- •Введение.
- •1.Построение технологической схемы процесса и моделирование статического режима.
- •Работа №1. Основы работы с Аспен Плюс. Работа с шаблонами, с библиотекой технологических объектов, потоками, компонентами
- •Лабораторная работа №2. Колонна экстрактивного разделения смеси метилциклогексана и толуола с использованием фенола в качестве экстрагента.
- •Icon and Place a
- •Работа №3. Моделирование процесса с вариациями входных данных для исследования параметрической чувствительности.
- •If Your Saved File
- •If Your Saved File
- •Versus Phenol Flow
- •Работа № 4. Определение параметров процесса для достижения качества целевого продукта.
- •If Your Saved
- •If Your Saved File
- •If Your Saved File
- •If Your Saved File
- •Into the Feed Stream
- •Information for
- •Vapor Pressure
- •Лабораторная работа № 5.
- •Лабораторная работа № 6. Моделирование процесса очистки кислых вод от кислых примесей в отпарной колонне с использованием химии электролитов и исследование особенностей ее работы
- •Isobarically at 15 psia
- •Работа №.7. Моделирование динамических режимов технологических схем совместно с контурами регулирования
- •1 Tutorial 1 - Entering Dynamic
- •2 Tutorial 2 - Modifying the
- •Is used
- •Viewing Results for
- •Variable
- •Variable is
- •Initializing Controller
- •Variables
- •Работа №8. Исследование динамических свойств технологической схемы и подбор оптимальных контуров регулирования и их оптимальных настроек
- •3 Tutorial 3 - Running the
- •Viewing the Full
Работа №.7. Моделирование динамических режимов технологических схем совместно с контурами регулирования
АспенДинамикс является мощным средством анализа динамики сложных технологических схем и образует унегрированную систему с Аспен Плюс, который обеспечивает синтез и анализ стационарных технологических схем. При использовании этого инструмента вначале проводится синтез и анализ технологической схемы в стационарном режиме, затем проводится переход к стационарному режиму. При этом система требует ввода дополнительных данных о характеристиках используемого оборудования, связанные с емкостями и задерживающими способностями отдельных элементов технологических схем, которые необходимы для моделировании переходных процессах в отдельных аппаратах технологических схем. После ввода всех технологических данных, проводится моделирование в динамическом режиме и системы сама расставляет необходимые регуляторы в тех точках технологической схемы, где заданы условия работы. Например, уровень в емкости, температура и давление в аппарате, и др. После этого можно экспортировать полученные результаты динамического моделирования в специально созданную рабочую папку. Из этой рабочей папки можно открыть задачу моделирования в программном комплексе АспенДинамикс, исследовать динамическое поведение схемы при наличии различных возмущений и усовершенствовать, при необходимости контуры регулирования и изменить их настройки для получения заданного качества регулирования.
В Работе №7 будет проведено создание схемы динамического моделирования процесса, а в Работе №8 будет проведено исследование динамических свойст и модификация контуров управления и выбор оптимальных настроек регуляиров.
Выполнение работ производится в точном соотвтетствии с рабочими инструкциями программного комплекса АспенДинамкс
1 Tutorial 1 - Entering Dynamic
Data and Exporting a File
In this tutorial you will:
Use Aspen Plus to modify an existing steady-state example
Add the equipment data and heat transfer information
necessary to simulate the process dynamically in Aspen
Dynamics
Generate and export the dynamic simulation files from Aspen
Plus for using in Aspen Dynamics
Allow about 20 minutes for this tutorial.
Experienced Aspen Plus users You will be opening the file
MCHSPEC in the directory Program Files\AspenTech\Aspen Plus
11.1\GUI\xmp. If you already know how to do this, go to page 1-5.
1-2 Tutorial 1 - Entering Dynamic Data and Exporting a File Getting Started Guide
Starting Aspen Plus
To start Aspen Plus:
1. Click the Start button, point to Programs, then AspenTech,
then Aspen Engineering Suite, then Aspen Plus 11.1, then
click the Aspen Plus User Interface.
