Difference between revisions of "DWSIM/C2/Heat-Exchanger/English-timed"
From Script | Spoken-Tutorial
PoojaMoolya (Talk | contribs) (Created page with " {| border=1 ||'''Time''' ||'''Narration''' |- ||00:01 || Welcome to this tutorial on Simulating a '''Heat Exchanger '''in '''DWSIM'''. |- ||00:07 || In this tutorial, we wi...") |
Sandhya.np14 (Talk | contribs) |
||
(One intermediate revision by the same user not shown) | |||
Line 6: | Line 6: | ||
|- | |- | ||
||00:01 | ||00:01 | ||
− | || Welcome to this tutorial on | + | || Welcome to this tutorial on simulating a '''Heat Exchanger '''in '''DWSIM'''. |
|- | |- | ||
||00:07 | ||00:07 | ||
− | || In this tutorial, we will learn to: | + | || In this tutorial, we will learn to: simulate a''' Heat Exchanger''', |
|- | |- | ||
||00:13 | ||00:13 | ||
− | || | + | || calculate the '''Outlet stream temperatures''', |
|- | |- | ||
||00:16 | ||00:16 | ||
− | || | + | || calculate '''Thermal Efficiency '''and''' LMTD'''. |
|- | |- | ||
|| 00:20 | || 00:20 | ||
− | || To record this tutorial, I am using '''DWSIM 4.3 '''and '''Windows 7''' | + | || To record this tutorial, I am using '''DWSIM 4.3 '''and '''Windows 7'''. |
|- | |- | ||
Line 28: | Line 28: | ||
|| The process demonstrated in this tutorial is identical in other OS also, such as- | || The process demonstrated in this tutorial is identical in other OS also, such as- | ||
− | '''Linux''', | + | '''Linux''', '''Mac OS X '''or '''FOSSEE OS '''on '''ARM'''. |
|- | |- | ||
||00:40 | ||00:40 | ||
− | || To practice this tutorial, you should know how to add components to a '''flowsheet''' | + | || To practice this tutorial, you should know how to add components to a '''flowsheet''', |
|- | |- | ||
|| 00:47 | || 00:47 | ||
− | || | + | || select '''thermodynamic package'''s, |
|- | |- | ||
|| 00:50 | || 00:50 | ||
− | || | + | || add '''material stream''' and specify their properties. |
|- | |- | ||
|| 00:54 | || 00:54 | ||
− | || The prerequisite tutorials are mentioned on our website | + | || The prerequisite tutorials are mentioned on our website. |
|- | |- | ||
Line 56: | Line 56: | ||
|- | |- | ||
|| 01:09 | || 01:09 | ||
− | || Here we give '''Compounds '''and''' Inlet stream conditions.''' | + | || Here, we give '''Compounds '''and''' Inlet stream conditions.''' |
|- | |- | ||
|| 01:13 | || 01:13 | ||
− | || Here we give '''Heat Exchanger''' properties and '''Property package'''. | + | || Here, we give '''Heat Exchanger''' properties and '''Property package'''. |
|- | |- | ||
Line 104: | Line 104: | ||
|- | |- | ||
|| 02:01 | || 02:01 | ||
− | || Then click on '''Next '''button | + | || Then click on '''Next '''button. |
|- | |- | ||
Line 112: | Line 112: | ||
|- | |- | ||
||02:08 | ||02:08 | ||
− | || From '''Default Flash Algorithm '''select '''Nested Loops(VLE)''' | + | || From '''Default Flash Algorithm, '''select '''Nested Loops(VLE).''' |
|- | |- | ||
|| 02:14 | || 02:14 | ||
− | || Click on '''Next '''button | + | || Click on '''Next '''button. |
|- | |- | ||
Line 128: | Line 128: | ||
|- | |- | ||
|| 02:26 | || 02:26 | ||
− | || At the bottom, click on '''Finish '''button | + | || At the bottom, click on '''Finish '''button. |
|- | |- | ||
|| 02:30 | || 02:30 | ||
− | || Let us maximize the simulation window for better visibility. | + | || Let us maximize the '''simulation window''' for better visibility. |
|- | |- | ||
|| 02:35 | || 02:35 | ||
− | || Now let’s insert two material stream that enter the '''Heat Exchanger'''. | + | || Now, let’s insert two '''material stream''' that enter the '''Heat Exchanger'''. |
|- | |- | ||
Line 152: | Line 152: | ||
|- | |- | ||
