Based on the information provided, a hydrocarbon system and petroleum refining process type have been selected. The recommended property package is NRTL.
Does this help summarize the recommended package? Let me know if you need any clarification or have additional questions!
This is course on Plant Simulation will show you how to setup hypothetical compounds, oil assays, blends, and petroleum characterization using the Oil Manager of Aspen HYSYS.
You will learn about:
Hypothetical Compounds (Hypos)
Estimation of hypo compound data
Models via Chemical Structure UNIFAC Component Builder
Basis conversion/cloning of existing components
Input of Petroleum Assay and Crude Oils
Typical Bulk Properties (Molar Weight, Density, Viscosity)
Distillation curves such as TBP (Total Boiling Point)
ASTM (D86, D1160, D86-D1160, D2887)
Chromatography
Light End
Oil Characterization
Using the Petroleum Assay Manager or the Oil Manager
Importing Assays: Existing Database
Creating Assays: Manually / Model
Cutting: Pseudocomponent generation
Blending of crude oils
Installing oils into Aspen HYSYS flowsheets
Getting Results (Plots, Graphs, Tables)
Property and Composition Tables
Distribution Plot (Off Gas, Light Short Run, Naphtha, Kerosene, Light Diesel, Heavy Diesel, Gasoil, Residue)
Oil Properties
Proper
Boiling Point Curves
Viscosity, Density, Molecular Weight Curves
This is helpful for students, teachers, engineers and researchers in the area of R&D, specially those in the Oil and Gas or Petroleum Refining industry.
This is a "workshop-based" course, there is about 25% theory and about 75% work!
At the end of the course you will be able to handle crude oils for your fractionation, refining, petrochemical process simulations!
Aspen Plus basic course for Engineers.
Introduction to Process Modeling/Simulation Software.
INDEX:
Course Objectives
Introduction to Aspen Plus
User Interface & Getting Help
Physical Properties
Introduction to Flowsheet
Unit Operation Models
Reporting Results
Case Studies I, II and III
Case Study IV
Conclusion
Course by Chemical Engineering Guy
Check out full course:
http://www.chemicalengineeringguy.com/courses/aspen-plus-physical-properties-course/
Ask me for special discounts, or checkout "SURPIRSE" tab in my site for special discounts.
This is course on Process Simulation will show you how to model, manipulate and report thermodynamic, transport, physical and chemical properties of substances.
You will learn about:
Physical Property Environment
Physical Property Method & Method Assistant
Fluid and Property Packages
Physical property input, modeling, estimation and regression
Thermodynamic Properties (Material/Energy balances and Thermodynamic Processes)
Transport Properties for (Mass/Heat/Momentum Transfer)
Equilibrium Properties (Vapor-Liquid, Liquid-Liquid, etc...)
Getting Results (Plots, Graphs, Tables)
This is an excellent way to get started with Aspen Plus. Understanding the physical property environment will definitively help you in the simulation and flowsheet creation!
This is a "workshop-based" course, there is about 50% theory and about 50% practice!
LINK:
https://www.chemicalengineeringguy.com/courses/aspen-plus-intermediate-course/
The INTERMEDIATE Aspen Plus Course will show you how to model and simulate more complex Processes
Analysis of Unit Operation will help you in order to simulate more complex chemical processes, as well as to analyse and optimize existing ones.
You will learn about:
- Better Flowsheet manipulation
- Hierarchy, Flowsheeting, Sub-flowsheet creation
- Logical Operators / Manipulators
- Understand Property Method Selection and its effects on simulation results
- Study of more rigorous unit operations
- Model Analysis Tools such as sensitivity and optimization
- Reporting Relevant Results Plot relevant data for Heaters, Columns ,Reactors, Pumps
- Temperature Profiles, Concentration Profile, Pump Curves, Heat Curves, etc…
- Up to 3 Case Studies (in-depth analysis)
All theory is backed up by more than 30 Practical Workshops!
At the end of the course you will be able to setup more complex processes, increase your simulation and flow sheeting techniques, run it and debugging, get relevant results and make a deeper analysis of the process for further optimization.
This is course on Plant Simulation will show you how to setup hypothetical compounds, oil assays, blends, and petroleum characterization using the Oil Manager of Aspen HYSYS.
You will learn about:
Hypothetical Compounds (Hypos)
Estimation of hypo compound data
Models via Chemical Structure UNIFAC Component Builder
Basis conversion/cloning of existing components
Input of Petroleum Assay and Crude Oils
Typical Bulk Properties (Molar Weight, Density, Viscosity)
Distillation curves such as TBP (Total Boiling Point)
ASTM (D86, D1160, D86-D1160, D2887)
Chromatography
Light End
Oil Characterization
Using the Petroleum Assay Manager or the Oil Manager
Importing Assays: Existing Database
Creating Assays: Manually / Model
Cutting: Pseudocomponent generation
Blending of crude oils
Installing oils into Aspen HYSYS flowsheets
Getting Results (Plots, Graphs, Tables)
Property and Composition Tables
Distribution Plot (Off Gas, Light Short Run, Naphtha, Kerosene, Light Diesel, Heavy Diesel, Gasoil, Residue)
Oil Properties
Proper
Boiling Point Curves
Viscosity, Density, Molecular Weight Curves
This is helpful for students, teachers, engineers and researchers in the area of R&D, specially those in the Oil and Gas or Petroleum Refining industry.
This is a "workshop-based" course, there is about 25% theory and about 75% work!
At the end of the course you will be able to handle crude oils for your fractionation, refining, petrochemical process simulations!
Aspen Plus basic course for Engineers.
Introduction to Process Modeling/Simulation Software.
INDEX:
Course Objectives
Introduction to Aspen Plus
User Interface & Getting Help
Physical Properties
Introduction to Flowsheet
Unit Operation Models
Reporting Results
Case Studies I, II and III
Case Study IV
Conclusion
Course by Chemical Engineering Guy
Check out full course:
http://www.chemicalengineeringguy.com/courses/aspen-plus-physical-properties-course/
Ask me for special discounts, or checkout "SURPIRSE" tab in my site for special discounts.
This is course on Process Simulation will show you how to model, manipulate and report thermodynamic, transport, physical and chemical properties of substances.
You will learn about:
Physical Property Environment
Physical Property Method & Method Assistant
Fluid and Property Packages
Physical property input, modeling, estimation and regression
Thermodynamic Properties (Material/Energy balances and Thermodynamic Processes)
Transport Properties for (Mass/Heat/Momentum Transfer)
Equilibrium Properties (Vapor-Liquid, Liquid-Liquid, etc...)
Getting Results (Plots, Graphs, Tables)
This is an excellent way to get started with Aspen Plus. Understanding the physical property environment will definitively help you in the simulation and flowsheet creation!
This is a "workshop-based" course, there is about 50% theory and about 50% practice!
LINK:
https://www.chemicalengineeringguy.com/courses/aspen-plus-intermediate-course/
The INTERMEDIATE Aspen Plus Course will show you how to model and simulate more complex Processes
Analysis of Unit Operation will help you in order to simulate more complex chemical processes, as well as to analyse and optimize existing ones.
You will learn about:
- Better Flowsheet manipulation
- Hierarchy, Flowsheeting, Sub-flowsheet creation
- Logical Operators / Manipulators
- Understand Property Method Selection and its effects on simulation results
- Study of more rigorous unit operations
- Model Analysis Tools such as sensitivity and optimization
- Reporting Relevant Results Plot relevant data for Heaters, Columns ,Reactors, Pumps
- Temperature Profiles, Concentration Profile, Pump Curves, Heat Curves, etc…
- Up to 3 Case Studies (in-depth analysis)
All theory is backed up by more than 30 Practical Workshops!
At the end of the course you will be able to setup more complex processes, increase your simulation and flow sheeting techniques, run it and debugging, get relevant results and make a deeper analysis of the process for further optimization.
An overview of distillation column design concepts and major design considerations. Explains distillation column design concepts, what you would provide to a professional distillation column designer, and what you can expect back from a distillation system design firm. To speak with an engineer about your distillation column project, call EPIC at 314-207-4250.
Reactor and Catalyst Design
0 INTRODUCTION/PURPOSE
1 SCOPE
2 FIELD OF APPLICATION
3 DEFINITIONS
4 CATALYST DESIGN
4.1 Equivalent Pellet Diameter
4.2 Voidage
4.3 Pellet Density
5 REACTOR DESIGN
6 CATALYST SUPPORT
6.1 Choice of Support
TABLES
1 CATALYST SUPPORT SHAPES
2 SECONDARY REFORMER SPREADSHEET
FIGURES
1 GRAPH OF EFFECTIVENESS v THIELE MODULUS
2 VARIATION OF COSTS WITH CATALYST SIZE
3 VARIATION OF COSTS WITH CATALYST BED VOIDAGE
4 VARIATION OF COSTS WITH VESSEL DIAMETER
Types of Distillation & column internalsBharat Kumar
More:- https://chemicalengineeringworld.com
Distillation is a method of separating the components of a solution which depends upon distribution of the substances between a gas and liquid phase, applied to cases where all components are present in both phases.
* What is distillation ?
* Types of Distillation
* Batch Distillation
* Azeotropic Distillation
* Flooding
* Priming
* Coning
* Weeping
* Dumping
* Packed Column
* Tray column
* Reflux Ratio
* Relative volatility
* Distillation column
Distillation is a method of separating mixtures based on differences in volatility (volatility is the tendency of a substance to vaporize. Volatility is directly related to a substance's vapor pressure.) of components in a boiling liquid mixture. Distillation is a unit operation, or a physical separation process, and not a chemical reaction
CENTRIFUGAL COMPRESSOR SETTLE OUT CONDITIONS TUTORIALVijay Sarathy
Centrifugal Compressors are a preferred choice in gas transportation industry, mainly due to their ability to cater to varying loads. In the event of a compressor shutdown as a planned event, i.e., normal shutdown (NSD), the anti-surge valve is opened to recycle gas from the discharge back to the suction (thereby moving the operating point away from the surge line) and the compressor is tripped via the driver (electric motor or Gas turbine / Steam Turbine). In the case of an unplanned event, i.e., emergency shutdown such as power failure, the compressor trips first followed by the anti-surge valve opening. In doing so, the gas content in the suction side & discharge side mix.
Therefore, settle out conditions is explained as the equilibrium pressure and temperature reached in the compressor piping and equipment volume following a compressor shutdown
FULL COURSE:
https://courses.chemicalengineeringguy.com/p/flash-distillation-in-chemical-process-engineering/
Introduction:
Binary Distillation is one of the most important Mass Transfer Operations used extensively in the Chemical industry.
Understanding the concept behind Gas-Gas, Liquid-Liquid and the Gas-Liquid mass transfer interaction will allow you to understand and model Distillation Columns, Flashes, Batch Distillator, Tray Columns and Packed column, etc...
We will cover:
REVIEW: Of Mass Transfer Basics (Equilibrium VLE Diagrams, Volatility, Raoult's Law, Azeotropes, etc..)
Distillation Theory - Concepts and Principles
Application of Distillation in the Industry
Equipment for Flashing Systems such as Flash Drums
Design & Operation of Flash Drums
Material and Energy Balances for flash systems
Adiabatic and Isothermal Operation
Animations and Software Simulation for Flash Distillation Systems (ASPEN PLUS/HYSYS)
Theory + Solved Problem Approach:
All theory is taught and backed with exercises, solved problems, and proposed problems for homework/individual study.
At the end of the course:
You will be able to understand mass transfer mechanism and processes behind Flash Distillation.