The Aspen Plus Startup dialog box appears:
2. Select Blank Simulation, then click OK.
The Aspen Plus main window appears (see the picture on the
next page):
Getting Started Guide Tutorial 1 - Entering Dynamics Data and Exporting a File 1-3
1-4 Tutorial 1 - Entering Dynamic Data and Exporting a File Getting Started Guide
Opening an Existing Simulation
To open an existing simulation:
1. From the File menu, click Open.
2. In the Open dialog box, navigate to the folder where the
Aspen Plus User Interface was installed (for example,
C:\Program Files\AspenTech\Aspen Plus 11.1\GUI) then open
the xmp folder.
3. Click the file MCHSPEC to select it, then click Open.
A dialog box appears, asking if you want to close the current
run before opening a new run.
Getting Started Guide Tutorial 1 - Entering Dynamics Data and Exporting a File 1-5
4. Click Yes to close the current run and open the MCHSPEC
example backup file.
The MCHSPEC example file opens and the process flowsheet
appears (see the picture on the next page).
If you cannot see the Dynamic toolbar as shown
above, follow these steps to add the toolbar:
5. Ensure the flowsheet window is active, by clicking in it.
6. From the View menu, click Toolbar.
1-6 Tutorial 1 - Entering Dynamic Data and Exporting a File Getting Started Guide
7. In the Toolbars dialog box, ensure the Dynamic check box is
selected, like this:
8. Click OK.
The Dynamic toolbar is added to your toolbars.
About the MCH Steady-State
Simulation
The MCH example describes a simulation in which 98% pure
methylcyclohexane (MCH) is recovered from a mixture of MCH
and toluene. Because these components form a close-boiling
system that is difficult to separate by simple binary distillation,
phenol is used as an extractant to enhance the relative volatility of
MCH over toluene.
Aspen Plususes a design specification to determine the phenol
flow rate required to achieve the 98% purity in the distillate. You
can view the results of stream 2 to see that the required phenol
flow rate is approximately 1515 lbmol/hr.
Aspen Plus design specifications are often used for design
purposes and generally do not correspond directly to plant control
strategies. For this reason, Aspen Dynamics does not automatically
convert steady-state design specifications to dynamic controllers.
In tutorial 3, you will create a controller to maintain the product
purity.
Getting Started Guide Tutorial 1 - Entering Dynamics Data and Exporting a File 1-7
Entering Dynamic Data in Aspen Plus
Before entering any dynamic data in Aspen Plus, you would
usually run a steady-state simulation to ensure it completes
normally. For this tutorial you need not do this, because the
example file has already completed normally and has been saved
with results.
Before you can enter dynamic data, you have to click the Dynamic
button on the Dynamic toolbar. This enables you to access the
dynamic input data sheets for each block.
1. To access the dynamic data for the MCH column, click the
Dynamic button so that it is pressed in.
Dynamic button, pressed in
The RadFrac block (B1) contains forms that require dynamic
data, so the status indicator on the status bar changes to
Required Input Incomplete.
You can now use the Next button to guide you through the
required input data forms.
2. On the Data Browser toolbar, click the Next button and
the Flowsheet Complete dialog box appears.
1-8 Tutorial 1 - Entering Dynamic Data and Exporting a File Getting Started Guide
3. In the Flowsheet Complete dialog box, click OK to display
the first required input form.
The Data Browser opens with the Block B1 (RADFRAC)
Dynamic form displayed.
Note At this stage, no data is required on this form.
Getting Started Guide Tutorial 1 - Entering Dynamics Data and Exporting a File 1-9
Entering Condenser and Reboiler
Geometry and Heat Transfer Data
In this section, you will enter geometry and heat transfer data for
the condenser and reboiler. Geometry data is used to calculate the
vessel holdups. The required data are the vessel orientation, head
type, length and diameter.
For heat transfer purposes, you will use log-mean temperature
difference (LMTD) assumptions for the condenser. Heat duty is
dependent on the log mean temperature differential between the
process fluid and the heating/cooling medium. The reboiler heat
duty is assumed constant:
1. Click the Condenser sheet.
2. In the Heat transfer option box, click the down arrow to see
more options and from the list displayed, click LMTD.
Do not change the other default values. The Condenser sheet is
now complete.
