VLE Data - Selection and Use
0 INTRODUCTION/PURPOSE
1 SCOPE
2 FIELD OF APPLICATION
3 DEFINITIONS
4 DIAGRAMMATIC REPRESENTATION OF IDEAL
AND NON-IDEAL SYSTEMS
4.1 Ideal Mixtures
4.2 Non-Ideal Mixtures
5 REVIEW OF VLE MODELS
5.1 Ideal Behavior in Both Phases
5.2 Liquid Phase Non-Idealities
5.3 High Pressure Systems
5.4 Special Models
6 SETTING UP A VLE MODEL
6.1 Define Problem
6.2 Select Data
6.3 Select Correlation(s)
6.4 Produce Model
7 AVOIDING PITFALLS
7.1 Experimental Data is Better than Estimates
7.2 Check Validity of Fitted Model
7.3 Check Limitations of Estimation Methods
7.4 Know Your System
7.5 Appreciate Errors and Effects
7.6 If in Doubt – Ask
8 A CASE STUDY
8.1 The Problem
8.2 The System
8.3 Data Available
8.4 Selected Correlation
8.5 Simulation
8.6 Selection of Model
9 RECOMMENDED READING
10 VLE EXPERTS IN GBHE
APPENDICES
A USE OF EXTENDED ANTOINE EQUATION
B USE OF WILSON EQUATION
C USEFUL METHODS OF ESTIMATING
D EQUATIONS OF STATE FOR VLE CALCULATIONS
TABLES
1 SUMMARY OF VLE METHODS
2 LIST OF USEFUL REFERENCES
FIGURES
1 VAPOR-LIQUID EQUILIBRIUM - IDEAL SOLUTION
BEHAVIOR
2 VAPOR-LIQUID EQUILIBRIUM - A GENERALISED
Y-X DIAGRAM
3 VAPOR-LIQUID EQUILIBRIUM - MINIMUM BOILING
AZEOTROPE
4 VAPOR-LIQUID EQUILIBRIUM - MAXIMUM BOILING
AZEOTROPE
5 VAPOR-LIQUID EQUILIBRIUM - MINIMUM BOILING
AZEOTROPE -TWO LIQUID PHASES
6 SENSITIVITY TO ERROR IN VLE DATA (BASED ON FENSKE EQUATION)
7(a) FITTING WILSON 'A' VALUES TO VLE DATA - CASE A
7(b) FITTING WILSON 'A' VALUES TO VLE DATA - CASE B
7(c) FITTING WILSON 'A' VALUES TO VLE DATA - CASE C
In this project we basically studied scope of this project, its feasibility and market assessment, raw material availability, different routes to produce Syngas and their comparison, process selection and its complete description, its P&ID, and environmental consideration.
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.
Get full Course here:
www.ChemicalEngineeringGuy.com/Courses
The BASIC Aspen HYSYS Course will show you how to model and simulate Processes (From Petrochemical, to Ammonia Synthesis and Polymerisation).
Analysis of Unit Operation will help you in order to optimise the Chemical Plant.
This is helpful for students, teachers, engineers and researchers in the area of R&D and Plant Design/Operation.
The course is didactic, with a lot of applied theory and Workshops/Study cases.
At the end of the course you will be able to setup a simulation, run it, get results and more important, analysis of the process for further optimization.