|| 02:58 | || 02:58 | ||
− | || Click on the '''Material Stream '''“'''MSTR-000” '''to view its properties. | + | || Click on the '''Material Stream''' “'''MSTR-000” '''to view its properties. |
|- | |- | ||
Line 188: | Line 188: | ||
|- | |- | ||
|| 03:44 | || 03:44 | ||
− | || Now let us specify the '''feed stream compositions'''. | + | || Now, let us specify the '''feed stream compositions'''. |
|- | |- | ||
|| 03:49 | || 03:49 | ||
− | || Under '''Composition''', choose the '''Basis '''as '''Mole Fractions, '''if not already selected | + | || Under '''Composition''', choose the '''Basis '''as '''Mole Fractions, '''if not already selected. |
|- | |- | ||
Line 212: | Line 212: | ||
|- | |- | ||
|| 04:20 | || 04:20 | ||
− | || Now drag and drop another '''Material Stream '''to the flowsheet. | + | || Now drag and drop another '''Material Stream '''to the '''flowsheet'''. |
|- | |- | ||
|| 04:25 | || 04:25 | ||
− | || Click on '''Material Stream '''“'''MSTR-001” '''to view its properties. | + | || Click on '''Material Stream''' “'''MSTR-001” '''to view its properties. |
|- | |- | ||
Line 252: | Line 252: | ||
|- | |- | ||
|| 05:11 | || 05:11 | ||
− | || Now let us specify the '''Methanol In''' stream compositions. | + | || Now, let us specify the '''Methanol In''' stream compositions. |
|- | |- | ||
|| 05:17 | || 05:17 | ||
− | || Under '''Composition''', choose the '''Basis '''as '''Mole Fractions, '''if not already selected | + | || Under '''Composition''', choose the '''Basis '''as '''Mole Fractions, '''if not already selected. |
− | + | ||
By default, '''Mole Fractions '''is selected as '''Basis.''' | By default, '''Mole Fractions '''is selected as '''Basis.''' | ||
Line 274: | Line 273: | ||
|- | |- | ||
|| 05:48 | || 05:48 | ||
− | || Now let’s insert two more material | + | || Now, let’s insert two more '''material stream'''s that exit the '''Heat Exchanger'''. |
|- | |- | ||
Line 302: | Line 301: | ||
|- | |- | ||
|| 06:14 | || 06:14 | ||
− | || Leave that stream as unspecified. | + | || Leave that '''stream''' as unspecified. |
|- | |- | ||
Line 310: | Line 309: | ||
|- | |- | ||
|| 06:22 | || 06:22 | ||
− | || Now let us insert a '''Heat Exchanger '''into the '''flowsheet'''. | + | || Now, let us insert a '''Heat Exchanger '''into the '''flowsheet'''. |
|- | |- | ||
Line 343: | Line 342: | ||
|| 06:58 | || 06:58 | ||
|| Under '''Connections, '''click on the drop-down against '''Inlet Stream 1.''' | || Under '''Connections, '''click on the drop-down against '''Inlet Stream 1.''' | ||
− | |||
And select '''Methanol In.''' | And select '''Methanol In.''' | ||
Line 352: | Line 350: | ||
|- | |- | ||
||07:14 | ||07:14 | ||
− | || Then click on drop-down against '''Inlet Stream 2 | + | || Then click on drop-down against '''Inlet Stream 2 ''' and select '''Water In.''' |
− | + | ||
− | + | ||
|- | |- | ||
|| 07:21 | || 07:21 | ||
− | || Then click on drop-down against '''Outlet Stream 2 | + | || Then click on drop-down against '''Outlet Stream 2''' and select '''Water Out.''' |
− | + | ||
− | + | ||
|- | |- | ||
Line 376: | Line 370: | ||
|- | |- | ||
||07:39 | ||07:39 | ||
− | || Select '''Outlet Temperatures ''' | + | || Select '''Outlet Temperatures.''' |
|- | |- | ||
|| 07:43 | || 07:43 | ||
− | || Next, click on the drop-down against '''Flow Direction''' | + | || Next, click on the drop-down against '''Flow Direction'''. Select '''Counter Current.''' |
− | + | ||
− | Select '''Counter Current.''' | + | |
|- | |- | ||
|| 07:51 | || 07:51 | ||
|| Then click on the field against '''Cold Fluid Pressure Drop '''and enter '''0.002 bar.''' | || Then click on the field against '''Cold Fluid Pressure Drop '''and enter '''0.002 bar.''' | ||
