Apresentacao PROII
-
Upload
caique-ferreira -
Category
Documents
-
view
81 -
download
7
Transcript of Apresentacao PROII
-
2010 Invensys. All Rights Reserved. The names, logos, and taglines identifying the products and services of Invensys are proprietary marks of Invensys or its subsidiaries. All third party trademarks and service marks are the proprietary marks of their respective owners.
Introduction to PRO/II
-
Neliana DAlessandri
Telefone: [email protected]
-
Course Content
Introduction
PRO/II Basics
Simulation Setup
Main Parts of a Simulation
Components
Thermodynamics
Stream Data
Unit Operations
Phase Equilibrium Considerations
Distillation
Utilities and Keywords
Customization and Output
Help
-
2010 Invensys. All Rights Reserved. The names, logos, and taglines identifying the products and services of Invensys are proprietary marks of Invensys or its subsidiaries. All third party trademarks and service marks are the proprietary marks of their respective owners.
Introduction
-
PIPEPHASENETOPTTACITE
Oil and Gas Production
PRO/IIVISUAL FLOW
INPLANT
ProcessEngineering
ROMeoARPMMBM
CONNOISSEUR
On-LinePerformance
DYNSIMFSIM
TRISIMOTS
DynamicSimulation
Products fall into one of four
Solution SuitesSolution SuitesSolution SuitesSolution SuitesSolution SuitesSolution SuitesSolution SuitesSolution Suites
SIMSCI Solution Suites
-
SIM4ME Portal Excel integration with Simsci software simulation packages. Allows for bidirectional transfer of applicable variables between programs, and allows users without simulation experience the opportunity to interact with the simulator without necessitating prior knowledge or experience with the simulation software.
SIM4ME Portal
SIM4ME Portal is an integration application that facilitates the
powerful combination of SIMSCI-ESSCORs various process
simulation products (PRO/II, VISUAL FLOW, INPLANT, PIPEPHASE,
and ROMeo/ARPM) with Microsoft Excel.
-
2010 Invensys. All Rights Reserved. The names, logos, and taglines identifying the products and services of Invensys are proprietary marks of Invensys or its subsidiaries. All third party trademarks and service marks are the proprietary marks of their respective owners.
PRO/II Basics
-
Slide 9
Objectives
Learn how to build a simulation from scratch
Get familiar with PRO/II Capabilities & Features
Know where to find further information
-
PRO/II Capabilities and Features
Large component and thermodynamics databank
1700+ Components
60+ Thermodynamic Methods
Electrolytes capabilities with OLI and OLI MSE
1900+ Components
100+ Thermodynamic Methods
Polymers and solids handling capabilities
Flexible and powerful refining capabilities
Reactive and electrolytic distillation modeling
-
PRO/II Capabilities and Features
Regression and data management tools
Customizable
Components
Calculational and thermodynamic methods
User interface
Report
OLE Functionality (Excel Unit)
Graphs, tools, charts, tables, and plots can be exported to other tools
-
PRO/II Capabilities and Features
Advanced flowsheet sequencing and integration capabilities
Excel Interfacing
SIM4ME Reports
SIM4ME Portal
Excel Unit Operation
COM Interface
KG Tower
HTRI
AMSIM
CAPE-OPEN
BATCHFRAC and RATEFRAC
-
PRO/II vs. PROVISION vs SIM4ME
PRO/II is the calculation engine
PROVISION is the graphical user interface
Makes PRO/II easy to use
Over time, older operating systems are no longer supported while
newer ones become supported
SIM4ME Portal is similar to PROVISION, but encompasses all
products
Common platform for multiple SimSci products
-
Steady State Simulator
No Time Dependent Phenomena
Exception: Depressuring Unit
Controllers and Instrumentation are Irrelevant
-
Simplify the Flowsheet by...
Grouping units if desired
-
12 3
Sequential-Modular Simulator
Units solved one at a time
Feeds must be known
Recycles automatically handled
-
2010 Invensys. All Rights Reserved. The names, logos, and taglines identifying the products and services of Invensys are proprietary marks of Invensys or its subsidiaries. All third party trademarks and service marks are the proprietary marks of their respective owners.