Chemical Engineers
Process Engineers
Students related to engineering fields
Teachers willing to learn more about process simulation
Petrochemical Engineers
VLE Data - Selection and Use
0 INTRODUCTION/PURPOSE
1 SCOPE
2 FIELD OF APPLICATION
3 DEFINITIONS
4 DIAGRAMMATIC REPRESENTATION OF IDEAL
AND NON-IDEAL SYSTEMS
4.1 Ideal Mixtures
4.2 Non-Ideal Mixtures
5 REVIEW OF VLE MODELS
5.1 Ideal Behavior in Both Phases
5.2 Liquid Phase Non-Idealities
5.3 High Pressure Systems
5.4 Special Models
6 SETTING UP A VLE MODEL
6.1 Define Problem
6.2 Select Data
6.3 Select Correlation(s)
6.4 Produce Model
7 AVOIDING PITFALLS
7.1 Experimental Data is Better than Estimates
7.2 Check Validity of Fitted Model
7.3 Check Limitations of Estimation Methods
7.4 Know Your System
7.5 Appreciate Errors and Effects
7.6 If in Doubt – Ask
8 A CASE STUDY
8.1 The Problem
8.2 The System
8.3 Data Available
8.4 Selected Correlation
8.5 Simulation
8.6 Selection of Model
9 RECOMMENDED READING
10 VLE EXPERTS IN GBHE
APPENDICES
A USE OF EXTENDED ANTOINE EQUATION
B USE OF WILSON EQUATION
C USEFUL METHODS OF ESTIMATING
D EQUATIONS OF STATE FOR VLE CALCULATIONS
TABLES
1 SUMMARY OF VLE METHODS
2 LIST OF USEFUL REFERENCES
FIGURES
1 VAPOR-LIQUID EQUILIBRIUM - IDEAL SOLUTION
BEHAVIOR
2 VAPOR-LIQUID EQUILIBRIUM - A GENERALISED
Y-X DIAGRAM
3 VAPOR-LIQUID EQUILIBRIUM - MINIMUM BOILING
AZEOTROPE
4 VAPOR-LIQUID EQUILIBRIUM - MAXIMUM BOILING
AZEOTROPE
5 VAPOR-LIQUID EQUILIBRIUM - MINIMUM BOILING
AZEOTROPE -TWO LIQUID PHASES
6 SENSITIVITY TO ERROR IN VLE DATA (BASED ON FENSKE EQUATION)
7(a) FITTING WILSON 'A' VALUES TO VLE DATA - CASE A
7(b) FITTING WILSON 'A' VALUES TO VLE DATA - CASE B
7(c) FITTING WILSON 'A' VALUES TO VLE DATA - CASE C
In this project we basically studied scope of this project, its feasibility and market assessment, raw material availability, different routes to produce Syngas and their comparison, process selection and its complete description, its P&ID, and environmental consideration.
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.
Get full Course here:
www.ChemicalEngineeringGuy.com/Courses
The BASIC Aspen HYSYS Course will show you how to model and simulate Processes (From Petrochemical, to Ammonia Synthesis and Polymerisation).
Analysis of Unit Operation will help you in order to optimise the Chemical Plant.
This is helpful for students, teachers, engineers and researchers in the area of R&D and Plant Design/Operation.
The course is didactic, with a lot of applied theory and Workshops/Study cases.
At the end of the course you will be able to setup a simulation, run it, get results and more important, analysis of the process for further optimization.
Chemical Engineers
Process Engineers
Students related to engineering fields
Teachers willing to learn more about process simulation
Petrochemical Engineers
Slides for the eLearning course Separation and purification processes in biorefineries (https://open-learn.xamk.fi) in IMPRESS project.
Section: Distillation
Subject: 1.1 Vapor Liquid Equilibrium
Simulation of Chemical Rectors - Introduction to chemical process simulators ...CAChemE
Learn the fundamentals of any chemical process simulator software by means of free and open source software as an alternative to Aspen, Aspen HYSYS, etc. We will be using DWSIM (open source and free) and COCO Simulator (freeware) for this course. Material is licensed under CC BY-NC-SA 3.0.
You can find more learning material for chemical engineers in http://CAChemE.org
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.
Slides for the eLearning course Separation and purification processes in biorefineries (https://open-learn.xamk.fi) in IMPRESS project (https://www.spire2030.eu/impress).
Section: Distillation
Subject: 0.2 Introduction to distillation.
Reactive distillation
LeChatelier’s law
conventional process
mtbe production using Reactive distillation
various contact devices used for Reactive distillation
advantages of Reactive distillation
disadvantages of Reactive distillation
application of Reactive distillation
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!
Episode 3 : Production of Synthesis Gas by Steam Methane ReformingSAJJAD KHUDHUR ABBAS
Episode 3 : Production of Synthesis Gas by Steam Methane Reforming
History of Synthesis Gas
In 1780, Felice Fontana discovered that combustible gas develops if water vapor is passed over carbon at temperatures over 500 °C. This CO and H2 containing gas was called water gas and mainly used for lighting purposes in the19th century.
As of the beginning of the 20th century, H2/CO-mixtures were used for syntheses of hydrocarbons and then, as a consequence, also called synthesis gas.
Haber and Bosch discovered the synthesis of ammonia from H2 and N2 in 1910 and the first industrial ammonia synthesis plant was commissioned in 1913.
The production of liquid hydrocarbons and oxygenates from syngas conversion over iron catalysts was discovered in 1923 by Fischer and Tropsch.
Much of the syngas conversion processes were being developed in Germany during the first and second world wars at a time when natural resources were becoming scare and alternative routes for hydrogen production, ammonia synthesis, and transportation fuels were a necessity.
In 1943/44, this was applied for large-scale production of artificial fuels from synthesis gas in Germany.
