- •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
2 Tutorial 2 - Modifying the
Control Scheme
To use this tutorial, you must have successfully completed tutorial
1 of this book.
In this tutorial, you will use Aspen Dynamics to:
Modify the control scheme associated with the column in the
MCHDYN simulation by adding a composition controller to
maintain the purity of the distillate stream (stream 3).
The controller will measure the MCH composition in the
distillate stream and manipulate the phenol solvent stream
(stream 2).
Modify the controller tuning parameters (gain and integral
time) for better control performance.
Allow about 25 minutes for this tutorial.
2-2 Tutorial 2 - Modifying the Control Scheme Getting Started Guide
About Aspen Dynamics Control
Features
In Aspen Dynamics you can easily:
Add, change and remove control elements
Select measured and manipulated variables from selection lists
Configure cascade control loops
Import control structures from other Aspen Dynamics
generated input files
When an Aspen Dynamics simulation is created, level, pressure
and temperature controllers are automatically included where
appropriate. For flow-driven dynamic simulations, these controllers
are configured as shown in this table:
For this type
of control
This type of controller
Is used
To directly
manipulate
Liquid level Proportional only Liquid flow rate
Pressure Proportional integral Vapor flow rate or duty, as
appropriate
Temperature Proportional integral Duty
Getting Started Guide Tutorial 2 - Modifying the Control Scheme 2-3
Starting Aspen Dynamics
To start Aspen Dynamics:
➤ Click your desktop Start button, then point to:
Programs | AspenTech | Aspen Engineering Suite | Aspen
Dynamics 11.1
When you first start Aspen Dynamics, you will see that there is no
simulation information and you start with a blank simulation. The
following diagram shows the three windows of Aspen Dynamics:
2-4 Tutorial 2 - Modifying the Control Scheme Getting Started Guide
The three windows of Aspen Dynamics are:
The Process Flowsheet window
The Simulation Messages window
The Simulation Explorer, which is split into two panes:
All Items pane, which contains the library or folder of
models
Contents pane, which contains all the individual objects of
the selected library or folder
The default pane orientation of the Simulation Explorer has the All
Items pane above the Contents pane. If your panes are currently
displayed side by side, it is recommended that you change back to
the default pane orientation to make it easier to follow the tutorial.
To do this:
1. Ensure the Simulation Explorer window is active by clicking
in it.
2. From the View menu, point to Pane Orientation, then click
Top to Bottom.
Tip You can rearrange, resize and reposition any of your
windows.
To open an existing simulation:
1. From the File menu, click Open.
2. In the Open dialog box that appears, locate the drive or folder
that contains the Mchdyn files that you exported from
tutorial 1.
3. In the Files of type list, ensure Aspen Dynamics Files (*.dynd,
*.dynf) is selected.
Opening an Existing
Simulation
Getting Started Guide Tutorial 2 - Modifying the Control Scheme 2-5
4. Select Mchdyn, then click Open to load the Mchdyn
simulation.
The file takes a few moments to open, then the flowsheet
appears.
Each automatically-generated controller has a Process variable,
Operator set point, and Controller output whose values are
calculated from the steady-state results of the Aspen Plus run. Each
controller also has its own tuning parameters such as gain, integral
time, derivative time, and so on. You can modify the values of
these control parameters as shown on page 2-14.
For this example, Aspen Dynamics creates these controllers by
default:
Reflux drum liquid level (LC1)
Top stage pressure (PC2)
Sump liquid level (LC3)
The pressure controller PC2 is defined as a Proportional Integral
(PI) action controller, with defaults for gain and integral time,
while the level controllers are proportional-only controllers with
default values for gain.