You will be able to continue with Batch Distillation, Fractional Distillation, Continuous Distillation and further courses such as Multi-Component Distillation, Reactive Distillation and Azeotropic Distillation.
About your instructor:
I majored in Chemical Engineering with a minor in Industrial Engineering back in 2012.
I worked as a Process Design/Operation Engineer in INEOS Koln, mostly on the petrochemical area relating to naphtha treating.
There I designed and modeled several processes relating separation of isopentane/pentane mixtures, catalytic reactors and separation processes such as distillation columns, flash separation devices and transportation of tank-trucks of product.
A Better Way to Capture and Manage Cement Lab Datapvisoftware
The design and test of cement slurries are integral parts of every cementing job. Variability between wells can make this process time-consuming and expensive. This white paper talks about how to use an integrated database management application to formulates slurries, calculates required weights for all ingredients, generates weight-up sheets, stores test results, and generates lab reports from anywhere, at any time.
An overview of distillation column design concepts and major design considerations. Explains distillation column design concepts, what you would provide to a professional distillation column designer, and what you can expect back from a distillation system design firm. To speak with an engineer about your distillation column project, call EPIC at 314-207-4250.
Reactor and Catalyst Design
0 INTRODUCTION/PURPOSE
1 SCOPE
2 FIELD OF APPLICATION
3 DEFINITIONS
4 CATALYST DESIGN
4.1 Equivalent Pellet Diameter
4.2 Voidage
4.3 Pellet Density
5 REACTOR DESIGN
6 CATALYST SUPPORT
6.1 Choice of Support
TABLES
1 CATALYST SUPPORT SHAPES
2 SECONDARY REFORMER SPREADSHEET
FIGURES
1 GRAPH OF EFFECTIVENESS v THIELE MODULUS
2 VARIATION OF COSTS WITH CATALYST SIZE
3 VARIATION OF COSTS WITH CATALYST BED VOIDAGE
4 VARIATION OF COSTS WITH VESSEL DIAMETER
Types of Distillation & column internalsBharat Kumar
More:- https://chemicalengineeringworld.com
Distillation is a method of separating the components of a solution which depends upon distribution of the substances between a gas and liquid phase, applied to cases where all components are present in both phases.
* What is distillation ?
* Types of Distillation
* Batch Distillation
* Azeotropic Distillation
* Flooding
* Priming
* Coning
* Weeping
* Dumping
* Packed Column
* Tray column
* Reflux Ratio
* Relative volatility
* Distillation column
Distillation is a method of separating mixtures based on differences in volatility (volatility is the tendency of a substance to vaporize. Volatility is directly related to a substance's vapor pressure.) of components in a boiling liquid mixture. Distillation is a unit operation, or a physical separation process, and not a chemical reaction
CENTRIFUGAL COMPRESSOR SETTLE OUT CONDITIONS TUTORIALVijay Sarathy
Centrifugal Compressors are a preferred choice in gas transportation industry, mainly due to their ability to cater to varying loads. In the event of a compressor shutdown as a planned event, i.e., normal shutdown (NSD), the anti-surge valve is opened to recycle gas from the discharge back to the suction (thereby moving the operating point away from the surge line) and the compressor is tripped via the driver (electric motor or Gas turbine / Steam Turbine). In the case of an unplanned event, i.e., emergency shutdown such as power failure, the compressor trips first followed by the anti-surge valve opening. In doing so, the gas content in the suction side & discharge side mix.
Therefore, settle out conditions is explained as the equilibrium pressure and temperature reached in the compressor piping and equipment volume following a compressor shutdown
FULL COURSE:
https://courses.chemicalengineeringguy.com/p/flash-distillation-in-chemical-process-engineering/
Introduction:
Binary Distillation is one of the most important Mass Transfer Operations used extensively in the Chemical industry.
Understanding the concept behind Gas-Gas, Liquid-Liquid and the Gas-Liquid mass transfer interaction will allow you to understand and model Distillation Columns, Flashes, Batch Distillator, Tray Columns and Packed column, etc...
We will cover:
REVIEW: Of Mass Transfer Basics (Equilibrium VLE Diagrams, Volatility, Raoult's Law, Azeotropes, etc..)
Distillation Theory - Concepts and Principles
Application of Distillation in the Industry
Equipment for Flashing Systems such as Flash Drums
Design & Operation of Flash Drums
Material and Energy Balances for flash systems
Adiabatic and Isothermal Operation
Animations and Software Simulation for Flash Distillation Systems (ASPEN PLUS/HYSYS)
Theory + Solved Problem Approach:
All theory is taught and backed with exercises, solved problems, and proposed problems for homework/individual study.
At the end of the course:
You will be able to understand mass transfer mechanism and processes behind Flash Distillation.
You will be able to continue with Batch Distillation, Fractional Distillation, Continuous Distillation and further courses such as Multi-Component Distillation, Reactive Distillation and Azeotropic Distillation.
About your instructor:
I majored in Chemical Engineering with a minor in Industrial Engineering back in 2012.
I worked as a Process Design/Operation Engineer in INEOS Koln, mostly on the petrochemical area relating to naphtha treating.
There I designed and modeled several processes relating separation of isopentane/pentane mixtures, catalytic reactors and separation processes such as distillation columns, flash separation devices and transportation of tank-trucks of product.
A Better Way to Capture and Manage Cement Lab Datapvisoftware
The design and test of cement slurries are integral parts of every cementing job. Variability between wells can make this process time-consuming and expensive. This white paper talks about how to use an integrated database management application to formulates slurries, calculates required weights for all ingredients, generates weight-up sheets, stores test results, and generates lab reports from anywhere, at any time.
Case Study: Modelling Refinery ProcessesFlex Process
Flex Process modelled most of an oil refinery using Pro/II, giving the client a platform to test modifications off-line, try out new operating regimes, and run different feed stocks, with no risk to the process.
Scale Up Methodology for the Fine Chemical Industry - The Influence of the Mi...Aldo Shusterman
Abstract- In this article the authors, based on the VisiMix Software, the experience of VisiMix users and personal knowledge from more than ten years of experience using VisiMix for API, Fine Chemicals and others, processes simulation, show a Method for Scale Down – Scale Up of Batch – Semi Batch operations built under Hydrodynamics study of the Mixing procedure in the reactor system. The use of the recommended method will offer the user the possibility to achieve the best results during production stage with saving among time and currency, and at the same time increasing the knowledge of the performed process. Several examples at the end of the article show the benefits of the proposed VisiMix Method Loops for Scale Down - Scale Up and Hydrodynamics Considerations.
Scale Up Methodology for the Fine Chemical Industry - The Influence of the Mi...Aldo Shusterman
Chemical production is a result of several chemical reactions and purification steps. Purification steps and processes yield are a direct function of the level of understanding of the reaction system. Reaction quality results have a tremendous impact in separation technology.
Chemical production is frequently performed on stirred vessels that are operated at batch or semi-batch configuration. The choice process configuration is determined at the development stage of the project. Therefore, if the chemical reaction and mixing are not well understood, wrong selections will be adopted in the process development
As a service provider for hit identification, Exquiron needs to offer a state-of-the-art cheminformatics, data analysis and reporting platform to their clients. For historical reasons, this platform was based, until recently, on Accelrys’ PipelinePilot. An effort was started end of 2013 to evaluate and migrate all required workflows to the KNIME platform using the Infocom/ChemAxon nodes. With the help of the ChemAxon consulting team and support from KNIME, complex protocols were successfully migrated to the new environment. The presentation will highlight two specific examples of this effort.
Riccardo Bianco
Topology optimization - Altair suite
tecnologia, scenari e scelte strategiche per la transizione digitale dell'industria manifatturiera
Process Simulation (CE2105) Aston University 1 Dr Amir ADaliaCulbertson719
Process Simulation (CE2105) Aston University
1
Dr Amir Amiri
Coursework
--------------------------------------------------------------------------------------------------------------
Important Notes:
1. The designated coursework enable you to demonstrate your skills in practical
utilisation of the commercial process simulators for process computations. Moreover,
you show your competence in analysing the results.
2. This is a group work in which all members MUST evenly contribute. Peer
assessment will be done to evaluate individual members’ contributions.
3. As the class test will be an individual assessment with similar elements to this work,
your attempts for this commitment certainly equip you with the necessary skills to
properly accomplish that part of the module’s assessment too.
4. The given problem is same for all groups. The contents that can make your work
more distinguishable are, but not limited to, a good literature review, rigorous results,
high quality interpretation, well managed and articulated report, etc. These are highly
recommended as definitely make your work outstanding.
5. Critical thinking and interpretation of the results is required and highly acknowledged.
The more professional/technical interpretation, the higher value. This is an open task
that you can put in creativity and analysis skills. Few examples, but not all, can be
commenting on: How well the process is simulated and if you see any problem how
you can resolve/improve it? What are the assumptions used for simulation simplicity
that might be risky for final results’ accuracy, why? Can these assumptions be
avoided? If so how? How the simulation results improves your understandings about
this case study? How can you use them to suggest process improvement strategies?
Support your answers with examples and results.
6. You should submit your simulation and report files. Maximum page limits are given
for some sections of the report, and are indicated with square brackets.
7. You are welcome to ask your questions by contacting Lecture/tutors. The
response(s) to your question might be posted on the website (BB) to be accessible
by all students.
8. Further guidance will be given in lecture/tutorial times or via the website updates.
Technical tasks and report preparation
Part A: Simulation Principle and VLE [Repot: 4 pages, Marks: 20]
(a) Which Fluid Package/Property Method can be suitable for this simulation? Justify
your answer through Vapour Liquid Equilibrium (VLE) evaluation.
Note: In order to make decision on which Fluid Package/Properly Method is
suitable for this project, you may compare VLE data (such as xy, Txy and Pxy
equilibrium data) attained using 3 to 4 Fluid Package/Property Method and judge
which one(s) are more reliable. Moreover, you may compare the theoretical xy
data (achieved by using Fluid Package/Property Method) with practical data for
the same species and under same conditions (T, P). For practical data you may
refer ...
This is a slideshow / resource / support material of the course.
Get full access (videlectures)
https://www.chemicalengineeringguy.com/courses/aspen-plus-bootcamp-with-12-case-studies/
x-x-x
Requirements
Basic understanding of Plant Design & Operation
Strong Chemical Engineering Fundamentals
Aspen Plus V10 (at least 7.0)
Aspen Plus – Basic Process Modeling (Very Recommended)
Aspen Plus – Intermediate Process Modeling (Somewhat Recommended)
Description
This BOOTCAMP will show you how to model and simulate common industrial Chemical Processes.
It is focused on the “BOOTCAMP” idea, in which you will learn via workshops and case studies, minimizing theory to maximize learning.
You will learn about:
Better Flowsheet manipulation and techniques
Understand Property Method Selection and its effects on simulation results
More than 15 Unit Operations that can be used in any Industry
Model Analysis Tools required for process design
Reporting Relevant Results Plot relevant data
Analysis & Optimization of Chemical Plants
Economic Analysis
Dynamic Simulations
At the end of this Bootcamp, you will be able to model more industrial processes, feel confident when modeling new processes as well as applying what you have learnt to other industries.
An introduction to Augustus, an open source scoring engine for statistical and data mining models based on the Predictive Model Markup Language (PMML). Augustus is able to produce and consume models with 10,000s of segments. Developed by Open Data Group, written in Python, PMML 4.0 compliant and freely available.