Fixed Bed Reactor Scale-up Checklist
The purpose of this checklist is to identify the stages and potential problems associated with the scale up of fixed bed reactors from the drawing board to the full scale plant, and to determine how they should be checked.
The checking can be done using various methods. These are:
• Literature data.
• Lab testing.
• Calculation.
• Modeling.
• Semi-tech testing.
• Piloting or Sidestream testing.
Identifying the stages that need to be addressed for a particular catalyst/reactor development will help in estimating the time needed for the development of the reactor
Slides for the eLearning course Separation and purification processes in biorefineries (https://open-learn.xamk.fi) in IMPRESS project.
Section: Distillation
Subject: 1.1 Vapor Liquid Equilibrium
Simulation of Chemical Rectors - Introduction to chemical process simulators ...CAChemE
Learn the fundamentals of any chemical process simulator software by means of free and open source software as an alternative to Aspen, Aspen HYSYS, etc. We will be using DWSIM (open source and free) and COCO Simulator (freeware) for this course. Material is licensed under CC BY-NC-SA 3.0.
You can find more learning material for chemical engineers in http://CAChemE.org
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.
Slides for the eLearning course Separation and purification processes in biorefineries (https://open-learn.xamk.fi) in IMPRESS project (https://www.spire2030.eu/impress).
Section: Distillation
Subject: 0.2 Introduction to distillation.
Reactive distillation
LeChatelier’s law
conventional process
mtbe production using Reactive distillation
various contact devices used for Reactive distillation
advantages of Reactive distillation
disadvantages of Reactive distillation
application of Reactive distillation
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!
Episode 3 : Production of Synthesis Gas by Steam Methane ReformingSAJJAD KHUDHUR ABBAS
Episode 3 : Production of Synthesis Gas by Steam Methane Reforming
History of Synthesis Gas
In 1780, Felice Fontana discovered that combustible gas develops if water vapor is passed over carbon at temperatures over 500 °C. This CO and H2 containing gas was called water gas and mainly used for lighting purposes in the19th century.
As of the beginning of the 20th century, H2/CO-mixtures were used for syntheses of hydrocarbons and then, as a consequence, also called synthesis gas.
Haber and Bosch discovered the synthesis of ammonia from H2 and N2 in 1910 and the first industrial ammonia synthesis plant was commissioned in 1913.
The production of liquid hydrocarbons and oxygenates from syngas conversion over iron catalysts was discovered in 1923 by Fischer and Tropsch.
Much of the syngas conversion processes were being developed in Germany during the first and second world wars at a time when natural resources were becoming scare and alternative routes for hydrogen production, ammonia synthesis, and transportation fuels were a necessity.
In 1943/44, this was applied for large-scale production of artificial fuels from synthesis gas in Germany.
Fixed Bed Reactor Scale-up Checklist
The purpose of this checklist is to identify the stages and potential problems associated with the scale up of fixed bed reactors from the drawing board to the full scale plant, and to determine how they should be checked.
The checking can be done using various methods. These are:
• Literature data.
• Lab testing.
• Calculation.
• Modeling.
• Semi-tech testing.
• Piloting or Sidestream testing.
Identifying the stages that need to be addressed for a particular catalyst/reactor development will help in estimating the time needed for the development of the reactor
Voltage Stability Improvement by Reactive Power Rescheduling Incorporating P...IJMER
In this paper, reactive power rescheduling is done to keep the voltage stable. Due to system
disturbances the active as well as reactive power flows changes. Generators being always connected to the
system reactive power rescheduling of generators can be effectively done. Therefore it is selected as the
suitable method for voltage control. The voltage and reactive power management is studied from the
generator’s point of view to minimize generator reactive power loss. To reduce the reactive losses
optimization procedure is used. The simulations are done using MATLAB.
The study is aimed to determine the measurement of sensor tool made in Model Real Time Hybrid LFG-PV-Genset by finding the correction factor produced at TPA Bontang City, East Borneo. The research was conducted by using ampere clammeter, variable voltage regulator, thermometer, odalog7000 series. The calculation results show that the calibration test of Model Real Time Hybrid LFG-PV-Genset from MQ4 sensor data that has been designed capable of having errors of 1,91% and the LM35 temperature sensor is capable of monitoring tempertures of 30°C to 120°C and has an error value of 0,519°C. ZMPT 101B voltage sensor has a linear output change to input changes and has an average error of 1.499V. While the current sensor SCT 013 has an aerage error value of 0,0022A CO2.