Simulation Setup
-
Started PROII
Slide 18
-
Color coded borders
RED = Data required
GREEN = Default data already entered
BLUE = User data entered
YELLOW = Default data, but suggested
to review
Toolbar
Menu bar
PFD
GUI-Desktop Environment
-
Menu Bar
-
New File
Open
Save
Assay Char.
Rec Data
Print
Basic Windows Functions
PDF Pallet UOMs
Notes Comps
Comp Props
Thermo
Main Pro/II Setup Options
TDM
RXN Data
RXN Proc
Case Study
Sequence
Advanced Options
Toolbar
-
2010 Invensys. All Rights Reserved. The names, logos, and taglines identifying the products and services of Invensys are proprietary marks of Invensys or its subsidiaries. All third party trademarks and service marks are the proprietary marks of their respective owners.
Simulation Steps
-
1Build Flowsheet
Check Units of Measure
2
Define Components
3
Select Thermo
4
Supply Stream
Data
5
Provide Process
Conditions
6
Run & View
Results
7
Simulation in 7 Steps
-
Adding Units and Streams to the Flowsheet
1 2 3
4 5
-
Hot - Horizontal
Cold
P = 0
Vapor
Liquid
Water from the bottom
Beware of Defaults
-
Simulation in Seven Steps
1
Build Flowsheet
2
Define Components
3
Check Units of Measure
4
Supply Stream
Data
5
Provide Process
Conditions
6
Run & View
Results
7
Select Thermo
-
Common source of errors
English is default
Units of Measure
-
Common source of errors
English is default
Defaults can be changed either
Globally (for all future simulations)
Options Simulation Defaults UOM
For single flowsheet
Locally in DEW
Can define custome set of UOM
Options Units of measure list
Units of Measure
-
Slide 29
Changing UOM Locally
Change units of measureFor example,32F 32C
Convert value to new UOMFor example,32F 0C
-
Can define custome set of UOM
Options Units of measure list
Units of Measure
-
1Build Flowsheet
2
Define Components
3
Check Units of Measure
4
Supply Stream
Data
5
Provide Process
Conditions
6
Run & View
Results
7
Select Thermo
Simulation in 7 Steps
-
Component Selection
Library Components
User-defined Components
Petroleum Components
Assays (covered in Streams section)
-
Built-in Databanks:
SIMSCI (default)
PROCESS
OLILIB
User Libraries
Organized by Groups
Sort By options:
Full Name
Alias
Formula
Dynamic Search
Library Components
-
Databank Hierarchy
For Library Components Only
Designates library databank
order that PRO/II uses to
search for components
Searches top library first
Must use when using
customer components
from TDM
-
Petroleum Components
Normal Boiling Point
Gravity
Molecular Weight
At least 2 of 3 required
-
2010 Invensys. All Rights Reserved. The names, logos, and taglines identifying the products and services of Invensys are proprietary marks of Invensys or its subsidiaries. All third party trademarks and service marks are the proprietary marks of their respective owners.
Exercise 1Chiller Plant, Part 1, pg 6
-
Recover liquids and deliver gas to pipeline
Only doing part 1 right now
C2
PipelineGas
T1Stabilizer
M2
M1 Natural GasLiquids (NGL)
S14
S18 S20
S1
S19
V1
HX3
F3
Refrigerant
S12
S10 S11
S13S17
F1
Cooling Air
S9
C1
HX1
F2S2 S4 S5
S6
S7
S3
Inlet Gas
S8
HX2
S16
S15
S1
Simulate a Chiller Plant in 4 Parts
-
Slide 38
Chiller Plant, Part 1, pg 6
1
Build Flowsheet
2
Define Components
3
Check Units of Measure
4
Supply Stream
Data
5
Provide Process
Conditions
6
Run & View
Results
7
Select Thermo
-
User-defined Components
Only provide name in Component Selection DEW
Properties entered in Component Properties DEW
-
Component Properties
All component properties managed here
View or change any component properties
Local to individual simulation file
Global changes made in TDM
-
Component Properties
-
Component Properties
-
Component Properties
-
Component Data Output Report
Always 1st page
9 Properties
displayed in
output
Most commonly
referred to
properties
-
Simulation in Seven Steps
IPS Confidential
1
Build Flowsheet
2
Define Components
3
Check Units of Measure
4
Supply Stream
Data
5
Provide Process
Conditions
6
Run & View
Results
7
SelectThermo
-
ThermodynamicSystem
CondenserDuty
Reflux/FeedRatio
Peng-Robinson -59.6 13.1Grayson-Streed -37.3 8.2
Example: Propane/Propylene Splitter
Choice of thermo method strongly affects results!
