aspen tutorial reaction
TRANSCRIPT
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Aspen TutorialChBE 431Spring 2005
Author: Joseph Zakzeski
Getting Started 2
Setup 2
VLE diagrams 4
Reactions 6
The Reactor 8
Separation: Flash Columns 11
Distillation Columns 12
Heat Exchangers 17
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Getting started
ClickAspen Plus User Interface icon and enter password once the simulator finishes initializing. Save
the file as a new file name and SAVE OFTEN with different versions (ie save as design1, make a change,
then save the new design as design2. If something goes wrong, then, its still possible to go back to
design1 and fix problems).
The simulator will open with the following screen after the password has been entered.
Setup
First, click the Data pull-down menu then clickSetup. This section allows the title, base units, and other
characteristics to be manipulated. Name the project and switch to the appropriate units. Note the toolbar
on the left part of the screen displayed in outline form. The rest of the system properties can be specified
using this toolbar by simply going down the list until all the sections have BLUE checkmarks.
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After finishing the initial setup, click on the Components section to define the species present. Click the
box under component ID and type in the name of the component (ie hydrogen or water). Select the type
(typically conventional). The Tab button can be used to move to remaining sections. The simulator will
input the component name and formula automatically if the species is present in the database. Enter all
elements accordingly.
3
Toolbar1: Name the
Project
2: Set the units
3. Set globalproperties
Select
Components
1: Type in compound ID
(ie hydrogen)
2: Select type (usuallyconventional)
3: Ensure that compound
name and formula are
correct
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After the components are entered, select Properties and Specifications on the toolbar. This section is
where the THERMODYNAMIC MODEL is selected. First, select an appropriate thermodynamic model
for that adequately models the components present. Using a correct thermodynamic model is crucial
because the entire separation system will be based on it. Select the thermodynamic model in the Base
Method section. Depending on the model chosen, the simulator should input the remaining required
information. Enter in any necessary information if required in the appropriate section. The section iscompleted when blue checkmarks appear on the screen.
VLE diagrams
Make sure to check the VLE diagrams to make sure that the boiling points, and components of the mixtures
match the components and that theres no unusual occurrences. To check the VLE diagrams, after
selecting the model, go to Tools, then Analysis, then Property, and finally Binary.
4
SelectSpecifications
under
Components
Select the
thermodynamic model
in the Base MethodSection
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Select the analysis type (typically Txy) and the components of interest. Setup the computer to use mole
fraction based on a particular component, and under the property method select the thermodynamic model
used. Select Go to get the Txy diagram, which should be analyzed for accuracy.
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1: Set Txy
diagram
2: Select
Components
3: Select Basis
and Component
4: Select phases
(typically Vapor
Liquid)
5: Set the pressure
(or temperature)
6: Select the
thermodynamic model
7: Select Go
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Reactions
The next step is to enter reaction stoichiometry and chemical kinetics. Scroll down on the toolbar to the
folder marked Reactions. Click Reactions, then click the subfolderReactions. A new screen should
appear. Click the New button.
On the next screen, hit the New button and fill in the information on the Edit Reaction Screen. Enter the
Reactants and the appropriate coefficients (Aspen automatically places a minus sign on the reactants) along
with the products. When the stoiciometry is correct, hit the Kinetics Tab
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Click
Reactionsand then
subfolder
Reactions
1: Click the New
button
2: Name the
reaction
3: Select the
reaction type
4: Click OK
Ensure no unusual
behavior (like spikes)
and that boiling points
match
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Under kinetics, select the appropriate reaction, select the phase (ie vapor), and enter the kinetic parameters.
Do not fill in the To space. When all the parameters have been entered, select Driving Force.
Under driving force, enter the appropriate basis (ie partial pressure for gases) for term1. Enter the correct
coefficients based on the kinetics (typically the reactants have a 0 exponential unless theyre present in the
rate equation). For the coefficients for driving force, unless theres a temperature dependence known, enter0s for all parameters. Under Term 2, the exponentials of all components is typically set at 0. Select Next.
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1: Hit New
2: Enter
Reactant
3: Enter coefficient
4: Select
Reaction Type
(usually kinetic)
5: Enter
Products and
Coefficients
6: Click Next
7: When finished, select
Kinetics Tab
1: Select
Reaction
2: Select
Phase
3: Enter kinetic
Parameters (ensure
units are correct)
Leave To
blank!