Quantitative structure - activity relationship (QSAR)
Why QSAR?
costs – 800M$ to bring a new drug to market
Patent life time is limited (generic drugs)
Synthesis / Purification of compounds is expensive and time consume-able
It is like find a needle in the haystack
QSAR helps for focusing most promising drug candidates
QSAR is a mathematical relationship between a “biological activity of a molecular system” and its “geometric and chemical characteristics”.
Such relationships holds – Equations can be drawn up- some confidence
to which should be Fit to the target
QSAR what actually do?
IDENTIFY AND QUANTIFY the Physico-chemical properties effect on Drug’s Biological activity
Aims
To relate the biological activity of a series of compounds to their physicochemical parameters in a quantitative fashion using a mathematical formula
Requirements
Quantitative measurements for biological and physicochemical properties
Physicochemical Properties
Hydrophobicity of the molecule
Hydrophobicity of substituents
Electronic properties of substituents
Steric properties of substituents
QSAR equations are only applicable to compounds in the same structural class (e.g. ethers)
However, log Po is similar for anaesthetics of different structural classes (ca. 2.3)
Structures with log P ca. 2.3 enter the CNS easily
(e.g. potent barbiturates have a log P of approximately 2.0)
Can alter log P value of drugs away from 2.0 to avoid CNS side effects
Physical properties are measured for the molecule as a whole
Properties are calculated using computer software
No experimental constants or measurements are involved
Properties are known as ‘Fields’
Steric field - defines the size and shape of the molecule
Electrostatic field - defines electron rich/poor regions of molecule
Hydrophobic properties are relatively unimportant
No reliance on experimental values
Can be applied to molecules with unusual substituents
Not restricted to molecules of the same structural class
Predictive capability
Comparative molecular field analysis (CoMFA) - Tripos
Build each molecule using modelling software
Identify the active conformation for each molecule
Identify the pharmacophore
THANKING YOU
Design of Controllers for Continuous Stirred Tank ReactorIAES-IJPEDS
The objective of the project is to design various controllers for temperature control in Continuous Stirred Tank Reactor (CSTR) systems. Initially Zeigler-Nichols, modified Zeigler-Nichols, Tyreus-Luyben, Shen-Yu and IMC based method of tuned Proportional Integral (PI) controller is designed and comparisons are made with Fuzzy Logic Controller. Simulations are carried out and responses are obtained for the above controllers. Maximum peak overshoot, Settling time, Rise time, ISE, IAE are chosen as performance index. From the analysis it is found that the Fuzzy Logic Controller is a promising controller than the conventional controllers.
Explore the innovative world of trenchless pipe repair with our comprehensive guide, "The Benefits and Techniques of Trenchless Pipe Repair." This document delves into the modern methods of repairing underground pipes without the need for extensive excavation, highlighting the numerous advantages and the latest techniques used in the industry.
Learn about the cost savings, reduced environmental impact, and minimal disruption associated with trenchless technology. Discover detailed explanations of popular techniques such as pipe bursting, cured-in-place pipe (CIPP) lining, and directional drilling. Understand how these methods can be applied to various types of infrastructure, from residential plumbing to large-scale municipal systems.
Ideal for homeowners, contractors, engineers, and anyone interested in modern plumbing solutions, this guide provides valuable insights into why trenchless pipe repair is becoming the preferred choice for pipe rehabilitation. Stay informed about the latest advancements and best practices in the field.
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.
Overview of the fundamental roles in Hydropower generation and the components involved in wider Electrical Engineering.
This paper presents the design and construction of hydroelectric dams from the hydrologist’s survey of the valley before construction, all aspects and involved disciplines, fluid dynamics, structural engineering, generation and mains frequency regulation to the very transmission of power through the network in the United Kingdom.
Author: Robbie Edward Sayers
Collaborators and co editors: Charlie Sims and Connor Healey.
(C) 2024 Robbie E. Sayers
Water scarcity is the lack of fresh water resources to meet the standard water demand. There are two type of water scarcity. One is physical. The other is economic water scarcity.