-
Selecting a Thermo Method
A thermo method is required for all simulations
-
Selecting a Thermo Method
Ideal
Equations of State (SRK, PR, BWRS, Lee-Kesler-Plocker, etc)
Liquid Activity Models (NRTL, UNIQUAC, Wilson, UNIFAC, etc)
Generalized Correlations (Braun K10, Grayson-Streed, etc)
Special Packages (Alcohol, Glycol, Sour, GPA Sour Water, Amine)
Electrolytes (Amines, Acids, Mixed Salts, Sour Water, Caustic, etc)
Polymers
User-added Methods
CAPE-OPEN
Chapter 3 of the PRO/II Reference Manual
-
Enabling VLLE Calculations
-
Modifying a Thermo Method
Select method for
each property
K-values
Mass Balances
Enthalpies
Heat Balances
Densities
Entropies
-
Water Decant Option Rigorous VLLE Calcs
Water Decant Options
-
Water Decant Options
-
Vapor
Pure WaterLiquid
Water VaporPressure
VLE K-values
Water Solubility
Water Decant Options
-
VLE K-valuesVapor
Liquid 2Liquid 1
VLE K-values
LLE K-values
Rigorous VLLE Calculations
-
Can turn them off/on
Required for certain unit operations:
Columns
Rigorous Heat Exchangers
Pipes
Dissolvers
Depressuring Units
Specific output report properties
Transport Properties
-
2 Liquid Diffusivity
Wilke-Chang
User-defined
5 Overall Methods:
Pure
Petroleum
TRAPP
TACITE
User-defined
Transport Properties
-
Suggestions: Hydrocarbon Systems
Refining Processes:
Grayson-Streed: Hydrogen rich systems, Crude tower, Vaccum
unit, Coker fractionator, FCC main fractionator
SRK and PR: Light ends columns, Splitters, Gas recovery plants,
Hydrogen rich systems (SRKM)
SOUR, GPSWATER: Sour water systems
SRKK, SRKM, SRKS, IGS: Use if hydrocarbon solubility in liquid
water (VLLE) is important.
-
Suggestions: Hydrocarbon Systems
Gas Processing:
SRK and PR: All types of processing plants, cryogenic systems
SRKM, PRM, and SRKS: Systems with water, methanol, and other
polar components
GLYCOL: Dehydration with TEG. Improved for aromatic emissions.
Based on SRKM.
AMINE: Natural gas sweetening
SRKK, IGS, SRKM, SRKS: Use if light gas solubility in water (VLLE)
is important
-
Online Thermodynamic Help
Reference Manual
Detailed technical reference with
application guidelines for when to
use each method
Volume 1 refers to technical data
on component and thermo specific
information
Accessed through:
Start All Programs SIMSCI PRO/II
PRO/II Documentation Reference Manual
Volume 1
Windows Explorer folders shown
-
Simulation in Seven Steps
1
Build Flowsheet
2
Define Components
3
Check Units of Measure
4
Supply Stream
Data
5
Provide Process
Conditions
6
Run & View
Results
7
Select Thermo
-
Types of Streams
-
Stream Attributes
Flowrate
Composition
Defined by components
Defined by assay data
Referenced to another stream
Solids only stream
Thermo Conditions
Provide 2
Temperature
Pressure
Bubble Point
Dew Point
Liquid Mole Fraction
Liquid Weight Fraction
Liquid Volume Fraction
-
Compositional Streams
Consist of:
Library components
Petroleum components
User-defined components
Normalize composition
Composition and flowrate
basis in:
Weight
Mole
Liquid Volume
Vapor Volume
-
Assay Streams
Entire assay definition entered in stream
-
Assay Streams
Entire assay definition entered in stream
Flowrate required
Optional
Using a different cutpoint set
Excluding an assay stream from blending
-
Assay Streams - Definition
Required:
Percent Distilled
vs Temperature
Gravity Data
Average value
Curve data
Optional:
Molecular Weight
Lightends
Refinery Inspection
Properties
User-defined
parameters
-
How to Get Assay Data
T
% Distilled
Thermometer
Burner V
T
-
Assay Processing Steps
-
Light Ends Matching
-
Computing NBPs and Gravities
-
100
150
200
250
300
350
400
450
500
0 10 20 30 40 50 60 70 80 90 100
Percent Distilled
T
e
m
p
e
r
a
t
u
r
e
(
F
)
NBP-288NBP-311NBP-262
Only two petrocomponentsin overlap region
Cutpoint Sets
Not enough pseudocomponents?