EUGM15 - Matthias Negri, Árpád Figyelmesi (Boehringer Ingelheim, ChemAxon):Ch...ChemAxon
Currently, analysis of large patent sets is a tedious and cumbersome work. In order to improve and speed up this process we developed a patent curation-workflow, in which relevant chemical information, such as Markush structures and chemical compound collections (e.g. exemplified structures), are extracted from a patent set and successively enriched with text-mining retrieved data in semi-automatic manner. The outputs of cheminformatic, OCR/OSR and text-mining tools are combined by means of KNIME and the joined data are finally visualized side by side with the original documents using the ChemCurator application. As well as advanced visualization capabilities ChemCurator offers essential functions for validation and manual refining of the automatically extracted chemical information. The created project specific content gives a solid information base of value to any phase of a drug discovery project.
Automation Framework - gFast: generic Framework for Automated Software Testing - QTP Framework
The Most sophisticated frameworks in Automation Testing is Designed with highly experienced Automation Consultants of Heyday Software Solution for all the areas. This makes us to make the impossible things to make possible very fast with our proprietary framework "gFAST".This is a QTP Framework
About gFAST: generic Framework for Automated Software Testing
****************
Developed on Quick Test Professional supporting all Platforms(addin's) with KeyWord Driven Framework.
Key Features
****************
* Better ROI
* Internationalization Support
* Supports Multiple Projects/TestSuites/TestCases
* 24/7 Automatic Regression Tests Running Facility
* Generates Email Reports
* Generates Test Logs
* Simple way to Create Test Cases(without any new QTP Scripts development)
* Easy to Create Test Cases with Test Cases Generator
* Easy way to Create Tests With Excel/Text files facility)
* Easy to Maintain.(Whole Framework will Have 3 QTP script Files -Driver and Two
Controllers and Libraries.)
* Screen Capturing on Error for Each of the Test Cases
* Global Configuration Files
* Multiple Browser windows support
* Easy to build automation for the Projects
Our Frameworks:
Selenium Framework
WATIR RUBY Framework
Silk Framework
Winrunner Framework
QTP Framework
Generic Automation Framework
Perl Automation Framework
An Overview to the most common Industrial Mass Transfer Operations & Process Separation Technologies
Course Description
In this course we will cover the most basic processes involved in Mass Transfer Operations. This is an overview of what type of processes, methods and units are used in the industry. This is mostly an introductory course which will allow you to learn, understand and know the approach towards separation processes involving mass transfer phenomena.
It is an excellent course before any Mass Transfer Process or Unit Operation Course such as Distillations, Extractions, Leaching, Membranes, Absorption, etc...
This course is extremely recommended if you will continue with the following:
Flash Distillation, Simple Distillation, Batch Distillation
Gas Absorption, Desorption & Stripping
Binary Distillation, Fractional Distillation
Scrubbers, Gas Treating
Sprayers / Spray Towers
Bubble Columns / Sparged Vessels
Agitation Vessels
Packed Towers, Tray Towers
Membranes
Liquid Extraction
Dryers / Humidifiers
Adsorbers
Evaporators/Sublimators
Crystallizers
Centrifugations
And many other Separation Technology!
At the end of the Course:
You will be able to understand the mass transfer operations concepts. You will be able to identify Mass Transfer Unit Operations. You will be also able to ensure the type of method of separation technology used.
You will be able to apply this theory in further Unit Operations.
Theory-Based Course
This is a very theoretical course, some calculations and exercises are present, but overall, expect mostly theoretical concepts.
An Overview to the most common Industrial Mass Transfer Operations & Process Separation Technologies
Course Description
In this course we will cover the most basic processes involved in Mass Transfer Operations. This is an overview of what type of processes, methods and units are used in the industry. This is mostly an introductory course which will allow you to learn, understand and know the approach towards separation processes involving mass transfer phenomena.
It is an excellent course before any Mass Transfer Process or Unit Operation Course such as Distillations, Extractions, Leaching, Membranes, Absorption, etc...
This course is extremely recommended if you will continue with the following:
Flash Distillation, Simple Distillation, Batch Distillation
Gas Absorption, Desorption & Stripping
Binary Distillation, Fractional Distillation
Scrubbers, Gas Treating
Sprayers / Spray Towers
Bubble Columns / Sparged Vessels
Agitation Vessels
Packed Towers, Tray Towers
Membranes
Liquid Extraction
Dryers / Humidifiers
Adsorbers
Evaporators/Sublimators
Crystallizers
Centrifugations
And many other Separation Technology!
At the end of the Course:
You will be able to understand the mass transfer operations concepts. You will be able to identify Mass Transfer Unit Operations. You will be also able to ensure the type of method of separation technology used.
You will be able to apply this theory in further Unit Operations.
Theory-Based Course
This is a very theoretical course, some calculations and exercises are present, but overall, expect mostly theoretical concepts.
An Overview to the most common Industrial Mass Transfer Operations & Process Separation Technologies
Course Description
In this course we will cover the most basic processes involved in Mass Transfer Operations. This is an overview of what type of processes, methods and units are used in the industry. This is mostly an introductory course which will allow you to learn, understand and know the approach towards separation processes involving mass transfer phenomena.
It is an excellent course before any Mass Transfer Process or Unit Operation Course such as Distillations, Extractions, Leaching, Membranes, Absorption, etc...
This course is extremely recommended if you will continue with the following:
Flash Distillation, Simple Distillation, Batch Distillation
Gas Absorption, Desorption & Stripping
Binary Distillation, Fractional Distillation
Scrubbers, Gas Treating
Sprayers / Spray Towers
Bubble Columns / Sparged Vessels
Agitation Vessels
Packed Towers, Tray Towers
Membranes
Liquid Extraction
Dryers / Humidifiers
Adsorbers
Evaporators/Sublimators
Crystallizers
Centrifugations
And many other Separation Technology!
At the end of the Course:
You will be able to understand the mass transfer operations concepts. You will be able to identify Mass Transfer Unit Operations. You will be also able to ensure the type of method of separation technology used.
You will be able to apply this theory in further Unit Operations.
Theory-Based Course
This is a very theoretical course, some calculations and exercises are present, but overall, expect mostly theoretical concepts.
An Overview to the most common Industrial Mass Transfer Operations & Process Separation Technologies
Course Description
In this course we will cover the most basic processes involved in Mass Transfer Operations. This is an overview of what type of processes, methods and units are used in the industry. This is mostly an introductory course which will allow you to learn, understand and know the approach towards separation processes involving mass transfer phenomena.
It is an excellent course before any Mass Transfer Process or Unit Operation Course such as Distillations, Extractions, Leaching, Membranes, Absorption, etc...
This course is extremely recommended if you will continue with the following:
Flash Distillation, Simple Distillation, Batch Distillation
Gas Absorption, Desorption & Stripping
Binary Distillation, Fractional Distillation
Scrubbers, Gas Treating
Sprayers / Spray Towers
Bubble Columns / Sparged Vessels
Agitation Vessels
Packed Towers, Tray Towers
Membranes
Liquid Extraction
Dryers / Humidifiers
Adsorbers
Evaporators/Sublimators
Crystallizers
Centrifugations
And many other Separation Technology!
At the end of the Course:
You will be able to understand the mass transfer operations concepts. You will be able to identify Mass Transfer Unit Operations. You will be also able to ensure the type of method of separation technology used.
You will be able to apply this theory in further Unit Operations.
Theory-Based Course
This is a very theoretical course, some calculations and exercises are present, but overall, expect mostly theoretical concepts.
An Overview to the most common Industrial Mass Transfer Operations & Process Separation Technologies
Course Description
In this course we will cover the most basic processes involved in Mass Transfer Operations. This is an overview of what type of processes, methods and units are used in the industry. This is mostly an introductory course which will allow you to learn, understand and know the approach towards separation processes involving mass transfer phenomena.
It is an excellent course before any Mass Transfer Process or Unit Operation Course such as Distillations, Extractions, Leaching, Membranes, Absorption, etc...
This course is extremely recommended if you will continue with the following:
Flash Distillation, Simple Distillation, Batch Distillation
Gas Absorption, Desorption & Stripping
Binary Distillation, Fractional Distillation
Scrubbers, Gas Treating
Sprayers / Spray Towers
Bubble Columns / Sparged Vessels
Agitation Vessels
Packed Towers, Tray Towers
Membranes
Liquid Extraction
Dryers / Humidifiers
Adsorbers
Evaporators/Sublimators
Crystallizers
Centrifugations
And many other Separation Technology!
At the end of the Course:
You will be able to understand the mass transfer operations concepts. You will be able to identify Mass Transfer Unit Operations. You will be also able to ensure the type of method of separation technology used.
You will be able to apply this theory in further Unit Operations.
Theory-Based Course
This is a very theoretical course, some calculations and exercises are present, but overall, expect mostly theoretical concepts.
The Principles required to understand Distillation, Absorption, Stripping, Flashing, Gas Treating, Scrubbing and more!
Introduction:
This course covers all the theory required to understand the basic principles behind Unit Operations that are based on Mass Transfer. Most of these Unit Operations (Equipments) are used in Process Separation Technologies in the Industry.Common examples are Distillation, Absorption and Scrubbing.
This course is required for the following:
Flash Distillation
Gas Absorption & Stripping
Simple Distillation
Batch Distillation
Binary Distillation
Fractional Distillation
Scrubbers
Gas Treating
Sprayers / Spray Towers
Bubble Columns / Sparged Vessels
Agitation Vessels
Packed Towers
Tray Towers
We will cover:
Mass Transfer Basics
Diffusion, Convection
Flux & Fick's Law
The Concept of Equilibrium & Phases
Gibbs Phase Rule
Vapor Pressure
Equilibrium Vapor-Liquid Diagrams (T-xy, P-xy, XY)
Equilibrium Curves
Dew Point, Bubble Point
Volatility (Absolute & Relative)
K-Values
Ideal Cases vs. Real Cases
Henry's Law
Raoult's Law
Deviations of Ideal Cases (Positive and Negative)
Azeotropes
Solubility of Gases in Liquids
Interphase Mass Transfer and its Theories
Two Film Theory
Mass Transfer Coefficients (Overall vs Local)
Getting Vapor-Liquid and Solubility Data
Solved-Problem Approach:
All theory is backed with:
Exercises
Solved problems
Proposed problems
Homework
Case Studies
Individual Study
At the end of the course:
You will be able to understand the mass transfer concepts behind various Unit Operations involving Vapor - Liquid Interaction.
You will be able to apply this theory in further Unit Operations related to Mass Transfer Vapor - Liquid, which is one of the most common interactions found in the industry.
About your instructor:
I majored in Chemical Engineering with a minor in Industrial Engineering back in 2012.
I worked as a Process Design/Operation Engineer in INEOS Koln, mostly on the petrochemical area relating to naphtha treating. There I designed and modeled several processes relating separation of isopentane/pentane mixtures, catalytic reactors and separation processes such as distillation columns, flash separation devices and transportation of tank-trucks of product.
The Principles required to understand Distillation, Absorption, Stripping, Flashing, Gas Treating, Scrubbing and more!
Introduction:
This course covers all the theory required to understand the basic principles behind Unit Operations that are based on Mass Transfer. Most of these Unit Operations (Equipments) are used in Process Separation Technologies in the Industry.Common examples are Distillation, Absorption and Scrubbing.