− | |||
Then press '''Enter.''' | Then press '''Enter.''' | ||
Line 400: | Line 391: | ||
|- | |- | ||
||08:15 | ||08:15 | ||
− | || Click on the field against '''Overall Heat Transfer Coefficient '''and enter it as '''450 Watt meter | + | || Click on the field against '''Overall Heat Transfer Coefficient '''and enter it as '''450 Watt meter square Kelvin.''' |
− | + | ||
Then press '''Enter.''' | Then press '''Enter.''' | ||
Line 407: | Line 397: | ||
|| 08:27 | || 08:27 | ||
|| Click on the field against '''Heat Exchange Area '''and enter it as '''250 meter square.''' | || Click on the field against '''Heat Exchange Area '''and enter it as '''250 meter square.''' | ||
− | |||
Then press '''Enter.''' | Then press '''Enter.''' | ||
|- | |- | ||
|| 08:37 | || 08:37 | ||
− | || Now we will run the '''simulation.''' | + | || Now we will '''run''' the '''simulation.''' |
|- | |- | ||
Line 448: | Line 437: | ||
|- | |- | ||
|| 09:28 | || 09:28 | ||
− | || Enter '''Name '''as '''Heat Exchanger – Stream Wise Results''' | + | || Enter '''Name '''as '''Heat Exchanger – Stream Wise Results'''. |
|- | |- | ||
Line 456: | Line 445: | ||
|- | |- | ||
|| 09:40 | || 09:40 | ||
− | || So we will not change it. | + | || So, we will not change it. |
|- | |- | ||
||09:43 | ||09:43 | ||
− | || Under '''Properties to display''', select '''Object '''as: '''Water In, Methanol In, Water Out, Methanol Out''' | + | || Under '''Properties to display''', select '''Object '''as: '''Water In, Methanol In, Water Out, Methanol Out'''. |
|- | |- | ||
|| 09:54 | || 09:54 | ||
− | || Under '''Property''', scroll down to see all the parameters. | + | || Under '''Property''', scroll-down to see all the parameters. |
|- | |- | ||
Line 470: | Line 459: | ||
||Now select the properties as: | ||Now select the properties as: | ||
− | '''Temperature''' | + | '''Temperature''', |
− | '''Pressure''' | + | '''Pressure''', |
− | '''Mass Flow''' | + | '''Mass Flow''', |
− | '''Molar Flow''' | + | '''Molar Flow''', |
|- | |- | ||
|| 10:11 | || 10:11 | ||
− | ||'''Molar Fraction(Mixture) / Methanol''' | + | ||'''Molar Fraction(Mixture) / Methanol''', |
|- | |- | ||
|| 10:15 | || 10:15 | ||
− | ||'''Molar Fraction(Mixture) / Water''' | + | ||'''Molar Fraction(Mixture) / Water'''. |
|- | |- | ||
Line 496: | Line 485: | ||
|- | |- | ||
|| 10:27 | || 10:27 | ||
− | ||Here we can see the corresponding results for '''Inlet''' and '''Outlet''' streams. | + | ||Here, we can see the corresponding results for '''Inlet''' and '''Outlet''' streams. |
|- | |- | ||
Line 524: | Line 513: | ||
|- | |- | ||
|| 10:59 | || 10:59 | ||
− | || Under '''Properties to display''', select '''Object '''as '''HE-004''' | + | || Under '''Properties to display''', select '''Object '''as '''HE-004'''. |
|- | |- | ||
Line 532: | Line 521: | ||
|- | |- | ||
|| 11:12 | || 11:12 | ||
− | ||Now select the properties as: '''Global Heat Transfer Coefficient (U)''' | + | ||Now, select the properties as: '''Global Heat Transfer Coefficient (U)''', |
|- | |- | ||
|| 11:17 | || 11:17 | ||
− | ||'''Heat Exchange Area (A)''' | + | ||'''Heat Exchange Area (A)''', |
− | + | '''Heat Load''', | |
− | '''Heat Load''' | + | |
|- | |- | ||
|| 11:21 | || 11:21 | ||
− | ||'''Cold fluid outlet temperature''' | + | ||'''Cold fluid outlet temperature''', |
− | + | '''Hot fluid outlet temperature''', | |
− | '''Hot fluid outlet temperature''' | + | |
|- | |- | ||
|| 11:26 | || 11:26 | ||
||'''Logarithmic mean temperature difference(LMTD)''' and | ||'''Logarithmic mean temperature difference(LMTD)''' and | ||
− | + | '''Thermal Efficiency'''. | |