-
100
150
200
250
300
350
400
450
500
0 10 20 30 40 50 60 70 80 90 100
Percent Distilled
T
e
m
p
e
r
a
t
u
r
e
(
F
)
Many petrocomponentsin overlap region
Cutpoint Sets
Add more cuts to the cutpoint set
-
Assay Characterization Options
Edit or create new cutpoint sets
Change methods used to define pseudocomponents
-
Assay Characterization Options
Edit or create new cutpoint sets
Change methods used to define pseudocomponents
-
Assay Characterization Options
Edit or create new cutpoint sets
Change methods used to define pseudocomponents
-
Assay Data Entry in PRO/II Summary
-
Assay Data Entry in PRO/II Summary
-
2010 Invensys. All Rights Reserved. The names, logos, and taglines identifying the products and services of Invensys are proprietary marks of Invensys or its subsidiaries. All third party trademarks and service marks are the proprietary marks of their respective owners.
Exercise 2
Naphtha Assay
Part 1, p. 39
-
Reference Streams
Attributes defined in terms of another stream
Composition *
Flowrate (molar) **
Temperature **
Pressure **
* = Cant be changed
** = Can be changed
-
Thermal Recycles
Solves in 3 iterations
-
Breaking Thermal Recycles
Solves in 1 iteration using a reference stream
-
2010 Invensys. All Rights Reserved. The names, logos, and taglines identifying the products and services of Invensys are proprietary marks of Invensys or its subsidiaries. All third party trademarks and service marks are the proprietary marks of their respective owners.
Exercise 3Chiller Plant, Part 2, pg 14
-
2010 Invensys. All Rights Reserved. The names, logos, and taglines identifying the products and services of Invensys are proprietary marks of Invensys or its subsidiaries. All third party trademarks and service marks are the proprietary marks of their respective owners.
Utilities
-
Slide 84
Stream Utilities
Hotkeys
Flash stream
BVLE
Phase Envelope
Heating/Cooling Curves
Copying streams
-
Slide 85
Stream Hotkeys
Flash
Find component molar flowrates of a stream
Determine phases of a stream
Calculate T with known P and liquid fraction
BVLE
Graph the phase equilibrium data for pairs of components
Plot activity coefficients, fugacity coefficients, K-values, and
compositions versus T, P, and composition
-
2010 Invensys. All Rights Reserved. The names, logos, and taglines identifying the products and services of Invensys are proprietary marks of Invensys or its subsidiaries. All third party trademarks and service marks are the proprietary marks of their respective owners.
Exercise 4Gas Cooling, pg 31
-
Before
After
Gas Cooling, pg 31
Which stream should you reference stream 5 to and why?
-
Simulation in Seven Steps
IPS Confidential
1
Build Flowsheet
2
Define Components
3
Check Units of Measure
4
Supply Stream
Data
5
Provide Unit Op
Conditions
6
Run & View
Results
7
Select Thermo
-
Slide 89
Unit Operations
50+ Unit Operations and counting
Cover various unit operations throughout the rest of training course
This section is information on unit operations in general
-
Slide 90
Unit Operations
-
All UOPs required feed stream data and product streams connected
Required data always in Red
Flash Drum Example:
Feed Rate
Flash Temperature
Flash Pressure
Choice of 1 other:
Flash Temperature
Flash Pressure
Duty
Product Rate
Product Composition
Product Property
Data Entry Example Flash Drum
-
Flash Calculations
-
Required
Feed Composition (N)
Feed Rate
Flash Temperature
or
Flash Pressure
Choice of One
Flash Temperature
Flash Pressure
Duty
Product Rate
Product Composition
Product Property
Flash Calcs - Degrees of Freedom (N+3)
-
Mixer Splitter
FM1
MNM
F1
FN
Valve
F1
FN
VLW
Flash CalculationUOPs that Perform Flash Calculations
-
Enthalpies from different methods
Using Multiple Thermo Methods
-
Changing the Enthalpy Method
Enthalpies from same methods
Thermo Reset Unit
-
2010 Invensys. All Rights Reserved. The names, logos, and taglines identifying the products and services of Invensys are proprietary marks of Invensys or its subsidiaries. All third party trademarks and service marks are the proprietary marks of their respective owners.
