Difference between revisions of "DWSIM/C2/Shell-and-Tube-Heat-Exchanger/English"

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(Created page with " {| border=1 ||'''Visual Cue''' ||'''Narration''' |- || '''Slide Number 1 '''Title Slide''' || Welcome to this tutorial on Simulating a '''Shell & Tube Heat Exchanger '''in '...")
 
 
(4 intermediate revisions by one other user not shown)
Line 13: Line 13:
 
'''Learning Objective'''
 
'''Learning Objective'''
 
|| In this tutorial, we will learn to:
 
|| In this tutorial, we will learn to:
−
 
−
 
 
* Simulate a''' Shell & Tube Heat Exchanger'''
 
* Simulate a''' Shell & Tube Heat Exchanger'''
 
* Calculate the '''Outlet stream temperatures'''
 
* Calculate the '''Outlet stream temperatures'''
Line 25: Line 23:
 
'''System Requirements'''
 
'''System Requirements'''
 
|| To record this tutorial, I am using
 
|| To record this tutorial, I am using
−
 
−
 
 
* '''DWSIM 4.3 '''and
 
* '''DWSIM 4.3 '''and
 
* '''Windows 7'''
 
* '''Windows 7'''
  
−
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  
 
* '''Mac OS X '''or  
Line 41: Line 36:
 
'''Pre-requisites '''
 
'''Pre-requisites '''
 
|| To practice this tutorial, you should know how to
 
|| To practice this tutorial, you should know how to
−
 
−
 
 
* add components to a '''flowsheet'''
 
* add components to a '''flowsheet'''
 
* select '''thermodynamic '''packages and
 
* select '''thermodynamic '''packages and
Line 51: Line 44:
  
 
'''Prerequisite Tutorials and Files'''
 
'''Prerequisite Tutorials and Files'''
−
|| The prerequisite tutorials are mentioned on our website, '''spoken-tutorial.org'''
+
|| The prerequisite tutorials are mentioned on our website.
  
  
Line 93: Line 86:
  
 
Pressure: 5 bar
 
Pressure: 5 bar
−
|| Here, We will develop a '''flowsheet '''to determine:
+
|| Here, we will develop a '''flowsheet '''to determine:
  
 
* '''Outlet stream temperatures'''
 
* '''Outlet stream temperatures'''
 
* '''Overall Heat Transfer coefficient '''and  
 
* '''Overall Heat Transfer coefficient '''and  
 
* '''Heat Exchange area.'''
 
* '''Heat Exchange area.'''
 +
 +
 +
  
  
Line 186: Line 182:
 
|-
 
|-
 
|| Click on '''Next.'''
 
|| Click on '''Next.'''
−
|| '''At the bottom, click on Next. '''
+
|| At the bottom, click on '''Next'''
  
 
|-
 
|-
Line 197: Line 193:
  
 
Double click on '''Raoult’s Law'''
 
Double click on '''Raoult’s Law'''
−
|| From '''Available Property Package '''list, double-click on '''Raoult’s Law.'''
+
|| From the '''Available Property Packages''', double-click on '''Raoult’s Law.'''
  
 
|-
 
|-
Line 249: Line 245:
 
|-
 
|-
 
|| Click on '''MSTR-000'''
 
|| Click on '''MSTR-000'''
−
|| Click on '''Material Stream '''“'''MSTR-000” '''to view its properties.
+
|| Click on '''MSTR-000 '''to view its properties.
  
 
|-
 
|-
Line 332: Line 328:
  
  
−
'''S'''elect '''Flash Spec '''as '''Temperature and Pressure (TP).'''
+
Select '''Flash Spec '''as '''Temperature and Pressure (TP).'''
  
  
Line 393: Line 389:
 
|-
 
|-
 
||  
 
||  
−
|| Leave that stream as unspecified.
+
|| Leave that '''stream''' as unspecified.
  
 
|-
 
|-
Line 409: Line 405:
 
|-
 
|-
 
||  
 
||  
−
|| Leave that stream as unspecified.
+
|| Leave that '''stream''' as unspecified.
  
 
|-
 
|-
Line 434: Line 430:
 
Drag and drop it to the '''flowsheet.'''
 
Drag and drop it to the '''flowsheet.'''
  
−
|-
 
−
||
 
−
|| Let us now arrange it as required for better visibility.
 