4: Select
Driving force
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The Reactor
At this point, the simulator is now ready for the unit operations. The best and place to start is with the
Reactor since this component is the most important in the process. On the main screen, select the Reactors
tab, click on the icon for the desired reactor (ie RPlug), and click on the screen to place the reactor. On the
far left part of the screen is a materials stream button. After placing the reactor, click on the material screen
and click on the blue arrow either entering or leaving the reactor to place the stream. Left clicking places
the streams, and right clicking deselects the materials button. To delete the reactor, simply right click the
icon on the screen and select the Delete Block option on the menu.
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1: Select Basis and Term
2: Set ex onentials
3: Select coefficients
4: Set up Term 2 in
kinetic reaction
5: Select Next
1: Select Reactors tab2: Click reactor and lace
3: Click materials
button and place
streams
Note: Reactants enter
the Top in the Blue
arrows. Coolant streams
enter through the Red
arrows
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Double click the stream entering into the reactor to specify its components. Select the appropriate
temperature and pressure along with the species present in the stream. Click next when finished.
The next step is to setup the reactor block. Select Blocks on the outline on the left. Select Setup. Select
the desired reactor type (ie isothermal, adiabatic, etc.). When finished, click configuration.
Enter the reactor length and diameter under configuration. Aspen uses these values to calculate conversion.
Click the Reactions tab when finished
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1: Double
click stream
2: Set Temperature
and Pressure
3: Specify
components
4: Ensure Total flow
equals Total flow
5: Click Next
1: Select
Blocks
2: Select theReactor and
then Setup
3: Select theReactor type and
enter necessary
information
4: When finished,
Click
configuration
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Under the reactions tab, simply select the reactions that are occurring in the reactor by double clicking the
reaction. Clicknext.
At this point, the simulator will attempt to converge the process flow diagram. Click OK and the computer
will run the simulation. To view the results of the process, double click the reactor or the stream leavingthe reactor to determine the species present.
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1: Enter
length and
diameter
2: Select
Reactions
Ensure correct phases
are allowed
1: Select
Reactions
2: Click Next
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Separation Flash Columns
In order to insert separation units, select the Separators Tab and select the desired unit. Place on thescreen as was done with the reactor. Right click the stream leaving the reactor and select Reconnect
Destination. Click on the separator to connect the stream. Finally, select the materials button and create
any other necessary streams. The example used is a flash column. Double click the flash column to set the
specifications including temperature and pressure. Clicknext to run the simulator. (NOTE: Flash Columns
cannot be sized in ASPEN to the best of my knowledge!)
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1: Double
Click stream
Species present
in stream
Three possibilities:
Error (red = plant blows up)
Results Available with Warnings(yellow = caution)
Results Available (blue =happiness)
1: Select
Separators
2: Place
Separator andReconnect Stream
Destination
3: Double click
separator and set
specifications
4: Click Next to
run Simulator
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Distillation Columns
Its best to start with a short-cut column before using a rigorous column in order to first acquire some
necessary information. First, click the columns tab and place the short-cut column on the screen. Connectthe stream similarly as was done with the flash column.
Double click the short-cut column to designate the specifications. Designate the column specifications (use
correlations). Clicknext to converge.
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1: Click
Columns Tab
2: Place short-cut
column
3: Reconnect
Streams
1: Set
specifications
2: Consider if itsbetter to have
Total or Partial
Condenser
3: Click Next
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Once the simulator converges and the system has adequately separated the components (takes some trial
and error), double click the short-cut column again. On the outline on the left part of the screen, click onresults and record the information. This information will aid in designing the rigorous column.
Delete the short-cut column and replace with the RadFrac column. This column is much more rigorous
(and also more difficult to converge). Use the information from the short-cut column to help design the
rigorous column.
Double click the RadFrac column. Under the Configuration Tab, enter the number of stages, select the
condenser type, distillate rate, and reflux ratio. Click the Streams tab when finished
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1: Double click
short-cut column
2: Click on Blocks,
The Distillation
Column, and then
Results3: Record all
information
4: When satisfied,
DELETE short-cut
column (save as a new
name in case you need to
go back)
1: Install
RadFrac
2: Reconnect
Lines
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On the Streams section, enter the feed stage and also where on the stage the stream enters (typically on
stage or above stage). Click the Pressure Tab.