− | '''Thermal Efficiency''' | + | |
|- | |- | ||
Line 570: | Line 556: | ||
|- | |- | ||
|| 11:45 | || 11:45 | ||
− | || In this tutorial, we have learnt to | + | || In this tutorial, we have learnt to: simulate a ''' Heat Exchanger''', |
|- | |- | ||
|| 11:50 | || 11:50 | ||
− | || | + | || calculate the''' Outlet stream temperatures, ''' |
|- | |- | ||
|| 11:53 | || 11:53 | ||
− | || | + | ||calculate''' Thermal Efficiency '''and''' LMTD'''. |
|- | |- | ||
|| 11:57 | || 11:57 | ||
− | || As an assignment, | + | || As an assignment, repeat this simulation with different '''Compounds, feed conditions '''and '''Thermodynamics'''. |
|- | |- | ||
Line 590: | Line 576: | ||
|- | |- | ||
|| 12:08 | || 12:08 | ||
− | ||It summarizes the Spoken Tutorial project. | + | ||It summarizes the '''Spoken Tutorial''' project. |
|- | |- | ||
|| 12:12 | || 12:12 | ||
− | || The Spoken Tutorial Project Team | + | || The Spoken Tutorial Project Team conducts workshops and gives certificates. |
− | + | ||
For more details, please write to us. | For more details, please write to us. | ||
Line 633: | Line 618: | ||
||13:09 | ||13:09 | ||
|| This tutorial is contributed by Kaushik Datta and Priyam Nayak. | || This tutorial is contributed by Kaushik Datta and Priyam Nayak. | ||
− | |||
Thanks for joining. | Thanks for joining. | ||
|} | |} |
Latest revision as of 11:13, 21 June 2018
Time | Narration |
00:01 | Welcome to this tutorial on simulating a Heat Exchanger in DWSIM. |
00:07 | In this tutorial, we will learn to: simulate a Heat Exchanger, |
00:13 | calculate the Outlet stream temperatures, |
00:16 | calculate Thermal Efficiency and LMTD. |
00:20 | To record this tutorial, I am using DWSIM 4.3 and Windows 7. |
00:28 | The process demonstrated in this tutorial is identical in other OS also, such as-
Linux, Mac OS X or FOSSEE OS on ARM. |
00:40 | To practice this tutorial, you should know how to add components to a flowsheet, |
00:47 | select thermodynamic packages, |
00:50 | add material stream and specify their properties. |
00:54 | The prerequisite tutorials are mentioned on our website. |
00:58 | You can access these tutorials and all the associated files from this site. |
01:04 | We will develop a flowsheet to determine the Outlet stream temperatures. |
01:09 | Here, we give Compounds and Inlet stream conditions. |
01:13 | Here, we give Heat Exchanger properties and Property package. |
01:18 | I have already opened DWSIM on my machine. |
01:23 | Go to File menu and select New Steady-state Simulation. |
01:28 | Simulation Configuration Wizard window appears. |
01:32 | At the bottom, click on Next button. |
01:36 | Now, in the Compounds Search tab, type Methanol. |
01:42 | Select Methanol from ChemSep database. |
01:46 | Similarly, add Water. |
01:49 | At the bottom, click on Next button. |
01:53 | Now comes Property Packages. |
01:56 | From Available Property Packages, double-click on Raoult’s Law. |
02:01 | Then click on Next button. |
02:04 | We are moved to a new window named Flash Algorithm. |
02:08 | From Default Flash Algorithm, select Nested Loops(VLE). |
02:14 | Click on Next button. |
02:17 | Next option is System of Units. |
02:21 | Under System of Units, select C5. |
02:26 | At the bottom, click on Finish button. |
02:30 | Let us maximize the simulation window for better visibility. |
02:35 | Now, let’s insert two material stream that enter the Heat Exchanger. |
02:41 | On the right hand side of the main simulation window, go to Flowsheet Objects. |
02:47 | In the Filter List tab, type Material Stream. |
02:52 | From the displayed list, drag and drop a Material Stream to the Flowsheet. |
