Difference between revisions of "DWSIM-3.4/C2/Shortcut-Distillation/English-timed"
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| 00:01 | | 00:01 | ||
− | | Welcome to the spoken tutorial on | + | | Welcome to the '''spoken tutorial''' on simulating a '''Shortcut distillation column''' in '''DWSIM.''' |
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| 00:06 | | 00:06 | ||
− | |I am Kannan Moudgalya | + | |I am Kannan Moudgalya. |
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| 00:08 | | 00:08 | ||
− | | In this tutorial, we will simulate a '''Shortcut distillation''' | + | | In this tutorial, we will simulate a '''Shortcut distillation column'''. |
|- | |- | ||
| 00:13 | | 00:13 | ||
− | |We will learn | + | |We will learn: * To calculate: |
− | '''Minimum number of stages ''' | + | * '''Minimum number of stages ''' |
− | '''Minimum reflux ratio ''' | + | * '''Minimum reflux ratio ''' |
− | '''Optimal Feed stage location ''' | + | * '''Optimal Feed stage location ''' |
− | '''Condenser and reboiler duty ''' | + | * '''Condenser and reboiler duty '''. |
|- | |- | ||
| 00:23 | | 00:23 | ||
− | |To achieve a particular product specification | + | |* To achieve a particular product specification. |
|- | |- | ||
|00:26 | |00:26 | ||
− | | To record this tutorial, I am using '''DWSIM''' 3.4 | + | | To record this tutorial, I am using '''DWSIM''' 3.4. |
|- | |- | ||
| 00:30 | | 00:30 | ||
− | | To practice this tutorial you should know | + | | To practice this tutorial, you should know: |
|- | |- | ||
|00:32 | |00:32 | ||
− | |How to add components to a flowsheet | + | |* How to add components to a flowsheet |
|- | |- | ||
| 00:35 | | 00:35 | ||
− | |How to select '''thermodynamic''' packages | + | |* How to select '''thermodynamic''' packages |
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| 00:37 | | 00:37 | ||
− | |How to add material streams and specify their properties | + | |* How to add material streams and specify their properties. |
|- | |- | ||
| 00:41 | | 00:41 | ||
− | |The prerequisite tutorials are mentioned on our website | + | |The prerequisite tutorials are mentioned on our website: '''spoken-tutorial.org'''. |
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| 00:55 | | 00:55 | ||
− | |This problem statement is given by Prof | + | |This problem statement is given by Prof. Bill Luyben of Lehigh University. |
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| 01:10 | | 01:10 | ||
− | |This allows us to | + | |This allows us to customize units which we will do next. |
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| 01:18 | | 01:18 | ||
− | | Add '''Benzene''' from the '''ChemSep''' Database | + | | Add '''Benzene''' from the '''ChemSep''' Database. |
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|01:27 | |01:27 | ||
− | | Next '''Toluene''' | + | | Next '''Toluene'''. |
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| 02:15 | | 02:15 | ||
− | | Let us insert a feed stream that has to be distilled. | + | | Let us insert a '''feed stream''' that has to be distilled. |
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| 02:57 | | 02:57 | ||
− | | Click on this field. Enter '''100.''' | + | | Click on this '''field'''. Enter '''100.''' |
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| 03:16 | | 03:16 | ||
− | | Let us insert a '''Shortcut column''' to the flowsheet. | + | | Let us insert a '''Shortcut column''' to the '''flowsheet'''. |
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| 03:34 | | 03:34 | ||
− | | Now let us insert two '''output streams.''' | + | | Now, let us insert two '''output streams.''' |
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| 03:37 | | 03:37 | ||
− | | One will be '''distillate''' the other is '''Bottoms.''' | + | | One will be '''distillate''', the other is '''Bottoms.''' |
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| 03:41 | | 03:41 | ||
− | | To do that let us drag two '''material streams.''' | + | | To do that, let us drag two '''material streams.''' |