  
 
|-
 
|-
 
|| Click on '''Heat Exchanger'''
 
|| Click on '''Heat Exchanger'''
−
|| We are now ready to specify the '''Heat Exchanger.'''
+
|| Let us now arrange it as required for better visibility.
  
  
Line 505: Line 498:
  
 
|-
 
|-
−
|| Select '''Shell and Tubes Exchanger Rating'''
+
|| Select '''Shell and Tubes Exchanger Ratings'''
−
|| Select '''Shell and Tubes Exchanger Rating.'''
+
|| Select '''Shell and Tubes Exchanger Ratings.'''
  
 
|-
 
|-
Line 552: Line 545:
 
|-
 
|-
 
|| Point to '''Shell and Tube Exchanger Properties '''window
 
|| Point to '''Shell and Tube Exchanger Properties '''window
−
|| Here, we can see the by default values for Shell and Tube side configurations.
+
|| Here, we can see the by default values for '''Shell and Tube side configurations'''.
  
 
|-
 
|-
 
||  
 
||  
−
|| First we will edit the Shell Side Configuration.
+
|| First we will edit the '''Shell Side Configuration.'''
  
 
|-
 
|-
−
|| '''Shells in Series>>1'''
+
|| '''Shell in Series>>1'''
−
|| Click on the field against '''Shells in Series''' and enter it as '''1'''
+
|| Click on the field against '''Shell in Series''' and enter it as '''1'''
  
 
|-
 
|-
Line 584: Line 577:
 
|-
 
|-
 
||  
 
||  
−
|| This completes the '''Shell Side''' Configuration.
+
|| This completes the '''Shell Side Configuration.'''
  
 
|-
 
|-
 
||  
 
||  
−
|| Now we will edit the '''Tube Side''' Configuration.
+
|| Now we will edit the '''Tube Side Configuration.'''
  
 
|-
 
|-
Line 661: Line 654:
 
||  
 
||  
 
|| Check '''Cold Fluid Outlet Temperature'''<nowiki>; It is </nowiki>'''66.15 degree C'''
 
|| Check '''Cold Fluid Outlet Temperature'''<nowiki>; It is </nowiki>'''66.15 degree C'''
−
 
  
 
Check '''Hot Fluid Outlet Temperature'''<nowiki>; It is </nowiki>'''40.95 degree C'''
 
Check '''Hot Fluid Outlet Temperature'''<nowiki>; It is </nowiki>'''40.95 degree C'''
−
 
  
 
Check '''Overall Heat Transfer Coefficient'''<nowiki>; It is </nowiki>'''191.83 W/m<sup>2</sup> K'''
 
Check '''Overall Heat Transfer Coefficient'''<nowiki>; It is </nowiki>'''191.83 W/m<sup>2</sup> K'''
Line 677: Line 668:
 
|| '''Results '''
 
|| '''Results '''
 
|| Under '''Results''' section, check '''Thermal efficiency;''' it is '''79.05 %'''
 
|| Under '''Results''' section, check '''Thermal efficiency;''' it is '''79.05 %'''
−
 
  
 
Check '''Log Mean Temperature Difference;''' it is '''21.25 degree C.'''
 
Check '''Log Mean Temperature Difference;''' it is '''21.25 degree C.'''
Line 716: Line 706:
 
|| Under '''Properties to display''', select '''Object '''as:
 
|| Under '''Properties to display''', select '''Object '''as:
  
−
 
+
'''Water In, Methanol In, Water Out '''and''' Methanol Out.'''
−
'''Water In, Methanol In, Water Out '''and''' Methanol Out,.'''
+
  
 
|-
 
|-
 
|| '''Configure Master Property Table>>Property'''
 
|| '''Configure Master Property Table>>Property'''
 
|| Under '''Property''', scroll down to see all the parameters.
 
|| Under '''Property''', scroll down to see all the parameters.
−
 
  
 
Now select the properties as:
 
Now select the properties as:
Line 796: Line 784:
 
'''Hot fluid outlet temperature'''
 
'''Hot fluid outlet temperature'''
  
−
'''Logarithmic mean temperature difference LMTD'''
+
'''Logarithmic mean temperature difference LMTD''' and
  
 
'''Thermal Efficiency'''
 
