Compound''' settings be the default settings. <br />
<br />
|- <br />
|| '''Envelope type >> Pxy''' <br />
|| Select '''Envelope type''' as '''Pxy.''' <br />
<br />
|- <br />
|| X-Axis Basis >> Mole Fraction <br />
|| Select '''X-Axis Basis''' as '''Mole Fraction''', if not already selected. <br />
<br />
<br />
By default, '''Mole Fraction''' is selected as '''X-Axis Basis.''' <br />
<br />
|- <br />
|| '''Temperature >> 75 degree C''' <br />
|| Enter '''Temperature''' as '''75 degC.''' <br />
<br />
|- <br />
|| <br />
|| Here we are going to plot a '''Pxy '''diagram. <br />
<br />
<br />
So let us not worry about the '''temperature''' value. <br />
<br />
|- <br />
|| '''Property Package >> Soave-Redlich-Kwong (SRK) ''' <br />
|| Make sure that the property package is selected as '''Soave-Redlich-Kwong (SRK)''' <br />
<br />
|- <br />
|| Click on Calculate button at the bottom. <br />
|| Now click on '''Calculate '''button at the bottom. <br />
<br />
|- <br />
|| Point to '''Pxy''' diagram <br />
<br />
<br />
Point to '''X-axis''' <br />
<br />
<br />
Point to '''Y-axis''' <br />
|| The diagram generated is a '''Pxy''' diagram or '''Constant Temperature Phase Diagram'''. <br />
<br />
<br />
'''X-axis''' indicates the '''mole fraction''' of '''Ethanol'''. <br />
<br />
<br />
'''Y -axis''' indicates the Pressure range for which the '''VLE''' is generated. <br />
<br />
|- <br />
|| Point to '''Dew Points''' <br />
|| The lower line of the envelope represents '''Dew Points'''. <br />
<br />
|- <br />
|| Point to lower line '''Ethanol mole fraction''' value <br />
<br />
<br />
Point to dew point temperature value <br />
|| Hover the mouse to the lower line at '''Ethanol mole fraction '''of '''0.4.''' <br />
<br />
<br />
We can see the '''dew point pressure''' to be '''0.523 bar.''' <br />
<br />
|- <br />
|| Point to the line. <br />
|| For any mixture composition below this line, is completely '''vapour.''' <br />
<br />
|- <br />
|| Point to '''Bubble Points''' <br />
|| The upper line of the envelope represents '''Bubble Points'''. <br />
<br />
|- <br />
|| Point to upper line Ethanol mole fraction value <br />
<br />
<br />
Point to bubble point temperature value <br />
|| Hover the mouse to the upper line at '''Ethanol mole fraction '''of 0.8. <br />
<br />
<br />
We can see the '''bubble point pressure''' to be '''0.782 bar.''' <br />
<br />
|- <br />
|| Point to the line. <br />
|| For any mixture composition above this line, is completely '''liquid.''' <br />
<br />
|- <br />
|| Point to '''VLE region''' <br />
|| The area enclosed between these two lines is the '''VLE region'''. <br />
<br />
<br />
Here both vapor and liquid phases exist in '''equilibrium'''. <br />
<br />
|- <br />
|| Point to '''Results''' section <br />
<br />
Click on''' Table''' <br />
<br />
<br />
|| Now, go to '''Results''' section. <br />
<br />
Click on '''Table'''. <br />
<br />
Here we can see the corresponding '''mole fractions''' and '''pressure''' values.<br />
<br />
|- <br />
|| <br />
|| Let's summarize. <br />
<br />
|- <br />
|| '''Slide Number 7''' <br />
<br />
<br />
'''Summary''' <br />
|| In this tutorial, we have learnt to generate: <br />
<br />
<br />
* '''Txy''' plot at given '''pressure''' <br />
* '''xy''' plot for the '''Txy''' data obtained above <br />
* '''Pxy''' plot at given '''temperature''' <br />
|- <br />
|| '''Slide Number 8''' <br />
<br />
<br />
'''Assignment ''' <br />
|| Generate '''P(xy)''' plot for the '''Pxy''' data obtained. <br />
<br />
Generate the '''P(xy)''' plot using '''NRTL '''model. <br />
<br />
Compare the results. <br />
|- <br />
|| '''Slide Number 9''' <br />
<br />
'''About the Spoken Tutorial Project''' <br />
|| Watch the video available at following link. <br />
<br />
'''http://spoken-tutorial.org/ ''' <br />
<br />
It summarizes the Spoken Tutorial project. <br />
<br />
|- <br />
|| '''Slide Number 10''' <br />
<br />
'''Spoken Tutorial Workshops''' <br />
|| The Spoken Tutorial Project Team <br />
<br />
* Conducts workshops and gives certificates <br />
* For more details, please write to us.<br />
<br />
|- <br />
|| '''Slide Number 11''' <br />
<br />
<br />
'''Forum Slide''' <br />
<br />
<br />
* Do you have questions in this '''Spoken Tutorial?''' <br />
<br />
* Please visit this site <br />
<br />
* Choose the minute and second where you have the question. <br />
<br />
* Explain your question briefly. <br />
<br />
* Someone from the FOSSEE team will answer them. <br />
|| Please post your times queries in this forum. <br />
<br />
|- <br />
|| '''Slide Number 12<br />
'''DWSIM Flowsheeting Project''' <br />
<br />
<br />
|| The '''FOSSEE '''team coordinates conversion of existing flow sheets into '''DWSIM'''. <br />
<br />
We give honorarium and certificates. <br />
<br />
For more details, please visit this site. <br />
<br />
|- <br />
|| '''Slide Number 13<br />
'''TextBook Companion Project''' <br />
|| The '''FOSSEE '''team coordinates coding of solved examples of popular books. <br />
<br />
We give honorarium and certificates. <br />
<br />
For more details, please visit this site. <br />
<br />
|- <br />
|| '''Slide Number 14'''<br />
<br />
'''Lab Migration Project''' <br />
|| The '''FOSSEE '''team helps migrate commercial simulator labs to '''DWSIM.''' <br />
<br />
We give honorarium and certificates. <br />
<br />
For more details, please visit this site <br />
<br />
|- <br />
|| '''Slide Number 15'''<br />
<br />
'''Acknowledgements''' <br />
|| '''Spoken Tutorial '''and '''FOSSEE '''projects are funded by '''NMEICT, MHRD''', Government of India. <br />
<br />
|- <br />
|| '''Slide Number 16'''<br />
<br />
'''Thanks''' <br />
|| This tutorial is contributed by Kaushik Datta and Priyam Nayak. <br />
<br />
<br />
Thanks for joining. <br />
|-<br />
|}</div>Kaushik Datta