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| 04:05 | | 04:05 | ||
− | | Let us now insert two '''Energy streams | + | | Let us now insert two '''Energy streams''' for '''Condenser duty '''and '''Reboiler duty.''' |
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| 04:48 | | 04:48 | ||
− | | Now click on the next option which says '''Distillate.''' | + | | Now, click on the next option which says '''Distillate.''' |
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| 04:51 | | 04:51 | ||
− | |Click on the drop down arrow and select '''Distillate.''' | + | |Click on the drop-down arrow and select '''Distillate.''' |
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| 04:56 | | 04:56 | ||
− | | Similarly for '''bottoms''' choose '''Bottoms''' | + | | Similarly, for '''bottoms''', choose '''Bottoms'''. |
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| 05:07 | | 05:07 | ||
− | | Similarly choose '''R-Duty '''for '''Reboiler.''' | + | | Similarly, choose '''R-Duty '''for '''Reboiler.''' |
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| 05:19 | | 05:19 | ||
− | |This section is used to specify various attributes of a Shortcut Column. | + | |This section is used to specify various attributes of a '''Shortcut Column'''. |
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| 05:52 | | 05:52 | ||
− | |Let us first specify light key details in '''bottoms.''' | + | |Let us first specify '''light key''' details in '''bottoms.''' |
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| 06:32 | | 06:32 | ||
− | | Similarly let us change reboiler pressure to '''1 atmosphere''' | + | | Similarly, let us change '''reboiler pressure''' to '''1 atmosphere''' |
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| 06:37 | | 06:37 | ||
− | | Now we will run the simulation. | + | | Now we will '''run''' the simulation. |
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| 06:42 | | 06:42 | ||
− | |Click on the '''Play''' button. Now click on the '''Recalculate''' button. | + | |Click on the '''Play''' button. Now, click on the '''Recalculate''' button. |
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| 06:58 | | 06:58 | ||
− | |This shows all the required results like | + | |This shows all the required results like: |
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| 07:10 | | 07:10 | ||
− | | I have tabulated these results in a slide. | + | | I have tabulated these results in a '''slide'''. |
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| 07:15 | | 07:15 | ||
− | | Let me save this simulation. | + | | Let me '''save''' this simulation. |
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| 07:24 | | 07:24 | ||
− | | Let me | + | | Let me summarize. |
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| 07:26 | | 07:26 | ||
− | | We learnt how to specify a shortcut distillation column. | + | | We learnt: * how to specify a shortcut distillation column. |
|- | |- | ||
| 07:29 | | 07:29 | ||
− | |To specify key components, purities, and minimum reflux ratio. | + | |* To specify key components, purities, and minimum reflux ratio. |
|- | |- | ||
| 07:34 | | 07:34 | ||
− | |To use custom units. | + | |* To use custom units. |
|- | |- | ||
| 07:36 | | 07:36 | ||
− | |To calculate minimum reflux ratio optimal feed location and total number of trays | + | |* To calculate minimum reflux ratio optimal feed location and total number of trays. |
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| 07:44 | | 07:44 | ||
− | | The assignment in this slide has to do with mass balances. | + | | The assignment in this '''slide''' has to do with mass balances. |
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| 07:52 | | 07:52 | ||
− | | Let us go to the next | + | | Let us go to the next assignment. |
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| 08:13 | | 08:13 | ||
− | | We have come to the end of this tutorial | + | | We have come to the end of this tutorial. |
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|08:16 | |08:16 | ||