'''Thermal Efficiency'''
Line 830: Line 818:
  
 
|-
 
|-
−
|| '''Slide Number 11 & 12'''
+
|| '''Slide Number 11, 12, 13 &  14'''
  
  
Line 839: Line 827:
  
  
−
'''Cold Stream:''' Toluene
+
Cold Stream: Toluene
  
−
'''Hot Stream:''' Acetone
+
Hot Stream: Styrene
  
  
Line 847: Line 835:
  
  
−
Mass Flow: 30000 lb/hr
+
Mass Flow: 50000 kg/h
  
−
Mole Fraction(C<sub>3</sub>H<sub>6</sub>O): 0
+
Mole Fraction(C<sub>7</sub>H<sub>8</sub>): 1
  
−
Mole Fraction(C<sub>6</sub>H<sub>5</sub>-CH<sub>3</sub>): 1
+
Mole Fraction(C<sub>8</sub>H<sub>8</sub>): 0
  
−
Temperature: 100 degree F
+
Temperature: 35 degree C
  
−
Pressure: 1 bar
+
Pressure: 6.5 bar
  
  
Line 861: Line 849:
  
  
−
Mass Flow: 15000 lb/hr
+
Mass Flow: 70000kg/h
  
−
Mole Fraction(C<sub>3</sub>H<sub>6</sub>O): 1
+
Mole Fraction(C<sub>7</sub>H<sub>8</sub>): 0
  
−
Mole Fraction(C<sub>6</sub>H<sub>5</sub>-CH<sub>3</sub>): 0
+
Mole Fraction(C<sub>8</sub>H<sub>8</sub>): 1
  
−
Temperature: 200 degree F
+
Temperature: 150 degree C
  
−
Pressure: 5 bar
+
Pressure: 3.5 bar
  
  
Line 877: Line 865:
 
Flow type: Counter-Current
 
Flow type: Counter-Current
  
−
<nowiki>Overall Heat Transfer Coefficient: 270 W/[m</nowiki><sup>2</sup>.K]
+
Cold Fluid Pressure Drop: 0.002 bar
  
−
Heat Exchanger Area: 75 m<sup>2</sup>
+
Hot Fluid Pressure Drop: 0.025 bar
  
−
Cold Fluid Pressure Drop: 0.0035 bar
+
Property Package: UNIFAC
  
−
Hot Fluid Pressure Drop: 0.0025 bar
 
  
−
Property Package: Raoult’s Law
+
'''Shell & Tube Exchanger Properties'''
 +
 
 +
 
 +
Type of Exchanger: 2-16 Shell & Tube Heat Exchanger
 +
 
 +
Total number of tubes: 1024
 +
 
 +
Tube Spacing: 75 mm
 +
 
 +
Tube Layout: Square
 +
 
 +
Thermal Conductivity of tube: 70 W/m K
 +
 
 +
Tube Roughness: 0.045 mm
 +
 
 +
Fouling Factor (tube side): 0 K m2/W
 +
 
 +
Tube Length: 5 m
 +
 
 +
External Diameter for tube: 60 mm
 +
 
 +
Tube thickness: 5 mm
 +
 
 +
Fouling Factor (shell side): 0 K m2/W
 +
 
 +
Shell Internal Diameter: 990.6 mm
 +
 
 +
Baffle Spacing : 250 mm
 +
 
 +
Baffle Cut: 25%
 +
 
 +
Fluid in Shell: Styrene
  
 
|| As an assignment,
 
|| As an assignment,
Line 893: Line 911:
  
 
|-
 
|-
−
|| '''Slide Number 13'''
+
|| '''Slide Number 15'''
  
 
'''About the Spoken Tutorial Project'''
 
'''About the Spoken Tutorial Project'''
Line 903: Line 921:
  
 
|-
 
|-
−
|| '''Slide Number 14'''
+
|| '''Slide Number 16'''
  
 
'''Spoken Tutorial Workshops'''
 
'''Spoken Tutorial Workshops'''
Line 910: Line 928:
 
* Conducts workshops and
 
* Conducts workshops and
 
* Gives certificates
 
* Gives certificates
−
* For more details, please write to contact@spoken-tutorial.org
+
* For more details, please write to us.
  
 
|-
 
|-
−
|| '''Slide Number 15'''
+
|| '''Slide Number 17'''
  