Exercise 7Chiller Plant, Part 3, pg 17
-
2010 Invensys. All Rights Reserved. The names, logos, and taglines identifying the products and services of Invensys are proprietary marks of Invensys or its subsidiaries. All third party trademarks and service marks are the proprietary marks of their respective owners.
Distillation
-
Tray Numbering
Use Theoretical Trays (Stages)
Each stage is another flash calculation
Numbered from Top to Bottom
Condenser is always stage 1 if used
Even for subcooled condenser
Reboiler is always the last stage if used
Certain types add more than 1 effective stages
Model your reboiler based on how the return stream mixes back into
the column, not by what the actual type of reboiler it is
General Rule of Thumb when Converting Packing to Stages:
2 3 feet of packing per stage
Modern structured packing could be inches, so check with the
manufacturer
-
Tray Efficiency
Murphree
Vaporization
Equilibrium
Vapor leaving stage not at dew point
Can lead to mixed phase condenser product
Better to use overall efficiencies
Theoretical / Actual trays to carry out separation
Use different values in different column zones
Dont forget condenser and reboiler!
-
Typical Overall Efficiencies (%)
Deethanizers 60-65
C3 Splitters 95-100
Crude Units
Stripping Section 30
Flash Zone to Gas Oil 30-40
G.O. Draw to Diesel Draw 40-50
Diesel Draw to Kero Draw 45-55
Top Section of Column 55-65
Columns with reboilers and condensers 60-80
Pumparounds eliminate trays 20-25
-
2010 Invensys. All Rights Reserved. The names, logos, and taglines identifying the products and services of Invensys are proprietary marks of Invensys or its subsidiaries. All third party trademarks and service marks are the proprietary marks of their respective owners.
Exercise 9Chiller Plant, Part 4, pg 21
-
Specifications and Variables
Specifications are constraints to be met by the column
Variables are calculated to meet specifications
Column always balances equations with unknowns (i.e. # of
specifications = # of variables)
To impose a specification, you must add a variable, other equations
and unknowns dont balance.
Example: Impose 2 product specifications by declaring reboiler and
condenser duties as variables
-
Improper Specifications
0% methane in crude column bottoms
Infinitely many solutions
300 lbmol/hr propylene in overhead
No solutions if column feed only has 250 lbmol/hr propylene
98% ethanol product
No solutions if water-ethanol azeotrope present
-
Keyword Files
Text version of PRO/II File
Significantly smaller size than *.prz files
Contains only the most important information for the simulation
Only shows items you have changed from default values
Keyword file runs very fast through batch mode
Useful for
Smaller size means less space when archiving simulation files or
sending via email
Running a large *.prz file in a shorter amount of time
Merging multiple *.prz files together (export *.prz files to keyword,
then copy/paste from 1 file to the other)
Troubleshoot input errors
Export *.prz file to keyword and reimport to clean simulation databases
Restore damaged *.prz files using input file in an output report
-
Exporting and Importing Keyword Files
To export a PRO/II file to keyword, go to File Export, then
choose Simulation Data to Keyword File
To import a keyword file to PRO/II,
go to File Import and select the
keyword file (*.inp)
-
Simulation in Seven Steps
1
Build Flowsheet
2
Define Components
3
Check Units of Measure
4
Supply Stream
Data
5
Provide Unit Op
Conditions
6
Run & View
Results
7
Select Thermo
-
Customization Options Menu
-
Customization SPTs and UOPTs
Stream and Unit Ops Property Lists
Convenient tool to view the composition
and properties of selected streams
-
Customization SPTs and UOPTs
Stream and Unit Ops Property Lists
Convenient tool to view the composition
and properties of selected streams
Easy to customize
Easy to export to Excel
Included with the PRZ as of PRO/II 8.0
Prior to PRO/II 8.0 you had to include the