− | | This video | + | | This video summarizes the '''Spoken Tutorial''' project. |
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| 08:24 | | 08:24 | ||
− | | We conduct workshops using '''Spoken Tutorials | + | | We conduct workshops using '''Spoken Tutorials'''; give certificates. Please contact us. |
|- | |- | ||
| 08:31 | | 08:31 | ||
− | | Do you have questions in | + | | Do you have questions in this '''Spoken Tutorial?''' |
|- | |- | ||
| 08:33 | | 08:33 | ||
− | |Choose the minute and second where you have the question. | + | |Choose the '''minute''' and '''second''' where you have the question. |
|- | |- |
Revision as of 10:51, 11 May 2016
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00:01 | Welcome to the spoken tutorial on simulating a Shortcut distillation column in DWSIM. |
00:06 | I am Kannan Moudgalya. |
00:08 | In this tutorial, we will simulate a Shortcut distillation column. |
00:13 | We will learn: * To calculate:
|
00:23 | * To achieve a particular product specification. |
00:26 | To record this tutorial, I am using DWSIM 3.4. |
00:30 | To practice this tutorial, you should know: |
00:32 | * How to add components to a flowsheet |
00:35 | * How to select thermodynamic packages |
00:37 | * How to add material streams and specify their properties. |
00:41 | The prerequisite tutorials are mentioned on our website: spoken-tutorial.org. |
00:47 | In the next two slides, we give specifications for the distillation problem. |
00:55 | This problem statement is given by Prof. Bill Luyben of Lehigh University. |
01:00 | I have already opened DWSIM. |
01:03 | Click on System of Units menu. |
01:07 | Select Custom 1. |
01:10 | This allows us to customize units which we will do next. |
01:14 | Let us click on Configure Simulation button. |
01:18 | Add Benzene from the ChemSep Database. |
01:27 | Next Toluene. |
01:33 | We will next click Thermodynamics and then Property Packages. |
01:40 | Scroll down and select Raoult’s Law. |
01:44 | Below the Thermodynamics option, you see Options menu. Click this. |
01:49 | Click Units System. |
01:53 | Let me bring this inside. |
01:56 | Pressure menu appears at the top of this list. |
01:58 | Click and choose atm for atmosphere. |
02:04 | Below the Pressure menu is the Molar flow rate menu. |
02:08 | Click it and select kmol/per hour. |
02:13 | Click on Back to simulation. |
02:15 | Let us insert a feed stream that has to be distilled. |
02:21 | Enter 0.4 for benzene and 0.6 for toluene. |
02:29 | Apply and Close. |
02:32 | We will change the name of this stream to Feed. |
02:39 | Click on Properties. Scroll to the top. |
02:43 | Click on Specification. |
02:46 | Choose Pressure and Vapor Fraction. |
02:50 | Locate the Molar flow rate option. |
02:53 | It has the units of kmol/per hour. |
02:57 | Click on this field. Enter 100. |
03:02 | Locate Molar Fraction (Vapor Phase). |
03:08 | The default value is 0. |
03:10 | This indicates saturated liquid. |
03:13 | Let us leave it as it is. |
03:16 | Let us insert a Shortcut column to the flowsheet. |
03:20 | Locate it from the Object palette. |
03:23 | The Shortcut Column is based on Fenske-Underwood-Gilliland method. |
03:27 | Click on it and drag it to the flowsheet. |
03:32 | Let us arrange it. |
03:34 | Now, let us insert two output streams. |
03:37 | One will be distillate, the other is Bottoms. |
03:41 | To do that, let us drag two material streams. |
03:46 | As they are output streams, we will leave them unspecified. |
03:56 | We will change the name of these streams to Distillate and Bottoms. |
04:05 | Let us now insert two Energy streams for Condenser duty and Reboiler duty. |
04:17 | Name these streams as C-Duty and R-Duty. |
04:24 | We are now ready to specify the Shortcut distillation column. |
04:27 | Click on it and select it. |
04:30 | Go to the Selected Object window. |
04:32 | Under theProperties tab, locate Connections menu. |
04:37 | The first option is Feed. |
04:38 | Let me click on Feed menu. A down arrow appears, indicating a menu. |