 
'''Forum Slide'''
 
'''Forum Slide'''
Line 931: Line 949:
  
 
|-
 
|-
−
|| '''Slide Number 16
+
|| '''Slide Number 18
 
'''DWSIM Flowsheeting Project'''
 
'''DWSIM Flowsheeting Project'''
  
Line 941: Line 959:
  
 
|-
 
|-
−
|| '''Slide Number 17
+
|| '''Slide Number 19
 
'''TextBook Companion Project'''
 
'''TextBook Companion Project'''
 
|| The '''FOSSEE '''team coordinates coding of solved examples of popular books.
 
|| The '''FOSSEE '''team coordinates coding of solved examples of popular books.
Line 952: Line 970:
  
 
|-
 
|-
−
|| '''Slide Number 18
+
|| '''Slide Number 20
 
'''Lab Migration Project'''
 
'''Lab Migration Project'''
 
|| The '''FOSSEE '''team helps migrate commercial simulator labs to '''DWSIM.'''
 
|| The '''FOSSEE '''team helps migrate commercial simulator labs to '''DWSIM.'''
Line 963: Line 981:
  
 
|-
 
|-
−
|| '''Slide Number 19
+
|| '''Slide Number 21
 
'''Acknowledgements'''
 
'''Acknowledgements'''
 
|| '''Spoken Tutorial '''and '''FOSSEE '''projects are funded by '''NMEICT, MHRD''', Government of India.
 
|| '''Spoken Tutorial '''and '''FOSSEE '''projects are funded by '''NMEICT, MHRD''', Government of India.
  
 
|-
 
|-
−
|| '''Slide Number 20
+
|| '''Slide Number 22
 
'''Thanks'''
 
'''Thanks'''
 
|| This tutorial is contributed by Kaushik Datta and Priyam Nayak.
 
|| This tutorial is contributed by Kaushik Datta and Priyam Nayak.

Latest revision as of 09:44, 9 March 2018

Visual Cue Narration
Slide Number 1

Title Slide

Welcome to this tutorial on Simulating a Shell & Tube Heat Exchanger in DWSIM.
Slide Number 2

Learning Objective

In this tutorial, we will learn to:
  • Simulate a Shell & Tube Heat Exchanger
  • Calculate the Outlet stream temperatures
  • Calculate Overall Heat Transfer Coefficient
  • Calculate Heat Exchange Area
  • Calculate Thermal Efficiency and LMTD
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
  • select thermodynamic packages and
  • add material stream and specify their properties.
Slide Number 5

Prerequisite Tutorials and Files

The prerequisite tutorials are mentioned on our website.


You can access these tutorials and all the associated files from this site.

Slide Number 6

Compounds and Inlet Condition


Cold Stream: Water

Hot Stream: Methanol


Cold Inlet Stream:


Mass Flow: 15000 kg/h

Mole Fraction(CH3OH): 0

Mole Fraction(H2O): 1

Temperature: 10 degree C

Pressure: 1 bar


Hot Inlet Stream:


Mass Flow: 25000kg/h

Mole Fraction(CH3OH): 1

Mole Fraction(H2O): 0

Temperature: 80 degree C

Pressure: 5 bar

Here, we will develop a flowsheet to determine:
  • Outlet stream temperatures
  • Overall Heat Transfer coefficient and
  • Heat Exchange area.



Here we give Compounds and Inlet stream conditions.

