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7/29/2019 Get Started Guide for New Users of Aspen HYSYS
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Get Started Guide for New Users of Aspen HYSYS V8.0
1. Lesson Objectives Learn how to create a new Aspen HYSYS simulation Learn to construct flowsheet, including adding blocks and streams, reconnecting streams, and
breaking/joining streams
2. Prerequisites Aspen HYSYS V8.0
3. BackgroundThis tutorial is for first-time Aspen HYSYS users. It shows new users:
How to launch Aspen HYSYS UI How to create a component list How to select a property package How to move from Properties environment to Simulation environment How to construct a f lowsheet
The examples presented are solely intended to illustrate specific concepts and principles. They may not
reflect an industrial application or real situation.
4. Aspen HYSYS Solution4.01. We will begin by launching Aspen HYSYS V8.0. From your desktop, select Startand then select All
Programs.
4.02. Select the folder titled AspenTech. Within this folder there is a folder called Process Modeling V8.0.Within the Process Modeling folder there will be folder titled Aspen HYSYS. Within this folder will be a
shortcut to AspenHysys.exe.
4.03. Clicking the Aspen HYSYS shortcut button will launch AspenHysys.exe. Once HYSYS loads up you havethe option of creating a new case or opening a previously saved case. If you wish to create a new case,
click the New button located on the Start Page. Right below the New button is the Open File
button. If you wish to open an example file, click the Examples button in the Get Started tab in the
ribbon.
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4.04. For this walkthrough we will create a new case. After selecting the New button on the Start Page, thefollowing page will appear.
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4.05. HYSYS wi ll open a new case starting in the Component Lists folder in the Properties environment.Creating a component list is the first step in creating a simulation. To create a component list, click the
Add button. This will create a HYSYS component list by default. If you wish to create an Aspen
Properties component list, you can select the down arrow and select Aspen Properties.
4.06. For this simulation we wi ll add components Methane, Ethane, Propane, i-Butane, n-Butane, and Water.In Component List 1 you wil l see a list of components on the right. You can simply double click on a
component from the list and it will be added to your simulation component list. If you wish to addmultiple components at a time, you can highlight a group of components and click the Add button.
4.07. In the following screenshot, you can see that after clicking the Add button, the selected components arenow in the component list on the left.
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4.08. You can also type the name of a component in the Search for field as shown below. Once you find thecomponent you are looking for, simply double click the component or click Add to add it to your
component list.
4.09. The completed component list for this simulation is shown below.
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4.10. The next step after creating a component list is to define a property package. Go to the Fluid Packagesfolder in the Navigation Pane. Clicking the Add button will create a fluid package from the HYSYS
database. You can also click the down arrow to select an Aspen Properties or COMThermo property
package.
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4.11. To choose a property package, click into the Basis-1 folder. You will be presented with a list of propertypackages that you can select from. For this simulation, we will choose the Peng-Robinsonequation of
state. Each property package has several options that you can select to more accurately model the
specific system you are working with.
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4.12. If you are working with petroleum assays, you may need to make use of the Petroleum Assays or OilManager folders. These subjects are discussed briefly in modules Dist-018 and Prop-005.
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4.13. If your system involves reactions, you will want to go to the Reactions folder. Here you can add reactionsets and specify reactions. HYSYS supports several types of reactions including conversion, equilibrium,
heterogeneous catalytic, kinetic, and simple rate.
4.14. The Component Maps folder lets you map fluid component composition across fluid packageboundaries. This is useful when dealing with hypothetical oil components. Two defined fluid packages
are required to perform a component mapping. In most cases you wil l not need to use this feature.
4.15. The User Properties folder is available for users to create their own properties. Once a user property isdefined, HYSYS will be able to calculate the value of the property for any stream through the User
Property util ity.
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4.16. For this simulation, after we have selected our property package, we wi ll move straight to theSimulation environment. To move to the Simulation environment, click the Simulation button in the
bottom left of the screen.
4.17. You should notice that the Model Palette automatically opens once you have moved to the Simulationenvironment. The model palette is where you can select unit operations and place them onto the
flowsheet. You should explore the model palette to get a sense of where certain unit operations are
located. Hovering the mouse over an icon will display a tool tip with the name of the unit operation.
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4.18. An alternative to the model palette is the Unit Ops window. Pressing F12will open the window shownbelow. This window lists every available unit operation in HYSYS. This window also includes radio
buttons to make finding the right unit operations easier.
4.19. To re-open the Model Palette, press F4. Place a Material Stream onto the flowsheet. Select the iconshown below and click on the f lowsheet where youd like to place the stream.
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4.20. Double click on the stream to rename it and specify the state variables, flowrate, and composition.When defining a stream you must specify a flowrate, composition, and two of the three state variables:
temperature, pressure, and vapour fraction.