This course is required for the following:
Flash Distillation
Gas Absorption & Stripping
Simple Distillation
Batch Distillation
Binary Distillation
Fractional Distillation
Scrubbers
Gas Treating
Sprayers / Spray Towers
Bubble Columns / Sparged Vessels
Agitation Vessels
Packed Towers
Tray Towers
We will cover:
Mass Transfer Basics
Diffusion, Convection
Flux & Fick's Law
The Concept of Equilibrium & Phases
Gibbs Phase Rule
Vapor Pressure
Equilibrium Vapor-Liquid Diagrams (T-xy, P-xy, XY)
Equilibrium Curves
Dew Point, Bubble Point
Volatility (Absolute & Relative)
K-Values
Ideal Cases vs. Real Cases
Henry's Law
Raoult's Law
Deviations of Ideal Cases (Positive and Negative)
Azeotropes
Solubility of Gases in Liquids
Interphase Mass Transfer and its Theories
Two Film Theory
Mass Transfer Coefficients (Overall vs Local)
Getting Vapor-Liquid and Solubility Data
Solved-Problem Approach:
All theory is backed with:
Exercises
Solved problems
Proposed problems
Homework
Case Studies
Individual Study
At the end of the course:
You will be able to understand the mass transfer concepts behind various Unit Operations involving Vapor - Liquid Interaction.
You will be able to apply this theory in further Unit Operations related to Mass Transfer Vapor - Liquid, which is one of the most common interactions found in the industry.
About your instructor:
I majored in Chemical Engineering with a minor in Industrial Engineering back in 2012.
I worked as a Process Design/Operation Engineer in INEOS Koln, mostly on the petrochemical area relating to naphtha treating. There I designed and modeled several processes relating separation of isopentane/pentane mixtures, catalytic reactors and separation processes such as distillation columns, flash separation devices and transportation of tank-trucks of product.
The Principles required to understand Distillation, Absorption, Stripping, Flashing, Gas Treating, Scrubbing and more!
Introduction:
This course covers all the theory required to understand the basic principles behind Unit Operations that are based on Mass Transfer. Most of these Unit Operations (Equipments) are used in Process Separation Technologies in the Industry.Common examples are Distillation, Absorption and Scrubbing.
This course is required for the following:
Flash Distillation
Gas Absorption & Stripping
Simple Distillation
Batch Distillation
Binary Distillation
Fractional Distillation
Scrubbers
Gas Treating
Sprayers / Spray Towers
Bubble Columns / Sparged Vessels
Agitation Vessels
Packed Towers
Tray Towers
We will cover:
Mass Transfer Basics
Diffusion, Convection
Flux & Fick's Law
The Concept of Equilibrium & Phases
Gibbs Phase Rule
Vapor Pressure
Equilibrium Vapor-Liquid Diagrams (T-xy, P-xy, XY)
Equilibrium Curves
Dew Point, Bubble Point
Volatility (Absolute & Relative)
K-Values
Ideal Cases vs. Real Cases
Henry's Law
Raoult's Law
Deviations of Ideal Cases (Positive and Negative)
Azeotropes
Solubility of Gases in Liquids
Interphase Mass Transfer and its Theories
Two Film Theory
Mass Transfer Coefficients (Overall vs Local)
Getting Vapor-Liquid and Solubility Data
Solved-Problem Approach:
All theory is backed with:
Exercises
Solved problems
Proposed problems
Homework
Case Studies
Individual Study
At the end of the course:
You will be able to understand the mass transfer concepts behind various Unit Operations involving Vapor - Liquid Interaction.
You will be able to apply this theory in further Unit Operations related to Mass Transfer Vapor - Liquid, which is one of the most common interactions found in the industry.
About your instructor:
I majored in Chemical Engineering with a minor in Industrial Engineering back in 2012.
I worked as a Process Design/Operation Engineer in INEOS Koln, mostly on the petrochemical area relating to naphtha treating. There I designed and modeled several processes relating separation of isopentane/pentane mixtures, catalytic reactors and separation processes such as distillation columns, flash separation devices and transportation of tank-trucks of product.
FULL COURSE:
https://courses.chemicalengineeringguy.com/p/flash-distillation-in-chemical-process-engineering/
Introduction:
Binary Distillation is one of the most important Mass Transfer Operations used extensively in the Chemical industry.
Understanding the concept behind Gas-Gas, Liquid-Liquid and the Gas-Liquid mass transfer interaction will allow you to understand and model Distillation Columns, Flashes, Batch Distillator, Tray Columns and Packed column, etc...
We will cover:
REVIEW: Of Mass Transfer Basics (Equilibrium VLE Diagrams, Volatility, Raoult's Law, Azeotropes, etc..)
Distillation Theory - Concepts and Principles
Application of Distillation in the Industry
Equipment for Flashing Systems such as Flash Drums
Design & Operation of Flash Drums
Material and Energy Balances for flash systems
Adiabatic and Isothermal Operation
Animations and Software Simulation for Flash Distillation Systems (ASPEN PLUS/HYSYS)
Theory + Solved Problem Approach:
All theory is taught and backed with exercises, solved problems, and proposed problems for homework/individual study.
At the end of the course:
You will be able to understand mass transfer mechanism and processes behind Flash Distillation.
You will be able to continue with Batch Distillation, Fractional Distillation, Continuous Distillation and further courses such as Multi-Component Distillation, Reactive Distillation and Azeotropic Distillation.
About your instructor:
I majored in Chemical Engineering with a minor in Industrial Engineering back in 2012.
I worked as a Process Design/Operation Engineer in INEOS Koln, mostly on the petrochemical area relating to naphtha treating.
There I designed and modeled several processes relating separation of isopentane/pentane mixtures, catalytic reactors and separation processes such as distillation columns, flash separation devices and transportation of tank-trucks of product.
COURSE LINK:
https://www.chemicalengineeringguy.com/courses/petroleum-refining/
COURSE DESCRIPTION:
The main scope of the course is to create strong basis and fundamentals regarding the processes in the Petroleum Refining. We take a look to the Oil&Gas Industry briefly and continue directly with the Refining Process. We then make a focus in each individual unit operation in the refinery.
Learn about:
* Oil& Gas Industry
* Difference between Petroleum Refining vs. Petrochemical Industry
* Overview of the most important operations and products
* Market insight (supply/demand) as well as (production/consumption)
* Several Petroleum Refineries around the World
Unit Operations & Processes
* Refining and Fractionation
* Atmospheric Distillation Column
* Vacuum Distillation
* Hydrotreating (Hydrogenation)
* Blending
* Reforming
* Isomerization
* Alkylation
* Steam Cracking
* Fluid Catalytic Cracking
* Gas Sweetening (Hydrodesulfurization)
* Coking
Components:
* Fuel Gas / Natural Gas
* Liquified Petroleum Gases (LPG)
* Propane, Butane
* Sulfur / Hydrogen Sulfide
* Gasoline / Automotive Gas Oil
* Naphtha Cuts (Light/Heavy)
* Kerosene
* Diesel
* Gasoil
* Lubricants
* Vacuum Residues
* Asphalt
* Coke
NOTE: This course is focused for Process Simulation
At the end of the course you will feel confident in the Petroleum Refining Industry. You will know the most common Process & Unit Operations as well as their distribution, production and importance in daily life.
----
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More likes, sharings, suscribers: MORE VIDEOS!
-----
CONTACT ME
Chemical.Engineering.Guy@Gmail.com
www.ChemicalEngineeringGuy.com
http://facebook.com/Chemical.Engineering.Guy
You speak spanish? Visit my spanish channel -www.youtube.com/ChemEngIQA
COURSE LINK:
https://www.chemicalengineeringguy.com/courses/petroleum-refining/
COURSE DESCRIPTION:
The main scope of the course is to create strong basis and fundamentals regarding the processes in the Petroleum Refining. We take a look to the Oil&Gas Industry briefly and continue directly with the Refining Process. We then make a focus in each individual unit operation in the refinery.
Learn about:
* Oil& Gas Industry
* Difference between Petroleum Refining vs. Petrochemical Industry
* Overview of the most important operations and products
* Market insight (supply/demand) as well as (production/consumption)
* Several Petroleum Refineries around the World
Unit Operations & Processes
* Refining and Fractionation
* Atmospheric Distillation Column
* Vacuum Distillation
* Hydrotreating (Hydrogenation)
* Blending
* Reforming
* Isomerization
* Alkylation
* Steam Cracking
* Fluid Catalytic Cracking
* Gas Sweetening (Hydrodesulfurization)
* Coking
Components:
* Fuel Gas / Natural Gas
* Liquified Petroleum Gases (LPG)
* Propane, Butane
* Sulfur / Hydrogen Sulfide
* Gasoline / Automotive Gas Oil
* Naphtha Cuts (Light/Heavy)
* Kerosene
* Diesel
* Gasoil
* Lubricants
* Vacuum Residues
* Asphalt
* Coke
NOTE: This course is focused for Process Simulation
At the end of the course you will feel confident in the Petroleum Refining Industry. You will know the most common Process & Unit Operations as well as their distribution, production and importance in daily life.
----
Please show the love! LIKE, SHARE and SUBSCRIBE!
More likes, sharings, suscribers: MORE VIDEOS!
-----
CONTACT ME
Chemical.Engineering.Guy@Gmail.com
www.ChemicalEngineeringGuy.com
http://facebook.com/Chemical.Engineering.Guy
You speak spanish? Visit my spanish channel -www.youtube.com/ChemEngIQA
COURSE LINK:
https://www.chemicalengineeringguy.com/courses/petrochemicals-an-overview/
Introduction:
The course is mainly about the petrochemical industry. Talks about several chemicals and their chemical routes in order to produce in mass scale the demands of the market.
Learn about:
Petorchemical Industry
Difference between Petroleum Refining vs. Petrochemical Industry
Paraffins, Olefins, Napthenes & Aromatics
Market insight (production, consumption, prices)
Two main Petrochemical Processes: Naphtha Steam Cracking and Fluid Catalytic Cracking
The most important grouping in petrochemical products
Petrochemical physical & chemical properties. Chemical structure, naming, uses, production, etc.
Basic Gases in the industry: Ammonia, Syngas, etc…
C1 Cuts: Methane, Formaldehyde, Methanol, Formic Acid, Urea, Chloromethanes etc…
C2 Cuts: Ethane, Acetylene, Ethylene, Ethylene Dichloride, Vinyl Chloride, Ethylene Oxide, Ethanolamines, Ethanol, Acetaldehyde, Acetic Acid, Ethylene Glycols (MEG, DEG, TEG)
C3 Cuts: Propane, Propylene, Propylene Oxide, Isopropanol, Acetone, Acrylonitrile, Propediene, Allyl chloride, Acrylic acid, Propionic Acid, Propionaldehyde, Propylene Glycol
C4 Cuts: Butanes, Butylenes, Butadiene, Butanols, MTBE (Methyl Tert Butyl Ethers)
C5 cuts: Isoprene, Pentanes, Piperylene, Cyclopentadiene, Dicyclopentadiene, Isoamyl, etc…
Aromatics: Benzene, Toluene, Xylenes (BTX), Cumene, Phenol, Ethyl Benzene, Styrene, Pthalic Anhydride, Nitrobenzene, Aniline, Benzoic Acid, Chlorobenzene, etc…
At the end of the course you will feel confident in how the petrochemical industry is established. You will know the most common petrochemicals as well as their distribution, production and importance in daily life. It will help in your future process simulations by knowing the common and economical chemical pathways.
COURSE LINK:
https://www.chemicalengineeringguy.com/courses/petrochemicals-an-overview/
Introduction:
The course is mainly about the petrochemical industry. Talks about several chemicals and their chemical routes in order to produce in mass scale the demands of the market.