SPROP.INI file
-
Customization Global UOM
Easy to create your own custom UOM slate
Located in your User directory in the p2uomin.ini
Units transferred UOM slate is not
-
Customization Simulation Defaults
-
Output Options
Generate Output Report
Text and Excel Options
Right Click View Results
Text and Excel Options
STPs and UOPTs and the Data Review Window
Copy/Paste
Tables and Plots
Excel Spreadsheets (Tools Spreadsheets)
SIM4ME Reports
-
Text Output Reports
Generate Text Output Report
Consists of:
Input File
Convergence History
Output Results
Similar results as Right Click View Results, but in more detail
Results customizable
-
Output Report Format
-
Output Units of Measure
-
Output Miscellaneous Data
-
Output Stream Properties
-
Right Click View Results
Each Unit Op and Stream has the right-click menu option for View
Results or View Excel Results
-
Copying/Pasting, Tables and Graphs
Copy/paste input data from UOPs/streams to and from Excel
Example: Entire column profile data
Results from SPTs/UOPTs, text output reports, tables/graphs, the
data review window, case studies, and more can be copy/pasted
into Excel directly
-
Copying/Pasting, Tables and Graphs
Copy/paste input data from UOPs/streams to and from Excel
Example: Entire column profile data
Results from SPTs/UOPTs, text output reports, tables/graphs, the
data review window, case studies, and more can be copy/pasted
into Excel directly
-
Copying/Pasting, Tables and Graphs
Copy/paste input data from UOPs/streams to and from Excel
Example: Entire column profile data
Results from SPTs/UOPTs, text output reports, tables/graphs, the
data review window, case studies, and more can be copy/pasted
into Excel directly
-
Excel Output - Spreadsheets
14 Customizable Excel output reports
Tools Spreadsheets
Quick and easy
-
Excel Output SIM4ME Reports
Create customer Excel reports with only the information you want
Customize
Which units/streams are reported
Level of detail they are reported
Layout of the results
Units of Measurement
Does not require an additional license
2 Customer reports already available
Summary Simplified Excel report for all units and streams. Similar to
Right Click View Results
Detailed Detailed Excel report for all units and streams. Similar to
generating the text output report.
-
New
Will open SIM4ME Reports
Select Active Report
Open Active Report
Will open SIM4ME Reports
Generate Excel Report
View Excel Report
Delete Active Report
Export Report
For others to use
Import Report
To use others SIM4ME Reports
Add to Active Report
Adds selected UOP/Stream to Active Report
SIM4ME Reports Report Manager
-
Toggles the Flowsheet Explorer tree on/off
New, Open, and Save Report
Messages, Generate Report, View Report, and Refresh
SIM4ME Reports Data Entry Window
-
2010 Invensys. All Rights Reserved. The names, logos, and taglines identifying the products and services of Invensys are proprietary marks of Invensys or its subsidiaries. All third party trademarks and service marks are the proprietary marks of their respective owners.
PRO/II Help
-
Where to find help?
PRO/II Manuals
Start Programs Simsci PRO/II PRO/II documentation
On Hard Drive: C:\SIMSCI\PROII\Manual Welcome.pdf
On the same CD-ROM as the program
PRO/II Help Menus
Searchable
Context Sensitive
-
Technical Support
Neliana Azacom
Email: [email protected]
Phone: +11-28440213
Technical Support
Email: [email protected]
-
2010 Invensys. All Rights Reserved. The names, logos, and taglines identifying the products and services of Invensys are proprietary marks of Invensys or its subsidiaries. All third party trademarks and service marks are the proprietary marks of their respective owners.
Questions?
-
2010 Invensys. All Rights Reserved. The names, logos, and taglines identifying the products and services of Invensys are proprietary marks of Invensys or its subsidiaries. All third party trademarks and service marks are the proprietary marks of their respective owners.
Thank You!