4.21. For this example, enter a Temperatureof25C, a Pressure of1 bar, and a Molar Flow of100 kgmole/h.
Note that you can change the global unit set from the Home tab in the ribbon.
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4.22. To specify the composition ofStream 1, go to the Composition form under the Worksheettab. To editthe composition, click the Edit button or enter a number in the Mole Fractions area. Once a number is
entered the Input Composition window will automatically open.
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4.23. Enter the Mole Fractions shown below for Stream 1 and click the OK button. Once the composition isdefined the stream should solve.
4.24. In HYSYS, every block or stream has a status bar at the bottom. When the status bar turns green andsays OK, this means that the block/stream has fully solved. The block or stream on the flowsheet will
also change to a dark blue color to indicate that is has solved.
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4.25. We will now add our first unit operation to the flowsheet. Open the Model Palette again (F4) and selecta Mixer and place it onto the flowsheet.
4.26. Double click on the mixer (MIX-100). To connect streams to a block simply select Inlet streams andOutletstreams from the Connections form. Select Stream 1 to be an Inlet for the mixer. After selecting
Stream1 as an Inlet, the stream will be attached to the mixer on the flowsheet.
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4.27. You can either add more material streams to the flowsheet from the model palette and then selectthem as inlets or outlets from the mixer, or you can create new streams directly from the mixer. To do
this, simply click the Outlet field and type in a new name for a stream. This stream wil l then be created
and shown on the flowsheet accordingly. For example, lets enter the stream named Mixed into the
Outlet field as shown below.
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4.28. Notice that the status bar of the mixer is now green and says OK. This indicates that the mixer hasenough information and has fully solved. Also note that the flowsheet is updated with an outlet stream
called Mixed and the mixer block has turned blue, indicating that it is solved.
4.29. Create a second Inlet stream into the mixer called Water, as shown below. Notice that when you add anew inlet stream the status bar turns yellow and says Not Solved. This is because the new stream
called Water is not yet defined.
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4.30. To define the Water stream, you can double click the stream on the flowsheet, or go to the Worksheettab within the Mixer window. From the Worksheet tab, you can edit the conditions and composition of
any attached streams, assuming the degrees of freedom allows you to do so. Enter a Temperatureof
50C, a Pressure of1 bar, and Molar Flow of100 kgmole/h for the Water stream.
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4.31. Go to the Composition tab and enter a Mole Fraction of1 for water in the Water stream. You willnotice that as soon as the mixer has enough information to solve, it wil l do so.
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4.32. To view the results of the Mixed stream, double click on the stream. Notice that you are not able tomodify any of the stream conditions or compositions. This is because this stream is being specified by
the mixer based on the two inlet streams.
4.33. HYSYS also allows you to perform back calculations. For example, double click on the Water stream anddelete the Molar Flow.
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4.34. After deleting the molar flow of the Water stream, you will notice that both the Water stream and themixer are not unsolved. Double click on the mixer outlet stream called Mixed. You will notice that this
stream is also unsolved, and now you are able to modify the conditions of this stream. If you enter a
Molar Flow of150 kgmole/h, HYSYS wi ll back calculate the molar flow required for the Water stream.
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4.35. Now lets say you want to separate the vapor and liquid components of the mixed stream. Add aSeparator block to the flowsheet from the model palette.
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4.36. Double click on the separator block (V-100). Select stream Mixed as the Inlet and create a vapor outletcalled Vapor and a l iquid outlet called Liquid. You will notice that the separator will automatically solve
as soon as it has enough information to do so.
4.37. If you would like to put the solver on hold so that it does not automatically solve when it has enoughinformation, go to the Home tab in the ribbon. Here you will see an option to either put the solver OnHold or make it Active.
4.38. You should now know how to create a component list, select a property package, define reactions, andknow the basics of how to add unit operations and streams to the flowsheet.
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5. ConclusionsAfter going through steps described in this tutorial, first-time Aspen HYSYS users should now have the skil ls to
begin to create their first simulations and to follow the steps described in the University Teaching Modules.
6. CopyrightCopyright 2012 by Aspen Technology, Inc. (AspenTech). All rights reserved. This work may not be
reproduced or distributed in any form or by any means without the prior written consent of
AspenTech. ASPENTECH MAKES NO WARRANTY OR REPRESENTATION, EITHER EXPRESSED OR IMPLIED, WITH
RESPECT TO THIS WORK and assumes no liability for any errors or omissions. In no event will AspenTech be
liable to you for damages, including any loss of profits, lost savings, or other incidental or consequential
damages arising out of the use of the information contained in, or the digital fi les supplied with or for use with,
this work. This work and its contents are provided for educational purposes only.
AspenTech, aspenONE, and the Aspen leaf logo, are trademarks of Aspen Technology, Inc.. Brands and
product names mentioned in this documentation are trademarks or service marks of thei r respective companies.
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