3. Click Next to go to the Reflux Drum sheet.
4. In the Vessel Type box, select Horizontal from the list box.
1-10 Tutorial 1 - Entering Dynamic Data and Exporting a File Getting Started Guide
5. In the Length box, type 6 ft and in the Diameter box, type 3 ft,
like this:
Do not change the other values. The Reflux Drum sheet is now
complete.
6. Click Next to continue and the Sump sheet appears.
7. In the Height box, type 5 ft and in the Diameter box, type 3 ft.
Do not change the other values.
8. Press Enter to accept the input.
The Sump sheet is now complete and you have finished entering
data for the condenser and reboiler.
Entering Tray Geometry
The tray geometry data is used to calculate the holdups on the
trays. Column B1 has 22 theoretical stages.Stage1 being the
condenser and Stage22 the reboiler. Stages 2 through 21 are the
theoretical trays.
In the previous section, you specified the necessary information for
the condenser (stage 1) and the reboiler (stage 22). In this section,
you will enter the tray diameter geometry for stages 2 through 21.
The default values of the other parameters will be used.
1. Click Next to go to the Hydraulics sheet.
2. In the Stage1 column, type 2 and in the Stage2 column, type
21.
3. In the Diameter column, delete 6.56168 and type 5.
Getting Started Guide Tutorial 1 - Entering Dynamics Data and Exporting a File 1-11
4. Press Enter to accept the input and leave the remaining values
at their defaults.
The Tray geometry specifications are now complete and the
sheet looks like this:
5. Click Next to continue.
The Required Input Complete dialog box appears.
You have entered the additional data needed for the RadFrac
column and you are now ready to run the steady-state simulation.
You do this to ensure that all the results required to export the
dynamic simulation are calculated.
1-12 Tutorial 1 - Entering Dynamic Data and Exporting a File Getting Started Guide
Running the Steady-State Simulation
Having entered the dynamic specifications, you run the steady-state
simulation. To do this:
1. On the Required Input Complete dialog box, click OK.
Aspen Plus displays the Control Panel where you can view
the simulation messages during the run.
2. Wait for the message Simulation Calculations Completed to
appear and Results Available to appear in the status bar. This
indicates that the run is complete.
3. Click the Close button , to close the Control Panel window.
Getting Started Guide Tutorial 1 - Entering Dynamics Data and Exporting a File 1-13
Exporting the Dynamic Simulation
You are now ready to export the files necessary to run this
simulation dynamically. To do this:
1. From the File menu, click Export.
2. Go to the drive and folder where you want to save your file,
for example C:\My Simulations. Choose a folder other than
the xmp folder from which you selected the MCHSPEC
example because this folder is for system files only.
3. In the Save as type box, select Flow Driven Dyn Simulation
(*.dynf & *dyn.appdf).
4. In the File name box, type Mchdyn, then click Save.
These files are created:
Mchdyn.dynf, the Aspen Dynamics input file
Mchdyndyn.appdf, which contains physical property data for
use by Properties Plus during the dynamic simulation
Saving the Backup File
To save your changes to the Aspen Plus backup file:
1. From the File menu, click Save As.
2. Go to the folder where you saved your exported dynamic
simulation files.
3. In the Save As box, select Aspen Plus Backup files (*.bkp).
1-14 Tutorial 1 - Entering Dynamic Data and Exporting a File Getting Started Guide
4. In the File name box, type Mchdyn then click Save.
A dialog box appears requesting if you want to save the file in
Aspen Plus Document (quick restart) format.
5. There is no need to save it as an Aspen Plus Document file, so
click No.
Your simulation is saved as a backup file called Mchdyn.bkp.
Quitting Aspen Plus
Now that you have generated the files necessary for a dynamic run,
you are ready to run Aspen Dynamics. To quit Aspen Plus:
➤ From the File menu, click Exit.
Tutorial Review
In this basic tutorial, you have learnt how to use Aspen Plus to:
Modify an existing steady-state example
Add the equipment data and heat transfer information
necessary to simulate the process dynamically in Aspen
Dynamics
Generate and export the dynamic simulation files for use in
Aspen Dynamics
Getting Started Guide Tutorial 2 - Modifying the Control Scheme 2-1