Learn about:
Petorchemical Industry
Difference between Petroleum Refining vs. Petrochemical Industry
Paraffins, Olefins, Napthenes & Aromatics
Market insight (production, consumption, prices)
Two main Petrochemical Processes: Naphtha Steam Cracking and Fluid Catalytic Cracking
The most important grouping in petrochemical products
Petrochemical physical & chemical properties. Chemical structure, naming, uses, production, etc.
Basic Gases in the industry: Ammonia, Syngas, etc…
C1 Cuts: Methane, Formaldehyde, Methanol, Formic Acid, Urea, Chloromethanes etc…
C2 Cuts: Ethane, Acetylene, Ethylene, Ethylene Dichloride, Vinyl Chloride, Ethylene Oxide, Ethanolamines, Ethanol, Acetaldehyde, Acetic Acid, Ethylene Glycols (MEG, DEG, TEG)
C3 Cuts: Propane, Propylene, Propylene Oxide, Isopropanol, Acetone, Acrylonitrile, Propediene, Allyl chloride, Acrylic acid, Propionic Acid, Propionaldehyde, Propylene Glycol
C4 Cuts: Butanes, Butylenes, Butadiene, Butanols, MTBE (Methyl Tert Butyl Ethers)
C5 cuts: Isoprene, Pentanes, Piperylene, Cyclopentadiene, Dicyclopentadiene, Isoamyl, etc…
Aromatics: Benzene, Toluene, Xylenes (BTX), Cumene, Phenol, Ethyl Benzene, Styrene, Pthalic Anhydride, Nitrobenzene, Aniline, Benzoic Acid, Chlorobenzene, etc…
At the end of the course you will feel confident in how the petrochemical industry is established. You will know the most common petrochemicals as well as their distribution, production and importance in daily life. It will help in your future process simulations by knowing the common and economical chemical pathways.
This is a slideshow / resource / support material of the course.
Get full access (videlectures)
https://www.chemicalengineeringguy.com/courses/aspen-plus-bootcamp-with-12-case-studies/
x-x-x
Requirements
Basic understanding of Plant Design & Operation
Strong Chemical Engineering Fundamentals
Aspen Plus V10 (at least 7.0)
Aspen Plus – Basic Process Modeling (Very Recommended)
Aspen Plus – Intermediate Process Modeling (Somewhat Recommended)
Description
This BOOTCAMP will show you how to model and simulate common industrial Chemical Processes.
It is focused on the “BOOTCAMP” idea, in which you will learn via workshops and case studies, minimizing theory to maximize learning.
You will learn about:
Better Flowsheet manipulation and techniques
Understand Property Method Selection and its effects on simulation results
More than 15 Unit Operations that can be used in any Industry
Model Analysis Tools required for process design
Reporting Relevant Results Plot relevant data
Analysis & Optimization of Chemical Plants
Economic Analysis
Dynamic Simulations
At the end of this Bootcamp, you will be able to model more industrial processes, feel confident when modeling new processes as well as applying what you have learnt to other industries.
COURSE LINK:
https://www.chemicalengineeringguy.com/courses/gas-absorption-stripping/
Introduction:
Gas Absorption is one of the very first Mass Transfer Unit Operations studied in early process engineering. It is very important in several Separation Processes, as it is used extensively in the Chemical industry.
Understanding the concept behind Gas-Gas and Gas-Liquid mass transfer interaction will allow you to understand and model Absorbers, Strippers, Scrubbers, Washers, Bubblers, etc…
We will cover:
- REVIEW: Of Mass Transfer Basics required
- GAS-LIQUID interaction in the molecular level, the two-film theory
- ABSORPTION Theory
- Application of Absorption in the Industry
- Counter-current & Co-current Operation
- Several equipment to carry Gas-Liquid Operations
- Bubble, Spray, Packed and Tray Column equipments
- Solvent Selection
- Design & Operation of Packed Towers
- Pressure drop due to packings
- Solvent Selection
- Design & Operation of Tray Columns
- Single Component Absorption
- Single Component Stripping/Desorption
- Diluted and Concentrated Absorption
- Basics: Multicomponent Absorption
- Software Simulation for Absorption/Stripping Operations (ASPEN PLUS/HYSYS)
----
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CONTACT ME
Chemical.Engineering.Guy@Gmail.com
www.ChemicalEngineeringGuy.com
http://facebook.com/Chemical.Engineering.Guy
You speak spanish? Visit my spanish channel -www.youtube.com/ChemEngIQA
COURSE LINK:
https://www.chemicalengineeringguy.com/courses/gas-absorption-stripping/
Introduction:
Gas Absorption is one of the very first Mass Transfer Unit Operations studied in early process engineering. It is very important in several Separation Processes, as it is used extensively in the Chemical industry.
Understanding the concept behind Gas-Gas and Gas-Liquid mass transfer interaction will allow you to understand and model Absorbers, Strippers, Scrubbers, Washers, Bubblers, etc…
We will cover:
- REVIEW: Of Mass Transfer Basics required
- GAS-LIQUID interaction in the molecular level, the two-film theory
- ABSORPTION Theory
- Application of Absorption in the Industry
- Counter-current & Co-current Operation
- Several equipment to carry Gas-Liquid Operations
- Bubble, Spray, Packed and Tray Column equipments
- Solvent Selection
- Design & Operation of Packed Towers
- Pressure drop due to packings
- Solvent Selection
- Design & Operation of Tray Columns
- Single Component Absorption
- Single Component Stripping/Desorption
- Diluted and Concentrated Absorption
- Basics: Multicomponent Absorption
- Software Simulation for Absorption/Stripping Operations (ASPEN PLUS/HYSYS)
----
Please show the love! LIKE, SHARE and SUBSCRIBE!
More likes, sharings, suscribers: MORE VIDEOS!
-----
CONTACT ME
Chemical.Engineering.Guy@Gmail.com
www.ChemicalEngineeringGuy.com
http://facebook.com/Chemical.Engineering.Guy
You speak spanish? Visit my spanish channel -www.youtube.com/ChemEngIQA
The courses, subjects, labs and projects that a student must undergo in order to become a Chemical Engineer.
We divide as follows:
4 blocks:
General Engineering
Theoretical Basis
Unit Operations
Plant Design/Operation
Applied Fluid Dynamics Course. Part 1 - Incompressible Flow
---
This is a Course Overview of Applied Fluid Dynamics Course.
The course is based in Engineering Applications
---
The course is structured in 7 Blocks
AFD1 The Mechanical Energy Equation
AFD2 Pipe, Fittings and Valves
AFD3 Energy Loss due to Friction
AFD4 Flow Measurement Equipment
AFD5 Pumps
AFD6 Incompressible Flow Applications
AFD7 Agitation and Mixing
Visit www.ChemicalEngineeringGuy.com/Courses for more information!
Vaccine management system project report documentation..pdfKamal Acharya
The Division of Vaccine and Immunization is facing increasing difficulty monitoring vaccines and other commodities distribution once they have been distributed from the national stores. With the introduction of new vaccines, more challenges have been anticipated with this additions posing serious threat to the already over strained vaccine supply chain system in Kenya.
CFD Simulation of By-pass Flow in a HRSG module by R&R Consult.pptxR&R Consult
CFD analysis is incredibly effective at solving mysteries and improving the performance of complex systems!
Here's a great example: At a large natural gas-fired power plant, where they use waste heat to generate steam and energy, they were puzzled that their boiler wasn't producing as much steam as expected.
R&R and Tetra Engineering Group Inc. were asked to solve the issue with reduced steam production.
An inspection had shown that a significant amount of hot flue gas was bypassing the boiler tubes, where the heat was supposed to be transferred.
R&R Consult conducted a CFD analysis, which revealed that 6.3% of the flue gas was bypassing the boiler tubes without transferring heat. The analysis also showed that the flue gas was instead being directed along the sides of the boiler and between the modules that were supposed to capture the heat. This was the cause of the reduced performance.
Based on our results, Tetra Engineering installed covering plates to reduce the bypass flow. This improved the boiler's performance and increased electricity production.
It is always satisfying when we can help solve complex challenges like this. Do your systems also need a check-up or optimization? Give us a call!
Work done in cooperation with James Malloy and David Moelling from Tetra Engineering.
More examples of our work https://www.r-r-consult.dk/en/cases-en/
Immunizing Image Classifiers Against Localized Adversary Attacksgerogepatton
This paper addresses the vulnerability of deep learning models, particularly convolutional neural networks
(CNN)s, to adversarial attacks and presents a proactive training technique designed to counter them. We
introduce a novel volumization algorithm, which transforms 2D images into 3D volumetric representations.
When combined with 3D convolution and deep curriculum learning optimization (CLO), itsignificantly improves
the immunity of models against localized universal attacks by up to 40%. We evaluate our proposed approach
using contemporary CNN architectures and the modified Canadian Institute for Advanced Research (CIFAR-10
and CIFAR-100) and ImageNet Large Scale Visual Recognition Challenge (ILSVRC12) datasets, showcasing
accuracy improvements over previous techniques. The results indicate that the combination of the volumetric
input and curriculum learning holds significant promise for mitigating adversarial attacks without necessitating
adversary training.
Welcome to WIPAC Monthly the magazine brought to you by the LinkedIn Group Water Industry Process Automation & Control.
In this month's edition, along with this month's industry news to celebrate the 13 years since the group was created we have articles including
A case study of the used of Advanced Process Control at the Wastewater Treatment works at Lleida in Spain
A look back on an article on smart wastewater networks in order to see how the industry has measured up in the interim around the adoption of Digital Transformation in the Water Industry.
Forklift Classes Overview by Intella PartsIntella Parts
Discover the different forklift classes and their specific applications. Learn how to choose the right forklift for your needs to ensure safety, efficiency, and compliance in your operations.
For more technical information, visit our website https://intellaparts.com
COLLEGE BUS MANAGEMENT SYSTEM PROJECT REPORT.pdfKamal Acharya
The College Bus Management system is completely developed by Visual Basic .NET Version. The application is connect with most secured database language MS SQL Server. The application is develop by using best combination of front-end and back-end languages. The application is totally design like flat user interface. This flat user interface is more attractive user interface in 2017. The application is gives more important to the system functionality. The application is to manage the student’s details, driver’s details, bus details, bus route details, bus fees details and more. The application has only one unit for admin. The admin can manage the entire application. The admin can login into the application by using username and password of the admin. The application is develop for big and small colleges. It is more user friendly for non-computer person. Even they can easily learn how to manage the application within hours. The application is more secure by the admin. The system will give an effective output for the VB.Net and SQL Server given as input to the system. The compiled java program given as input to the system, after scanning the program will generate different reports. The application generates the report for users. The admin can view and download the report of the data. The application deliver the excel format reports. Because, excel formatted reports is very easy to understand the income and expense of the college bus. This application is mainly develop for windows operating system users. In 2017, 73% of people enterprises are using windows operating system. So the application will easily install for all the windows operating system users. The application-developed size is very low. The application consumes very low space in disk. Therefore, the user can allocate very minimum local disk space for this application.
Student information management system project report ii.pdfKamal Acharya
Our project explains about the student management. This project mainly explains the various actions related to student details. This project shows some ease in adding, editing and deleting the student details. It also provides a less time consuming process for viewing, adding, editing and deleting the marks of the students.
Sachpazis:Terzaghi Bearing Capacity Estimation in simple terms with Calculati...Dr.Costas Sachpazis
Terzaghi's soil bearing capacity theory, developed by Karl Terzaghi, is a fundamental principle in geotechnical engineering used to determine the bearing capacity of shallow foundations. This theory provides a method to calculate the ultimate bearing capacity of soil, which is the maximum load per unit area that the soil can support without undergoing shear failure. The Calculation HTML Code included.