Slide Number 7

Heat Exchanger Properties


Flow type: Counter-Current

Cold Fluid Pressure Drop: 0.002 bar

Hot Fluid Pressure Drop: 0.025 bar

Property Package: Raoult’s Law

Here we give Heat Exchanger properties and Property package.
Slide Number 8 & 9


Shell & Tube Exchanger Properties


Type of Exchanger: 2-8 Shell % Tube Heat Exchanger


Total number of tubes: 2048

Tube Spacing: 25 mm

Tube Layout: Square

Thermal Conductivity of tube: 60 W/m K

Tube Roughness: 0.05 mm

Fouling Factor (tube side): 0.00035 K m2/W

Tube Length: 5 m

External Diameter for tube: 20 mm

Tube thickness: 2.5 mm

Fouling Factor (shell side): 0.00035 K m2/W

Shell Internal Diameter: 1000 mm

Baffle Spacing : 250 mm

Baffle Cut: 25%

Fluid in Shell: Methanol

Here we give Shell & Tube Heat Exchanger Properties.
I have already opened DWSIM on my machine.
File >>New Steady-state Simulation Go to File menu and select New Steady-state Simulation.
Point to Simulation Configuration Wizard window Simulation Configuration Wizard window appears.
Click on Next. At the bottom, click on Next.
Type Methanol in the Search tab Now, in the Compounds Search tab, type Methanol.
ChemSep database >>Methanol Select Methanol from ChemSep database.
Type Water in the Search tab Similarly, add Water.
Click on Next. At the bottom, click on Next
Point to Property Packages Now comes Property Packages.
Property Packages>> Available Property Package


Double click on Raoult’s Law

From the Available Property Packages, double-click on Raoult’s Law.
Click on Next. Then click on Next button.
Point to Flash Algorithm We are moved to a new window named Flash Algorithm.
Default Flash Algorithm >>Nested Loops (VLE) From Default Flash Algorithm select Nested Loops(VLE)
Click Next Click on Next button.
Point to System of Units Next option is System of Units.
System of Units >> C5 Under System of Units, select C5.
Click on Finish At the bottom, click on Finish button.
Let us maximize the simulation window for better visibility.
Now let’s insert two material streams that enter the Heat Exchanger.
Point to Flowsheet Objects. On the right hand side of the main simulation window, go to Flowsheet Objects.
In the Filter List tab, type Material Stream In the Filter List tab, type Material Stream.
Click and drag Material Stream to the flowsheet From the displayed list, drag and drop a Material Stream to the Flowsheet.
Click on MSTR-000 Click on MSTR-000 to view its properties.
Type Water In Let’s change the name of this stream to Water In.
Now we will specify the Water In stream properties.
Input Data>>Flash Spec>>Temperature and Pressure(TP) Go to 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.

Input Data >>Temperature >>10C

Press Enter

Change Temperature to 10 degC and press Enter.
Input Data >>Pressure >>1bar

Press Enter

Change Pressure to 1 bar and press Enter.
Input Data >>Mass Flow >>15000kg/h

Press Enter

Change Mass Flow to 15000 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 selected as Basis.

Methanol: 0 Now for Methanol, enter the Amount as 0 and press Enter.
Water: 1 Similarly, for Water, enter it as 1 and press Enter.
Click Accept Changes On the right, click on this green tick to Accept Changes.
Now drag and drop another Material Stream to the flowsheet.
Click on MSTR-000 Click on Material Stream “MSTR-001” to view its properties.
Type Methanol In Let’s change the name of this stream to Methanol In.
Now we will specify the Methanol In stream properties.
Input Data>>Flash Spec>>Temperature and Pressure(TP) Go to Input Data.


Select Flash Spec as Temperature and Pressure (TP).


By default, Temperature and Pressure are again already selected as Flash Spec.

Input Data >>Temperature >> 80 degC

Press Enter

Change Temperature to 80 degC and press Enter.
Input Data >>Pressure >>5 bar

Press Enter

Change Pressure to 5 bar and press Enter.
Input Data >>Mass Flow >>25000 kg/h

Press Enter

Change Mass Flow to 25000 kg/h and press Enter.
Now let us specify the Methanol In stream compositions.
Composition >>Basis >>Mole Fractions Under Composition, choose the Basis as Mole Fractions, if not already selected.


By default, Mole Fractions is selected as Basis.

Methanol: 1 Now for Methanol, enter the Amount as 1 and press Enter.
Water: 0 Similarly, for Water, enter it as 0 and press Enter.
Click Accept Changes On the right, click on this green tick to Accept Changes.
Now let’s insert two more material streams that exit the Heat Exchanger.
Click and Drag Material Stream to the flowsheet To do that, let us drag one Material Stream.
Let us now arrange it.
Leave that stream as unspecified.
Type Water Out We will change the name of this stream to Water Out.
Click and drag Material Stream to the flowsheet Next, we will insert another Material Stream.
Let us once again arrange it.
Leave that stream as unspecified.
Type Methanol Out And name this stream as Methanol Out.
Now let us insert a Heat Exchanger into the flowsheet.
Go to Flowsheet Objects Go to Flowsheet Objects.
In the Filter list tab, type Heat Exchanger. In the Filter list tab, type Heat Exchanger.
Click and drag Heat Exchanger to the flowsheet Click on the Heat Exchanger displayed.