02:58 | Click on the Material Stream “MSTR-000” to view its properties. |
03:04 | Let’s change the name of this stream to Water In. |
03:08 | Now we will specify the Water In stream properties. |
03:13 | Go to Input Data. |
03:15 | Select Flash Spec as Temperature and Pressure (TP), if not already selected. |
03:21 | By default, Temperature and Pressure are already selected as Flash Spec. |
03:27 | Change Temperature to 10 degC and press Enter. |
03:32 | Change Pressure to 1 bar and press Enter. |
03:37 | Change Mass Flow to 15000 kg per hour and press Enter. |
03:44 | Now, let us specify the feed stream compositions. |
03:49 | Under Composition, choose the Basis as Mole Fractions, if not already selected. |
03:56 | By default, Mole Fractions is selected as Basis. |
04:01 | Now for Methanol, enter the Amount as 0 and press Enter. |
04:08 | Similarly, for Water, enter it as 1 and press Enter. |
04:15 | On the right, click on this green tick to Accept Changes. |
04:20 | Now drag and drop another Material Stream to the flowsheet. |
04:25 | Click on Material Stream “MSTR-001” to view its properties. |
04:30 | Let’s change the name of this stream to Methanol In. |
04:35 | Now we will specify the Methanol In stream properties. |
04:40 | Go to Input Data. |
04:42 | Select Flash Spec as Temperature and Pressure(TP). |
04:46 | By default, Temperature and Pressure are again already selected as Flash Spec. |
04:42 | Change Temperature to 80 degC and press Enter. |
04:58 | Change Pressure to 5 bar and press Enter. |
05:03 | Change Mass Flow to 25000 kg/h and press Enter. |
05:11 | Now, let us specify the Methanol In stream compositions. |
05:17 | Under Composition, choose the Basis as Mole Fractions, if not already selected.
By default, Mole Fractions is selected as Basis. |
05:29 | Now for Methanol, enter the Amount as 1 and press Enter. |
05:36 | Similarly, for Water, enter it as 0 and press Enter. |
05:43 | On the right, click on this green tick to Accept Changes. |
05:48 | Now, let’s insert two more material streams that exit the Heat Exchanger. |
05:54 | To do that, let us drag one Material Stream. |
05:58 | Let us now arrange it. |
06:00 | Leave that stream as unspecified. |
06:03 | We will change the name of this stream to Water Out. |
06:07 | Next, we will insert another Material Stream. |
06:11 | Let us once again arrange it. |
06:14 | Leave that stream as unspecified. |
06:18 | And name this stream as Methanol Out. |
06:22 | Now, let us insert a Heat Exchanger into the flowsheet. |
06:27 | Go to the Flowsheet Objects. |
06:30 | In the Filter list tab, type Heat Exchanger. |
06:35 | Click on the Heat Exchanger displayed. |
06:39 | Drag and drop it to the flowsheet. |
06:42 | Let us now arrange it as required for better visibility. |
06:47 | We are now ready to specify the Heat Exchanger. Let's click on it. |
06:53 | On the left, we can see a tab called Property Editor Window. |
06:58 | Under Connections, click on the drop-down against Inlet Stream 1.
And select Methanol In. |
07:07 | Next, click on drop-down against Outlet Stream 1 and select Methanol Out. |
07:14 | Then click on drop-down against Inlet Stream 2 and select Water In. |
07:21 | Then click on drop-down against Outlet Stream 2 and select Water Out. |
07:28 | Now go to the next section- Calculation Parameters. |
07:32 | Here, the first option is Calculation Type. |
07:36 | Click on the drop-down against Calculation Type. |
07:39 | Select Outlet Temperatures. |
07:43 | Next, click on the drop-down against Flow Direction. Select Counter Current. |
07:51 | Then click on the field against Cold Fluid Pressure Drop and enter 0.002 bar.