2. Thanks for checking out this sample version of the course!
You can check out more content and courses at
Courses - Chemical Engineering Guy
If you have any doubt or inquiry, please send me an e-mail
Contact@chemicalengineeringguy.com
Keep enjoying the course!
www.ChemicalEngineeringGuy.com
3. 1. Course Objectives
2. Introduction to Aspen HYSYS
3. User Interface & Getting Help
4. Environment I: Physical Properties
5. Environment II: Introduction to Flowsheet
6. Basic - Unit Operation Models
7. Basic Reporting of Data and Results
8. Worked Case Studies (I, II and III)
9. Individual Case Study – IV and V
10. Conclusion
www.ChemicalEngineeringGuy.com
7. Makes us easier/faster work
Multiple and Simultaneous Simulations
Different Real-Life Scenarios
Change on raw/feed materials scenario
Pricing and Costs calculation
Raw Materials
Plant Cost
Utilities
How it would behave under different conditions
High/Low Pressure
Humidity Changes
Temperature change (cool/warm days/seasons)
www.ChemicalEngineeringGuy.com
8. Mainly:
Petrochemical
Oil&Gas
Other commodities such as:
Sulfuric acids
Chlorine/Caustic industry
Coatings
Ammonia
Hydrogen Gas
www.ChemicalEngineeringGuy.com
9. Helps us:
Stream flow rates
Compositions of streams
Physical properties such as P, T, v of streams
Unit operation operating conditions; Heat duty, T, P, Electricity, efficiency, Power…
Preliminary equipment sizing ideas/design
Important operational/design concerns/issues
As any Engineering problem, we require to set some data:
Mass & Energy balances
Transport phenomena (momentum, heat, mass)
Equilibrium relationships (Gibbs free energy, entropy, thermos’s law)
www.ChemicalEngineeringGuy.com
10. DESGIN:
Decrease in time
Decrease or experimental requirements
Improves Pilot Plants and Tests
Explore proprietary/experimental process technology
Allows Equipment design
OPERATION:
Helps to improve existing processes
Set possible set of scenarios
Determine best operational input
Safety Analysis (Safety Regulations)
Emissions studies (Environmental)
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11. Excelent for your curriculum as an engineer
Perfect for analytical/numerical minds
Good for debuging and fixing
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12. 1. Course Objectives
2. Introduction to Aspen HYSYS
3. User Interface & Getting Help
4. Physical Properties
5. Introduction to Flowsheet
6. Unit Operation Models
7. Reporting Results
8. Case Studies I, II and III
9. Case Study IV
10. Conclusion
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13. Basic Modeling of Substances & Processes
General Flowsheet Concepts
Basic Requirements to set up a Simulation
Setting the adequate Physical Properties
Flowsheet “manipulation” build, navigate, optimize
Basic – Most Common Unit Operations
Workshop Practice – Hands on!
Basic Reporting of Data and Results (tables, graphs, raw data)
Technical Stuff (extensions, versions, exporting, saving, etc...)
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14. Course Approach
Theory
Practice
More Practice via Workshops
3 Case Studies Fully Developed
1 Final Case Study – Only data is given!
Presentation of Results
Analysis of Data
Conclusions
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15. 1st Day
Getting started
User Interface & Getting Help
Physical Properties
Introduction to Flowsheet
Unit Operation Models
2nd Day
Case Studies I,II and III
4th Day
Case Studies IV
Review and Selfassesment
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16. About Aspen HYSYS ®
Why Aspen HYSYS ®
Aspen HYSYS ® vs. Plus ®
Benefits of simulations
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17. From the website:
“Aspen HYSYS is the energy industry’s leading process simulation software that’s
used by top oil and gas producers, refineries and engineering companies for process
optimization in design and operations.”
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http://www.aspentech.com/products/aspen-hysys/
18. My version V8.8 (May 2015)
Most recent version V10 & 10.1 (Nov 2017)
https://home.aspentech.com/en/v10
Main differences:
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http://origin-www.aspentech.com/products/aspen-hysys/whats-new/
19. V9
Refinery Planning Models are Easier to Update
Improvements to Acid Gas Cleaning
Reduce Risk with Sulfur Recovery Modeling
Get a More Detailed View of Your Distillation Columns
V10
Sequence With Staggered Analysis
Calibrate Models With Plant Data
More Accuracy for Dehydration With CPA
Predict Sulsim Degasser Performance
Improve CDU Modeling Using EO
New Solvents for Acid Gas Cleaning
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http://origin-www.aspentech.com/products/aspen-hysys/whats-new/
20. Aspen Plus
Chemical Industry (H2SO4, Polymers, Coatings, etc.)
Fine Chemistry (chemical reactions)
Non-ideal models (azeotropes, L-V equilibriums, etc.)
Electrolytes
Equation Oriented Mode
Aspen HYSYS
Mainly Petrochemical (upstream/downstream)
Hydrocarbon Oriented (Oil Industry)
Assays (Mixture of petrochemicals, i.e. petroleum)
Refinery Reactors (Catalytic reformer, FCC)
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21. Graphic User Interphase (GUI)
New File, Existing simulations, Exporting, etc…
Extension
Getting Help
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22. These exercises will be mentioned as we do Workshops, Practice Scenarios and Cases
It is pretty straight forward really…
“NEW” – Cases
Existing - Templates
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23. One Aspen HYSYS “Project” may involve:
HYSYS Simulation Case (.hsc)
HYSYS Template; HYSYS Column Template
HYSYS HSP file (.hsp - a snapshot taken during dynamics modeling.)
HYSYS HFL File (.hfl, save a selected part of a flowsheet to a file - import it to another flowsheet.)
HYSYS XML file
HYSYS backup simulations (*.bk0)
HYSYS Compound File (.hscz, zip file of all relevant attached files to the case file)
Fluid package file: *.fpk
Component list file: *.cml
Component List (*.cml)
Fluid Package (*.fpk)
Assay (*.oil)
Column Template (*.col)
Workbook (.wrk)
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24. Prepared “properties/preferences for
the user
Absorber
Sweetener
Reformer
Catalytic Cracker
User defined
“User” SI or English units
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25. Start Page
New, Open
Button (Ribbons) bar
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26. Start Page
New, Open
Button (Ribbons) bar
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27. Start Page
New, Open
Button (Ribbons) bar
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28. 001 Lading Page
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29. Properties Environment – all the steps needed to
fully define the physical property input
Simulation Environment – used to build and run
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Safety and Energy Analysis – Environments are not part of the scope of this course
30. Properties Environment:
Component selection and characterization
Select a property package
Create a Fluid Package
Setup assays and blends via Oil Manager
Create reactions
And more…
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31. Simulation Environment Models, and review/analyze results
Build and specify process flowsheets
Create and run analyses (Case Studies, Optimization, Equipment Sizing,
etc.)
Data Fit to match model data to measured data
Transfer simulation data to other AspenTech products:
Aspen EDR
Flare Network Design & Rating
Process Economic Analyzer
Many others
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32. Properties
Physical Properties
Thermodynamic Properties
Models of Equilibrium
Gas models
Simulation
Flow Sheet
Unit Operations “Blocks”
Stream of Mass/Energy “Lines”
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Setting the Universe
Setting the Process
35. 002 Environements & Physical Properties
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36. In this course and other users (recommended)
Aspen Tech directly, groups or direct contact
By yourself (Help Menu and other manuals)
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37. Direct Contact
Via Udemy Private Messages/Discussion boards
Via e-mail
Contact@ChemicalEngineeringGuy.com
Chemical.Engineering.Guy@gmail.com
Forums & Groups
http://www.egpet.net/
http://www.cheresources.com/
http://www.eng-tips.com/threadminder.cfm?pid=137
Facebook Group:
https://www.facebook.com/groups/aspenplushysysforum/ (250)
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38. LinkedIn
Aspen Plus Users
Official Aspen Plus User Community Official Aspen Plus User Community (869 users)
Official Aspen HYSYS User Community (9,000 users)
Aspen HYSYS® Dynamics UsersPrivate Group (1,800 users)
Aspen Tech
http://support.aspentech.com ***You got to be registered as a valid Aspen License User(s)
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39. Help Topics
Select Help Topics from the Help button on the ribbon
to launch online help:
Contents: Browse through the documentation and Help article by topic, including Reference
Manuals
Index: Search for help on a specific topic using the index entries
Search: Search for a help on a topic that includes any word or words
F1 Help
With the cursor in the desired field, press the <F1> function key to bring up help for field
and/or sheet
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40. Using Aspen Help Bar/Button
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Help Bar/Help Button
44. 003 Getting Help - Help Button
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45. 1. Set Physical Properties (Physical Environment)
2. Set Process in Flowsheet
Mass Streams (T,P, mass flow, fractions, etc.)
Heat/Work Explicit Duties (Q,W)
Unit Operations
Mass transfer (Distillation, flashes, etc.)
Heat Transfer (Heat Exchanger, single/double HEX, etc.)
Momentum Transfer (mixing, transportation of fluids, pumps, compressors, etc.)
Reaction Kinetic (Reactor, Equilibrium Reactors, Stoichiometric Reactors, etc.)
3. Run Simulation
4. Expect no Errors
If no errors Check solution in Reports
If there are errors Check type of error, try to fix if needed, re-run simulation
5. Analysis of Results, Sensitivity Analysis, Optimization, etc…
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49. Aspen HYSYS Library Components
Sufficient for the majority of hydrocarbon-based processes
Search by component name, alternate name, or formula
Can filter search based on component family
Aspen Properties Database
Represents many component databanks covering a variety of process industries
NIST Pure component data and NIST Thermo Data Engine (TDE) for improved data fitting and
estimation
Hypothetical Components***
Minimum data entry is one property (NBP, MW, density…)
Select desired methods to estimate unknown properties
Option to either define a single hypo or create a Hypo Group
More Advanced Courses –
Unique for HYSYS!
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50. Specification
Database (HYSYS)
Component (from Databases)*
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* At least 1 is required
All other Databases/Options/Hypo are
studied in other advanced courses
51. Property Package Selection
Plenty of packages!
Each has its specification…
Typically, you will know which Package to Apply
Recommended Method Asistant OR USE HELP BUTTON
SERACH: Aspen HYSYS Property Package Selection Assistant
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52. Choose the Method Assistant
Actually, it pop-ups a Help Site
Then, choose either Help button or
Method assistant
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54. Start by selecting one of the following options:
Specify component type
Select the type of component system:
Chemical system
Hydrocarbon system
Special (water only, amines, Sour water, electrolyte, aromatics only, thiols and hydrocarbons)
Specify process type
Select the type of process or application:
Chemical
Electrolyte
Environmental
Oil and Gas processing
Mineral and metallurgical
Petrochemical
Power
Refining
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Example:
Process
Gas dehydration
Use Peng-Robinson
CPA
Glycol Package.
55. www.ChemicalEngineeringGuy.com
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56. www.ChemicalEngineeringGuy.com
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57. www.ChemicalEngineeringGuy.com
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58. www.ChemicalEngineeringGuy.com
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59. IT also recommends!
Water + Ethanol
Choose Peng Robinson
NOT RECOMENDED
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61. STATEMENT
A stream of 10 kg/h of ethanol is added to another stream of 50 kg/h of water.
Both at 25°C and 1 atm.
They are mixed.