Drag and drop it to the flowsheet.


Click on Heat Exchanger Let us now arrange it as required for better visibility.


Let's click on it.

On the left, we can see a tab called Property Editor Window.
Go to Connections


Click on drop down arrow against Inlet Stream 1


Select Methanol In.

Under Connections, click on the drop-down against Inlet Stream 1.


And select Methanol In.

Click on drop down arrow against Outlet Stream 1


Select Methanol Out.

Next, click on the drop-down against Outlet Stream 1.


And select Methanol Out.

Click on the drop down against Inlet Stream 2


Select Water In.

Then click on the drop-down against Inlet Stream 2.


And select Water In.

Click on the drop down against Outlet Stream 2


Select Water Out.

Then click on the drop-down against Outlet Stream 2.


And select Water Out.

Hover mouse at Calculation Parameters Now go to the next section- Calculation Parameters.
Here, the first option is Calculation Type.
Click drop down against Calculation Type Click on the drop-down against Calculation Type.
Select Shell and Tubes Exchanger Ratings Select Shell and Tubes Exchanger Ratings.
Click drop down against Flow Direction.


Select Counter Current

Next, click on the drop-down against Flow Direction


Select Counter Current.

Cold Fluid Pressure Drop>>0.002 bar


Press Enter

Then click on the field against Cold Fluid Pressure Drop and enter 0.002 bar.


Then press Enter.

Hot Fluid Pressure Drop>>0.025bar


Click on the field against Hot Fluid Pressure Drop and enter it as 0.025 bar.
Press Enter Then press Enter.
Click Edit Shell and Tube Heat Exchanger Properties Now we will enter the properties of Shell & Tube Exchanger.


Click on Edit Shell and Tube Heat Exchanger Properties.

Shell and Tube Exchanger Properties window opens.
Point to Shell and Tube Exchanger Properties window Here, we can see the by default values for Shell and Tube side configurations.
First we will edit the Shell Side Configuration.
Shell in Series>>1 Click on the field against Shell in Series and enter it as 1
Shell Passes>>2 Click on the field against Shell Passes and enter it as 2
Internal Diameter>>1000 mm Click on the field against Internal Diameter and enter it as 1000
Fouling Factor>>0.00035 K m2/W Click on the field against Fouling Factor and enter it as 0.00035
Baffle Spacing >>250 mm Click on the field against Baffle Spacing and enter it as 250
Baffle Cut(% diameter)>>25% Click on the field against Baffle Cut(% diameter) and enter it as 25
This completes the Shell Side Configuration.
Now we will edit the Tube Side Configuration.
Internal Diameter>>15 mm Click on the field against Internal Diameter and enter it as 15
External Diameter>>20 mm Click on the field against External Diameter and enter it as 20
Length>>5 m Click on the field against Length and enter it as 5
Fouling Factor>>0.00035 K m2/W Click on the field against Fouling Factor and enter it as 0.00035
Roughness>>0.05 mm Click on the field against Roughness and enter it as 0.05
Thermal Conductivity>>60 W/m K Click on the field against Thermal Conductivity and enter it as 60
Passes per Shell>>4 Click on the field against Passes per Shell and enter it as 4
Tubes per Shell>>1024 Click on the field against Tubes per Shell and enter it as 1024
Tube Spacing>>25 mm Click on the field against Tube Spacing and enter it as 25
Tube Layout>>Square Click on the drop down against Tube Layout and select Square
Fluid in Tubes>>Cold Select the option Cold against Fluid in Tubes
Now all the Shell & Tube Exchanger Properties are specified.
Close the Shell and Tube Exchanger Properties window by clicking red cross mark on the top right of the window.
Now we will run the simulation.
Click Solve Flowsheet So, from the toolbar, click on Solve Flowsheet button.
Click Heat Exchanger When the calculations are completed, click on Heat Exchanger in the Flowsheet.
Hover mouse at Calculation Parameters From the Property Editor Window of Heat Exchanger, locate Calculation Parameters section.
Check Cold Fluid Outlet Temperature; It is 66.15 degree C

Check Hot Fluid Outlet Temperature; It is 40.95 degree C

Check Overall Heat Transfer Coefficient; It is 191.83 W/m2 K

Check Heat Exchange Area; It is 319.12 m2

Hover mouse at Results From the Property Editor Window of Heat Exchanger, locate Results section.
Results Under Results section, check Thermal efficiency; it is 79.05 %

Check Log Mean Temperature Difference; it is 21.25 degree C.