Then press Enter. |
08:03 | Click on the field against Hot Fluid Pressure Drop and enter it as 0.025 bar. |
08:11 | Then press Enter. |
08:15 | Click on the field against Overall Heat Transfer Coefficient and enter it as 450 Watt meter square Kelvin.
Then press Enter. |
08:27 | Click on the field against Heat Exchange Area and enter it as 250 meter square.
Then press Enter. |
08:37 | Now we will run the simulation. |
08:40 | So, from the toolbar, click on Solve Flowsheet button. |
08:45 | When the calculations are completed, click on Heat Exchanger in the Flowsheet. |
08:50 | From the Property Editor Window of Heat Exchanger, locate Results section. |
08:56 | Check Thermal efficiency; it is 94.5%. Check Log Mean Temperature Difference; it is 10.29 degree Centigrade. |
09:09 | Now we will check the stream-wise temperature results and Material balance. |
09:15 | Go to Insert menu and select Master Property Table. |
09:20 | Double-click on Master Property Table to edit it. |
09:24 | Configure Master Property Table window opens. |
09:28 | Enter Name as Heat Exchanger – Stream Wise Results. |
09:33 | Enter Object Type as Material Stream. By default, Material Stream is already selected. |
09:40 | So, we will not change it. |
09:43 | Under Properties to display, select Object as: Water In, Methanol In, Water Out, Methanol Out. |
09:54 | Under Property, scroll-down to see all the parameters. |
10:00 | Now select the properties as:
Temperature, Pressure, Mass Flow, Molar Flow, |
10:11 | Molar Fraction(Mixture) / Methanol, |
10:15 | Molar Fraction(Mixture) / Water. |
10:19 | Close this window. |
10:22 | Move the Master Property Table for better visibility. |
10:27 | Here, we can see the corresponding results for Inlet and Outlet streams. |
10:33 | Now we will check the properties of Heat Exchanger. |
10:37 | Go to Insert menu and select Master Property Table. |
10:42 | Double-click on Master Property Table. |
10:46 | Configure Master Property Table window opens. |
10:50 | Enter Name as Heat Exchanger – Results. |
10:55 | Enter Object Type as Heat Exchanger. |
10:59 | Under Properties to display, select Object as HE-004. |
11:06 | Under Property, scroll down to see all the parameters. |
11:12 | Now, select the properties as: Global Heat Transfer Coefficient (U), |
11:17 | Heat Exchange Area (A),
Heat Load, |
11:21 | Cold fluid outlet temperature,
Hot fluid outlet temperature, |
11:26 | Logarithmic mean temperature difference(LMTD) and
Thermal Efficiency. |
11:32 | Close this window. |
11:35 | Move the Master Property Table for better visibility. |
11:39 | Here we can see the corresponding results for Heat Exchanger. |
11:43 | Let's summarize. |
11:45 | In this tutorial, we have learnt to: simulate a Heat Exchanger, |
11:50 | calculate the Outlet stream temperatures, |
11:53 | calculate Thermal Efficiency and LMTD. |
11:57 | As an assignment, repeat this simulation with different Compounds, feed conditions and Thermodynamics. |
12:05 | Watch the video available at following link. |
12:08 | It summarizes the Spoken Tutorial project. |
12:12 | The Spoken Tutorial Project Team conducts workshops and gives certificates.
For more details, please write to us. |
12:20 | Please post your times queries in this forum. |
12:24 | The FOSSEE team coordinates conversion of existing flow sheets into DWSIM. |
12:29 | We give honorarium and certificates. For more details, please visit this site. |
12:36 | The FOSSEE team coordinates coding of solved examples of popular books. |
12:41 | We give honorarium and certificates. For more details, please visit this site. |
12:48 | The FOSSEE team helps migrate commercial simulator labs to DWSIM. |
12:54 | We give honorarium and certificates. For more details, please visit this site. |
13:00 | Spoken Tutorial and FOSSEE projects are funded by NMEICT, MHRD, Government of India. |
13:09 | This tutorial is contributed by Kaushik Datta and Priyam Nayak.
Thanks for joining. |