There is no heat exchange with the surroundings (no heat gain/loss)
The mixtures it then transported to ta Heater which increases Temp. from 25°C to 77°C
The streams go out in a single pipe
Verify new compositions
Physical Properties ONLY!
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62. Fill up all required Physical Properties
Components Water, Ethanol
Fluid Package NRTL
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63. You are ready to run the property simulation
Aspen HYSYS will run
Properties
Fluid Packages
Calculation
If any compound has a modeling problem, you will receive errors (non-typical)
You are ready to work in the Simulation Environment!
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64. 004 Filling Physical Properties Environment
Try different Packages
Show “not recommended”
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65. 1. Set Physical Properties (Physical Environment)
2. Set Process in Flowsheet
Mass Streams (T,P, mass flow, fractions, etc.)
Heat/Work Explicit Duties (Q,W)
Unit Operations
Mass transfer (Distillation, flashes, etc.)
Heat Transfer (Heat Exchanger, single/double HEX, etc.)
Momentum Transfer (mixing, transportation of fluids, pumps, compressors, etc.)
Reaction Kinetic (Reactor, Equilibrium Reactors, Stoichiometric Reactors, etc.)
3. Run Simulation
4. Expect no Errors
If no errors Check solution in Reports
If there are errors Check type of error, try to fix if needed, re-run simulation
5. Analysis of Results, Sensitivity Analysis, Optimization, etc…
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DONE
66. 1. Set Physical Properties (Physical Environment)
2. Set Process in Flowsheet
Mass Streams (T,P, mass flow, fractions, etc.)
Heat/Work Explicit Duties (Q,W)
Unit Operations
Mass transfer (Distillation, flashes, etc.)
Heat Transfer (Heat Exchanger, single/double HEX, etc.)
Momentum Transfer (mixing, transportation of fluids, pumps, compressors, etc.)
Reaction Kinetic (Reactor, Equilibrium Reactors, Stoichiometric Reactors, etc.)
3. Run Simulation
4. Expect no Errors
If no errors Check solution in Reports
If there are errors Check type of error, try to fix if needed, re-run simulation
5. Analysis of Results, Sensitivity Analysis, Optimization, etc…
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67. Set/Build System/Process
Must have 0 Degrees of Freedom (System is “Fixed”)
Set Input Data in Streams (energy, work and materials)
Set Properties to Unit Operations (Blocks)
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80. Right click on any PFD object to:
Rotate or flip the icon
Format the label
Hide the object
Display a summary table
Change the icon
Cut/copy/export the object
Right click on the PFD background to:
Add a Workbook table
Change label variable (i.e. show stream pressure instead of name)
Reveal hidden objects
Paste/import an object
81. Mass Streams Mainly
All inlet to process (raw material)
Intermediate streams (intermediate material)
All outlet to process (final products & by-products)
Heat and Work only if Required (direct Duty)
500 kJ must be applied
Loss of Heat due to cold temperature is 1054 KJ/s
14 HP Shaft Power Requirement
Pump has 12 BHP
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82. This is seen in Section – UNIT OPERATIONS – specifically
In the meantime, just add simple Unit Operations
Mixer
Heater
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83. STATEMENT
A stream of 10 kg/h of ethanol is added to another stream of 50/h kg of water.
Both at 25°C and 1 atm.
They are mixed.
There is no heat exchange with the surroundings (no heat gain/loss)
The mixtures it then transported to ta Heater which increases Temp. from 25°C to 77°C
The streams go out in a single pipe
Verify new compositions
Fill up the Simulation Environment!
Streams must be specified
Unit Operations must be specified
Connections must be specified
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85. Mixing unit…
Heater unit…
No need to add specifications/properties…
JUST add the unit and connect to the streams
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87. 006 Filling the Simulation Environement
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88. 1. Set Physical Properties (Physical Environment)
2. Set Process in Flowsheet
Mass Streams (T,P, mass flow, fractions, etc.)
Heat/Work Explicit Duties (Q,W)
Unit Operations
Mass transfer (Distillation, flashes, etc.)
Heat Transfer (Heat Exchanger, single/double HEX, etc.)
Momentum Transfer (mixing, transportation of fluids, pumps, compressors, etc.)
Reaction Kinetic (Reactor, Equilibrium Reactors, Stoichiometric Reactors, etc.)
3. Run Simulation
4. Expect no Errors
If no errors Check solution in Reports
If there are errors Check type of error, try to fix if needed, re-run simulation
5. Analysis of Results, Sensitivity Analysis, Optimization, etc…
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89. No!
Perfect!
Continue with Results and Analysis
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90. 1. Set Physical Properties (Physical Environment)
2. Set Process in Flowsheet
Mass Streams (T,P, mass flow, fractions, etc.)
Heat/Work Explicit Duties (Q,W)
Unit Operations
Mass transfer (Distillation, flashes, etc.)
Heat Transfer (Heat Exchanger, single/double HEX, etc.)
Momentum Transfer (mixing, transportation of fluids, pumps, compressors, etc.)
Reaction Kinetic (Reactor, Equilibrium Reactors, Stoichiometric Reactors, etc.)
3. Run Simulation
4. Expect no Errors
If no errors Check solution in Reports
If there are errors Check type of error, try to fix if needed, re-run simulation
5. Analysis of Results, Sensitivity Analysis, Optimization, etc…
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91. Solutions
Product Composition = 0.9275
Stream Results
Mixture: 60 kg/h; T = 25°C
Product: 60 kg/h; T = 77°C
Heat Duty = 1.274E04 kJ/h
*** More info in Section 7. Flowsheet Results
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92. STATEMENT
A stream of 10 kg/h of ethanol is added to another stream of 50/h kg of water.
Both at 25°C and 1 atm.
They are mixed.
There is no heat exchange with the surroundings (no heat gain/loss)
The mixtures it then transported to ta Heater which increases Temp. from 25°C to 77°C
The streams go out in a single pipe
Verify new compositions
Verify the new composition and conditions (T,P,Duty)
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93. www.ChemicalEngineeringGuy.com
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94. www.ChemicalEngineeringGuy.com
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95. 006 Environment Conclusion
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96. Basic
Common
Columns
Advanced
Upstream
Refining
Dynamics
Custom
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* Not Relevant in this Course
100. Or use F-12 Key
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101. 008 Introduction to Unit Operations
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104. Required
One streams inlet (Q,W,M)
One stream outlet (Q,W,M)
Useful for
In-pipe blending (T-shape)
Mixing tanks (Adiabatic Only)
Static Mixers
Pressure drop may be added
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Either Mass, Q or W!
105. Required
One streams inlet (MASS)
One stream outlet (MASS)
Useful for
Stream separation
Pressure drop may be added
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Just Mass, NOT: Q or W!
106. 008 Mixers & Tees
Mixer:
Stream 1 – inlet, P = 1 atm, T = 25°C (25% Benzene, 50% Toluene, 25% Xylene). FlowRate =
100 kg/h
Stream 2 – inlet, P = 1 atm, T = 25°C (50% Cyclohexane, 50% n-Hexane). FlowRate = 150
kg/h
Stream 3 – outlet, (Resulting T, P, Composition, Flow Rate)
Tees
Stream 3 – inlet,
Stream 4 – outlet, 33% of original Flow rate?
Stream 5 – outlet, 67% of original Flow rate?
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FP: PR
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107.
108. Typical Unit operation models:
Cooler
LNG
Exchanger
Fired Heater
Air Cooler
Heat
Exchanger
Heater
109. Models only one side of an exchanger
Can be used to:
Heating or cooling
Condense or evaporate
Designed for simple heat transfer calculations
preliminary design
Precursor
Not a detailed design!
110. Used to model heat transfer between two process streams (H/C)
Aspen EDR rigorous modeling software can be accessed through
Heat Exchanger (Advanced/specific Courses)
Select preferred Heat Exchanger Model depending on required
simulation detail
Recommended:
calculate heat transfer coefficient
pressure drop
exchanger geometry
111. LNG Exchanger
can be used to represent heat transfer between multiple hot and
cold streams
Air Cooler
Uses air to cool or heat a process stream to some specified
condition
Fired Heater
Performs heat and material balances on furnace-type fired heater
*Not part of this course!
113. 009 Heater and Cooler
Heater
Stream 1 – inlet, T = 25°C, P = 1 atm; (50% water, 50% ethanol) FlowRate = 10 kg/min
Q = ?, dP ?
Stream 2 – outlet, T = 50°C, P = 0.93 atm, Composition?, FlowRate?
Cooler
Stream 2 – inlet, T = 50°C, P = 0.93 atm
Q = 20000 kJ/h off of Duty , dP = 0.03
Stream 2 – outlet, T = ? , P = atm, Composition? FlowRate?
FP: PRSV
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010 – Flash Drum
Stream inlet
Composition: 15% ethane, 20% propane, 60% i-butane, 5% n-butane
T = 32°F, P = 50 psia, FlowRate = 100 lb/h
Find Vapor FlowRate and composition
Find Liquid FlowRate and composition
Fluid Package:
Peng Robinson
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119. 4 standard column templates are available
Distillation Column
Refluxed Absorber
Absorber
Reboiled Absorber
Three phase distillation column
Liquid-liquid extractor
Rate based column
Custom column templates
Shortcut distillation
120. Distillation column: contains a tray section, condenser and reboiler
With a total/full reflux condenser DOF = 2
With a partial condenser DOF = 3
Refluxed absorber: contains a tray section and a condenser
With a total/full reflux condenser DOF = 1
With a partial condenser DOF = 2
Absorber: contains only a tray section
DOF (Degrees of Freedom ) = 0
no additional operating specification can be given
Reboiled absorber: contains a tray section and a reboiler
DOF = 1, one additional operating specification has to be given
121. Distillation column: contains a tray section, condenser and reboiler
With a total/full reflux condenser DOF = 2
With a partial condenser DOF = 3
Refluxed absorber: contains a tray section and a condenser
With a total/full reflux condenser DOF = 1
With a partial condenser DOF = 2
Absorber: contains only a tray section
DOF (Degrees of Freedom ) = 0
no additional operating specification can be given
Reboiled absorber: contains a tray section and a reboiler
DOF = 1, one additional operating specification has to be given
122. The “Distillation” Template looks like this:
Condenser
Reflux flow
Distillate
Boilups
Bottoms
Total Stages
Feed (1)
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Parent Environment Column Environment
123. Distillation Column
Requires plenty of input!
It is done in 5 Steps
You must run/reset simulation
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Parent Environment
124. Step 1: Connections (Mass and Energy streams, specifications, trays)
Step 2: Reboiler Configuration (Type and Reboiler Selection)
Step 3: Pressure Profile
Condenser/Reboiler Pressures.
Pressure drop in column and each equipment is optional
Step 4: Optional Estimates
Optional aids in convergence
Temperature of Equipment
Step 5: Specifications (Reflux and/or FlowRate)
RUN!
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130. 013 - Columns
Input Data:
Inlet Stream (F)
T = 60°C , P = 106 kPa,
FlowRate = 100 kmol/h, 40% Benzene, 60%Toluene (molar)
Distillate = D, Bottoms = B
Heat Duty Compressor Qc; Heat Duty Reboiler Qr
Stages: N = 10, Feed = 5
Condenser: Total, P = 101 kPa, Reflux = 2.0 molar
Reboiler: Default HYSYS, P = 111 kPa
Distillate Rate = 40 kmol/h
Change of No. Trays from N = 10, to N = 20
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132. Moving fluids
Pressure change mainly
Friction generation Temperature
Contains piping-specific unit ops
Pipe Segment (pressure loss)
Various fittings
Decrease Pressure Valves, expander
Increase Pressure Compressor/Pump
Transport Fluids Pipings
• Advanced Gas Gathering Examples
133. Used to increase pressure in a liquid
Move a liquid
Recover loss of pressure
Increase Pressure
Inputs are
Inlet stream (mass)
Outlet stream (mass)
Inlet stream (Work)
You can assign 1 fluid package for it!
dP, Pressure Ratio, Adiabatic Eff.