In the Pressure Screen, designate the condenser pressure and clicknext. The Simulator should now attempt
to converge the Distillation Column. Check the outlet streams to ensure that the compositions the
conditions (Temperature and Pressure, etc.) are acceptable in each stream by double clicking the streams.
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1: Double
Click
RadFrac
2: Enter #
of Stages
3: Enter
Condenser,
Reboiler, andPhases
4: Input Operating
Specifications
5: Click the
Streams Tabwhen finished
1: Input Feed
Stage and
Convention
2: Ensure phases are
correct
3: Click Pressure
Tab
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In order to find the important information about the column, double click the column and select Results
Summary for condenser/reboiler duties and other information. Read through the other tabs for other
important or necessary information.
In order to size the trays, on the menu on the left, click the Tray Sizingfolder. On the screen that appears,
click the New button. A Tray Sizing Section Number should appear. Simply Click OK.
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1: Enter
Condenser
Conditions
2: ClickNext
1: Double
click
column
2: Click
Results
Summary
3: Admire what a
sweet column this is
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Aspen sizes the distillation columns on a single tray basis. Simply select a starting tray (ie 6) and an ending
tray. Also input the tray type. This section also indicates the spacing between the trays. Once everything
is designated, clickNext to converge the PFD.
After the simulator converges, double click the distillation column. The Tray Sizing folder will now have
a bluish color. Click the folder. On the new screen, select the box that says Results Available and hit the
edit button.
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1: Select
Tray Sizing
2: Click New
3: Select a
number and
press OK
1: Select
Starting Tray
(ie 6)
2: Select
Ending Tray
(ie 7)
3: Select tray
type
4: Click Next
Tray
Spacing
indicated
here
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On the new screen, click the results tab. The column diameter is listed on this menu.
Heat Exchangers
To insert a heat exchanger, click on the Heat Exchanger Tab and place the desired heat exchanger on the
screen (HeatX is the rigorous exchanger. Use this type rather than starting with a shortcut exchanger). TheHeatX exchanger requires both the shell side and tube side streams. If cooling, for example, without using
heat integration, simply designate the stream a water stream at the desired temperature by double clicking
the stream and filling in the appropriate information.
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1: Doubleclick
distillation
column
2: Click
Tray Sizing
(now blue)
3: Click
ResultsAvailable
4: Click Edit
1: Click
Results Tab
2: Record
Column
Diameter
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For the unspecified stream, just enter the desired temperatures and flowrates, then close the box
Double click the heat exchanger to specify the parameters. A shortcut calculation should suffice. Specify
the stream conditions (ie, hot stream outlet temperature, cold stream outlet temperature), and ensure that the
minimum approach temperature is AT LEAST 10K. When finished at this screen, select pressure drop.
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1: Select Heat
Exchangers Tab
2: Place Heat X
(rotate if desired)
3: Connect Material
Streams
4: Double click
unspecified
Stream
1: Enter
Temperature
2: Enter
Pressure
3: Enter species
and total flowrate
4: Close the box
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Specify the pressure drop that occurs in both the hot and the cold side of the exchanger. Click U Methods.
Select and appropriate U term for the system (depending on if the species are both liquids, liquid/gas,
condensing gas, etc.) Clicknext to converge PFD.
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1: Enter
Specification
2: Ensure minimum
approach temperature
at least 10K
3: Click Pressure
Drop
1: Designate
Hot or Coldside
2: Specifyoutlet pressure
3: Click U
Methods
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Double click the Heat Exchanger. Click the Thermal Results listing on the Outline, and clickExchanger
Details to find the heat duty and exchanger area. Make sure to check the streams leaving and entering the
exchanger to ensure appropriate conditions.
You should now have enough of the basic tools to design a chemical system using ASPEN. Several otherunit operations are available and can be placed and used similarly. Make sure to save often when making
changes under new file names because its easier to make changes to a working diagram than it is to fix and
make changes to one that doesnt work. Good luck!
1: Select
Appropriate U
(watch units!)
2: click Next
1: Double
Click Heat
Exchanger
2: Click Thermal
Results
3: Click
Exchanger
Details
4: Note
Duty, Area,
U, and otherinfo
5: Check actual streams to
ensure appropriate conditions