Now we will check the stream-wise temperature results and Material balance.
Insert >>Master Property Table Go to Insert menu and select Master Property Table.
Double click on Master Property Table Double-click on the Master Property Table to edit it.
Point to Configure Master Property Table Configure Master Property Table window opens.
Type Heat Exchanger – Stream Wise Results Enter Name as Heat Exchanger – Stream Wise Results
Object Type >>Material Stream Enter Object Type as Material Stream.


By default, Material Stream is already selected.

So we will not change it.
Object >>Methanol Out, Water Out, Methanol In and Water In. Under Properties to display, select Object as:

Water In, Methanol In, Water Out and Methanol Out.

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

Molar Fraction(Mixture) / Methanol

Molar Fraction(Mixture) / Water

Close this window. Close this window.
Move the Master Property Table for better visibility.


Here we can see the corresponding results for Inlet and Outlet streams.

Now we will check the properties of Heat Exchanger.
Insert >>Master Property Table Go to Insert menu and select Master Property Table.
Double click on Master Property Table Double-click on the Master Property Table.
Point to Configure Master Property Table Configure Master Property Table window opens.
Type Heat Exchanger – Results Enter Name as Heat Exchanger – Results.
Object Type >>Material Stream Enter Object Type as Heat Exchanger.
Object >>HE-004. Under Properties to display, select Object as HE-004
Configure Master Property Table>>Property Under Property, scroll down to see all the parameters.


Now select the properties as:


Global Heat Transfer Coefficient (U)

Heat Exchange Area (A)

Heat Load

Cold fluid outlet temperature

Hot fluid outlet temperature

Logarithmic mean temperature difference LMTD and

Thermal Efficiency

Close this window. Close this window.
Move the Master Property Table for better visibility.


Here we can see the corresponding results for Heat Exchanger.

Let's summarize.
Slide Number 10


Summary

In this tutorial, we have learnt to


  • Simulate a Shell & Tube Heat Exchanger
  • Calculate the Outlet stream temperatures
  • Calculate Overall Heat Transfer Coefficient
  • Calculate Heat Exchange Area
  • Calculate Thermal Efficiency and LMTD
Slide Number 11, 12, 13 & 14


Assignment


Compounds and Inlet Condition


Cold Stream: Toluene

Hot Stream: Styrene


Cold Inlet Stream:


Mass Flow: 50000 kg/h

Mole Fraction(C7H8): 1

Mole Fraction(C8H8): 0

Temperature: 35 degree C

Pressure: 6.5 bar


Hot Inlet Stream:


Mass Flow: 70000kg/h

Mole Fraction(C7H8): 0

Mole Fraction(C8H8): 1

Temperature: 150 degree C

Pressure: 3.5 bar


Heat Exchanger Properties


Flow type: Counter-Current

Cold Fluid Pressure Drop: 0.002 bar

Hot Fluid Pressure Drop: 0.025 bar

Property Package: UNIFAC


Shell & Tube Exchanger Properties


Type of Exchanger: 2-16 Shell & Tube Heat Exchanger

Total number of tubes: 1024

Tube Spacing: 75 mm

Tube Layout: Square

Thermal Conductivity of tube: 70 W/m K

Tube Roughness: 0.045 mm

Fouling Factor (tube side): 0 K m2/W

Tube Length: 5 m

External Diameter for tube: 60 mm

Tube thickness: 5 mm

Fouling Factor (shell side): 0 K m2/W

Shell Internal Diameter: 990.6 mm

Baffle Spacing : 250 mm

Baffle Cut: 25%

Fluid in Shell: Styrene

As an assignment,


Repeat this simulation with different Compounds, feed conditions and Thermodynamics.

Slide Number 15

About the Spoken Tutorial Project

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Slide Number 21

Acknowledgements

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Slide Number 22

Thanks

This tutorial is contributed by Kaushik Datta and Priyam Nayak.


Thanks for joining.

Contributors and Content Editors

Kaushik Datta, Nancyvarkey

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