Pump Curves, NPSH Curves, Efficiency Curves
134. 014 – Pumps
Input data:
Inlet Stream
T = 25°C, P = 1 atm
Pure water
P final Required = 10 atm
Final Data:
Outlet Temperature
Workload required (KW, HP)
135. Used to increase pressure in a gas
Move a gas
Recover loss of pressure
Increase Pressure
Inputs are
Inlet stream (mass)
Outlet stream (mass)
Inlet stream (Work)
dP, Pressure Ratio, Adiabatic/Polytropic Eff.
136. 015 – Compressor
Input data:
Inlet Stream
Enriched Oxygen Air (34% Nitrox)
T = 30°C, P = 14.7 psia
P final Required = 3000 psig
% efficiency = 65%
Final Data:
Outlet Temperature
Workload required (KW, HP)
138. You must add and specify the type of reaction
Types:
Conversion
Equilibrium
Kinetic
Rate
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139. C + O2 = CO2
C + ½ O2 = CO
H2O = H2 + O2
H2O = 2H + O
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140. It is based on Conversion of a reactant (X)
Requires Reaction
Stoichiometry!
All other calculations are based upon this
Enthalpy of reaction
Final T, P
Requires exact Stoichiometry
Final Composition
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141. Requires Reaction
Stoichiometry!
Forward-Reverse reactions
Based on activity coefficients Keq
Keq given
Keq calculated via Gibbs Free energy
Keq tabulated
All other calculations are based upon this
Reaction extent
Temperature, Pressure changes
Final Composition
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142. 014 - Reactors (Conversion)
Reactors Specs
Conversion if 95%
Adiabatic (Q= 0)
Methane Combustion (15% excess oxidant) CH4 + 2O2 = CO2 + 2H2O
Via pure oxygen
Inlet Fuel = 100 mol of CH4
Inlet Oxidant = 230 mol of O2
Final T
Final flowrates + composition
Via air (21% O2, 79% N2)
Inlet Fuel = 100 mol of CH4
Inlet Oxidant = 1095 mol of Air (230 mol of O2, 865 mol of N2)
Final T
Final flowrates + composition
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146. All info regarding:
Material Streams
Compositions
Energy Streams
Unit Operations
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147. Workbook “Menu”
Save/Export Workbook
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148. Streams
Mass
Energy
Compositions
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149. Export to Excel!
Engineers love Excel!
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150. Printable Version of Workbooks
Add multiple datasheet of interest
Can be formatted and fitted to many page-sizes
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151. Now you know how to model the most Basic Unit Operations of Aspen HYSYS ®
You can model plenty of Common Processes by now!
Get to practice on the Workshops!
Case Study I, II, III Apply all the knowledge into one process, step by step.
Case Study IV Apply your knowledge by your own. Compare final results with the template
result!
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152. VIDEOS
The Workbook
Exporting Data to Excel
Creating Reports
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153. Explain how to use the workshop
1. Statement
Read it carefully, write down all important data. Find data that might be useful
2. Building the Flowsheet
Build the diagram accordingly, “after”, “before” and “then”, “pre” are pretty important words
3. Data Input
Name Streams logically. Add all substances, fractions, masses that are required.
Add Blocks, name them accordingly to their functions. Add all data needed
4. Run Simulation
5. Results
Go to results; review there are no warnings, errors.
6. Analysis&Conclusion
Make an analysis and make your final conclusion
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155. 1. Statement
2. Building the Flowsheet
3. Data Input
Streams
Blocks
4. Run
5. Results & Reporting
6. Analysis
7. Conclusion
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156. We have a stream containing 15% ethane, 20% propane, 60% i-butane and 5% n-butane at T =
50°F and P = 1 atm. Flow rate is 100 kg/h
It will be compressed to P = 50 psia and cooled down to 32°F.
The chiller has a pressure loss of 10 kPa.
The resulting mixture must be splitted into liquid (valuable product for our client) and a gas
(must be burnt with air)
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157. A) How much mass is lost in flare?
B) How much product is recovered?
C) Specifications of liquid product.
C) Compressor Workload
D) Chiller Heat Duty requirements
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164. A) How much mass is lost in flare?
B) How much product is recovered?
C) Specifications of liquid product.
C) Compressor Workload
D) Chiller Heat Duty requirements
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165. 016 Case Study I – Solvent
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167. Sour water stripper Sample Aspen HYSYS
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168. 1. Statement
2. Building the diagram
3. Data Input
Streams
Blocks
4. Run Simulation
5. Results & Reporting
6. Analysis
7. Conclusion
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169. Cumene is typically produced from a benzene + propylene reaction at very low pressures
(vaccum).
The plant feedstock is 50%-50% B/P. It is about 80 lbmol/h.
It comes from a pump which delivers it at T = 220 F and P = 36 psia
The reactor is typically operated with a recycle stream of all volatile material in the
reactor’s outlet.
Final Reactors Temerature is not know but tt is imperative to cool down at T = 130 F
The sepation is carried out with a flash drum at P = 1 atm (for final product storage).
The flash is operated adiabatically
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170. Find:
Reactor’s Operation Temperature
Heat Duty of Cooler
Split Fraction of Separator
Flow rate of Recycle
Flow rate of product
Mol fraction of Cumene in product
Try it without recycle! (Same questions)
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172. Feed:
P = 36 psi
T = 220 F
F = 80 lbmol/h
X = 0.5 Benzene; 0.5 Propylene
Reactor
This is typically done via the reaction of Benzene + Propylene in a Reactor
Use Rstoic
Reaction is 1:1 1
90% conversión with respect to Benzene
Adibatical; i.e. Q = 0
P = 0 atm
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173. Cooler:
T cool = 130 F
P final = -0.1 psia (i.e. vacuum)
Flash Drum
P = 1 atm (final product)
Adiabatical, i.e. Q = 0
Recycle vapors
Liquids go to final product
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174. Run the simulation!
Debug required?
Warnings
Errors?
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175. Products:
X fraction of Cumene
Mol Flow of Product Stream
Recycle Mol flow stream
Blocks:
Reactor Temperature
Coolers Heat Duty
Recycle Split Fraction
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180. 1. Statement
2. Building the diagram
3. Data Input
Streams
Blocks
4. Run Simulation
5. Results & Reporting
6. Analysis
7. Conclusion
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181. You are in charge of mixing, transport and compressing a mixture of gases used for a furnace
application. They are stored in separate tanks reservoirs.
The furnace operates at 5 bar so we need to mix all gases and then transport it to the
furnace.
Due to friction losses; we have a 1.5 bar pressure loss from the mixer to the furnace.
Compression is required.
The methane gas (essentially natural gas) is stored at 15 bar; ethane gas is at 2 bar and the
propane gas is already at 5 bar.
Compressors work with the given isentropic and mechanical efficiencies
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182. Find:
Compressor 1 - Duty
Compressor 2 - Duty
Final Product Gas Composition
Initial Temperature of mixture
Final Temperature
Try it with a final heater!
Try it with a cooler before the Compressions!
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184. Feed:
Methane – 30°C, 15 bar, 155 kg/h
Ethane – 25°C, 2 bar, 200 kg/h
Propane – 35°C, 5 bar, 120 kg/h
COMP1
Compressor
Isentropic
Discharge P = 5 bar
95% Isentropic Efficiency
88% Mechanical Efficiency
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185. Mixer:
P = 5 bar
Friction loss:
Model as Valve
Pressure Drop = 1.5 bar
Adiabatic Flash
COMP2
Compressor
Isentropic
Discharge P = 5 bar
90% Isentropic Efficiency
85% Mechanical Efficiency
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186. Run the simulation!
Debug required?
Warnings
Errors?
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187. Products:
Mass Fraction of all gases
Final Temperature
Final Pressure
Blocks:
Compressor 1 Workload
Compressor 2 Workload
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188. Tempearture increases:
What if, cooling before any compression?
Workload of heater/cooler vs. Compression
Energy optimization?
$$??
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189. 018 Case Study III - Gas Compression
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191. Now its time to practice alone!
Make your simulation
Compare with the results shown in the Course’s Workshop
If there are warning/error shown
Try troubleshooting
Send your results to me! @CHEMENG (any contact given before)
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193. Now its time to practice alone!
Make your simulation
Compare with the results shown in the Course’s Workshop
If there are warning/error shown
Try troubleshooting
Send your results to me! @CHEMENG (any contact given before)
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194. WRITTEN STATEMENT
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Thanks for checking out this sample version of the course!
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If you have any doubt or inquiry, please send me an e-mail
Contact@chemicalengineeringguy.com
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201. PERSONAL VIDEO!
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202. Finally! You made it!
By now you should be able to know:
General Flowsheet Concepts
Basic Requirements to set up a Simulation
Setting the adequate Physical Properties
Flowsheet “manipulation”
Major and Common Unit Operations
Workshop Practice
Reporting Results (Tables)
Technical Stuff (extensions, versions, exporting, saving, etc...)
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203. 1. Course Objectives
2. Introduction to Aspen Plus
3. User Interface & Getting Help
4. Physical Properties
5. Introduction to Flowsheet
6. Unit Operation Models
7. Reporting Results
8. Case Studies I, II and III
9. Case Study IV
10. Conclusion
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204. Continue with the next course Intermediate and Advance!
Other specific courses
Dynamic
Oil & Gas applications
Petroleum Assay
Economic Analysis
You will learn…
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205. Files:
Creating and editing templates
Reviewing samples/exercises/previous projects
More on extensions and backup, onedrive
Exchange, Support and Live chats
Continuous training
Physical Properties Environment:
More on Methods and how to use them
More on substances and YOUR own substances/assays
Graphs + Substances Properties charts
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206. Dymamics/Transient State
Steady vs. Unsteady/Transient states
Batch modeling
Economy Environment
Safety Environment
Energy Environment
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207. Unit Operations:
Rigourous/Detailed Heat Exchange
Rigourous/Detailed Distillation; Petroleum Refinery
Batch Separation (Columns)
Reactor Engineering
Modeling for mechanisms and kinetic theory
Extractions
Logical Operators
Hydraulics (pressure drops, equipments)
Review of Unit Operations with Solids
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208. Running Simulations
More on Debugging, warnings, and fixing Errors
Degrees of Freedom
Process simplification
Reporting Results
Excel export/import
Sensitivity Analysis
Charts, Graphs, Tables
Programming tools
Set
Recycle
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209. It was awesome to share the course!
Hope you like it
Please leave a Review! It really helps other students to find the course easier
If I get students; I get motivated to do MORE material XD
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211. Try “Aspen Plus – Basic Process Modeling” Course with a 90% off discount
Coupon Code = 90OFF-HYSYS-STUDENT
Link
https://www.udemy.com/aspen-plus-process-modeling/?couponCode=90OFF-HYSYS-STUDENT
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Editor's Notes
When explaining this concept to customers compare to MS Outlook – mail and calendar
When explaining this concept to customers compare to MS Outlook – mail and calendar
When explaining this concept to customers compare to MS Outlook – mail and calendar