04:44 | Click this arrow. Here we choose Feed. |
04:48 | Now, click on the next option which says Distillate. |
04:51 | Click on the drop-down arrow and select Distillate. |
04:56 | Similarly, for bottoms, choose Bottoms. |
04:59 | The next option is Condenser Duty. |
05:02 | Let me click on it and select C-Duty. |
05:07 | Similarly, choose R-Duty for Reboiler. |
05:12 | This completes the connectivity of the flowsheet. |
05:14 | Under Properties tab, locate Parameters section. |
05:19 | This section is used to specify various attributes of a Shortcut Column. |
05:25 | In this section, the first option is Condenser. |
05:30 | By default, it is total condenser. |
05:33 | If a partial condenser is required, you can change it here. |
05:36 | Here we leave it as it is. |
05:39 | Let us enter the reflux ratio. Click on it. |
05:42 | Here we enter the value 2 in the field next to it. |
05:49 | We will specify the Product composition. |
05:52 | Let us first specify light key details in bottoms. |
05:57 | To do this, let me click light key. |
06:01 | Click the arrow and choose Benzene. |
06:04 | In the given field on the next row, enter 0.05. |
06:10 | Similarly for heavy key, choose Toluene. |
06:15 | Now we specify the heavy key in Distillate. |
06:18 | We enter 0.05. |
06:23 | Next in the list is Condenser Pressure. |
06:26 | The default value is 0 atmosphere. We will change it to 1 atmosphere. |
06:32 | Similarly, let us change reboiler pressure to 1 atmosphere |
06:37 | Now we will run the simulation. |
06:39 | To do this, go to the calculator options. |
06:42 | Click on the Play button. Now, click on the Recalculate button. |
06:47 | When the calculations are completed, click on the Shortcut column. |
06:53 | Under Properties tab, locate Results menu. |
06:58 | This shows all the required results like: |
07:00 | Minimum Reflux Ratio |
07:03 | Minimum Number of Stages |
07:05 | Actual Number of Stages |
07:07 | Optimal Feed Stage, etc. |
07:10 | I have tabulated these results in a slide. |
07:15 | Let me save this simulation. |
07:20 | I have saved this as shortcut end. |
07:24 | Let me summarize. |
07:26 | We learnt: * how to specify a shortcut distillation column. |
07:29 | * To specify key components, purities, and minimum reflux ratio. |
07:34 | * To use custom units. |
07:36 | * To calculate minimum reflux ratio optimal feed location and total number of trays. |
07:43 | Let me give some assignments. |
07:44 | The assignment in this slide has to do with mass balances. |
07:48 | I use blue colour to indicate streams and equipment. |
07:52 | Let us go to the next assignment. |
07:54 | Carry out energy balance as mentioned. |
07:58 | Repeat the simulation with different product purities. |
08:02 | Determine how the energy requirement changes. |
08:06 | Repeat this simulation with different thermodynamics. |
08:08 | Repeat this simulation with different feed conditions. |
08:12 | Try to reason your results. |
08:13 | We have come to the end of this tutorial. |
08:16 | This video summarizes the Spoken Tutorial project. |
08:20 | If you do not have good bandwidth, you may download and watch it. |
08:24 | We conduct workshops using Spoken Tutorials; give certificates. Please contact us. |
08:31 | Do you have questions in this Spoken Tutorial? |
08:33 | Choose the minute and second where you have the question. |
08:37 | Explain your question briefly. |
08:38 | Someone from the FOSSEE team will answer them. |
08:41 | Please visit this site. |
08:44 | The FOSSEE team coordinates coding of solved examples of popular books. |
08:48 | We give honorarium and certificates to those who do this. |
08:52 | For more details, please visit this site. |
08:56 | The FOSSEE team helps migrate commercial simulator labs to DWSIM. |
09:00 | We give honorarium and certificates to those who do this. |
09:04 | For more details, please visit this site. |
09:07 | Spoken Tutorial and FOSSEE projects are funded by NMEICT, MHRD, Government of India. |
09:14 | Thanks for joining. Good bye. |