Hybrid optimization of pumped hydro system and solar- Engr. Abdul-Azeez.pdffxintegritypublishin
Advancements in technology unveil a myriad of electrical and electronic breakthroughs geared towards efficiently harnessing limited resources to meet human energy demands. The optimization of hybrid solar PV panels and pumped hydro energy supply systems plays a pivotal role in utilizing natural resources effectively. This initiative not only benefits humanity but also fosters environmental sustainability. The study investigated the design optimization of these hybrid systems, focusing on understanding solar radiation patterns, identifying geographical influences on solar radiation, formulating a mathematical model for system optimization, and determining the optimal configuration of PV panels and pumped hydro storage. Through a comparative analysis approach and eight weeks of data collection, the study addressed key research questions related to solar radiation patterns and optimal system design. The findings highlighted regions with heightened solar radiation levels, showcasing substantial potential for power generation and emphasizing the system's efficiency. Optimizing system design significantly boosted power generation, promoted renewable energy utilization, and enhanced energy storage capacity. The study underscored the benefits of optimizing hybrid solar PV panels and pumped hydro energy supply systems for sustainable energy usage. Optimizing the design of solar PV panels and pumped hydro energy supply systems as examined across diverse climatic conditions in a developing country, not only enhances power generation but also improves the integration of renewable energy sources and boosts energy storage capacities, particularly beneficial for less economically prosperous regions. Additionally, the study provides valuable insights for advancing energy research in economically viable areas. Recommendations included conducting site-specific assessments, utilizing advanced modeling tools, implementing regular maintenance protocols, and enhancing communication among system components.
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Saudi Arabia stands as a titan in the global energy landscape, renowned for its abundant oil and gas resources. It's the largest exporter of petroleum and holds some of the world's most significant reserves. Let's delve into the top 10 oil and gas projects shaping Saudi Arabia's energy future in 2024.
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.
3. Introduction
ASPEN plus
To optimize throughput, quality and energy use
Includes databases
Pure component data
Phase equilibrium data
for various electrolytes, solids and polymers.
5. Introduction
The Pitzer model was developed as an improvement upon an
earlier model proposed by Guggenheim (1935, 1955).
The earlier model worked well at low electrolyte concentrations,
but contained discrepancies at higher concentrations (>0.1M).
The Pitzer model resolved these discrepancies, without resorting
to excessive arrays of higher-order terms.
It cannot be used for mixed solvent electrolyte systems.
6. The PITZER property method is based on an aqueous electrolyte
activity coefficient model.
It has no overlap with other activity coefficient models.
It can accurately calculate the behavior of aqueous electrolyte
solutions with or without molecular solutes up to 6 molal ionic
strength.
Many interaction parameters from regression of experimental data
are included in databanks and data packages
Do not use this model if a non-aqueous solvent exists.
7. You can model the solubility of supercritical gases using Henry’s
law.
Heats of mixing are calculated using the Pitzer model.
The Redlich-Kwong-Soave equation of state is used for the vapor
phase fugacity coefficient, all other vapor phase properties are
assumed ideal. Redlich-Kwong-Soave cannot model association
behavior in the vapor phase (for example, carboxylic acids or HF).
For carboxylic acids, choose a non-electrolyte activity coefficient
model with Hayden-O’Connell or Nothnagel; for HF choose
ENRTL-HF or WILS-HF.
8. Mixture Types
You can use the Pitzer model for any aqueous electrolyte
solution up to 6M ionic strength, not showing association in
the vapor phase.
Range
Vapor phase fugacities are described accurately up to
medium pressures.
Interaction parameters should be fitted in the range of
operation.
12. Pitzer Activity Coefficient
Model
The Pitzer model in the Aspen Physical Property System involves user
supplied parameters that are used in the calculation of binary and ternary
parameters for the electrolyte system.
Five elements (P1 through P5) account for the temperature dependencies
of parameters β (0), β (1),β (2), β (3), cϕ , and θ .
These parameters follow the temperature dependency relation:
13.
14. Application of the Pitzer Model to Aqueous Strong
Electrolyte Systems
Pitzer modified his basic
equation to make it more
useful for data correlation
of aqueous strong
electrolytes.
He defined a set of more
directly observable
parameters to represent
combinations of the
second and third virial
coefficients.
The cation-anion parameters B and C are characteristic for an aqueous single electrolyte system.
These parameters can be determined by the properties of pure (apparent) electrolytes.
B is expressed as a function of β(0) and β(1), β(2) and β(3)
The modified Pitzer equation is:
Subscripts c, c′ , and a, a′ denote cations and anions of the
solution.
B, C, θ, and Ψ are interaction parameters.
f(I) is an electrostatic term as a function of ionic strength.
16. Cubic Equations of State in the Aspen Physical Property
System
Peng-Robinson based
• Peng-Robinson
• Peng-Robinson
• Peng-Robinson-MHV2
• Peng-Robinson-WS
Redlich-Kwong(-Soave) based
• Redlich-Kwong Standard
• Standard Redlich-Kwong-Soave
• Redlich-Kwong-Soave
• Redlich-Kwong-ASPEN
• Schwartzentruber-Renon
• Redlich-Kwong-Soave-MHV2
• Predictive SRK
• Redlich-Kwong-Soave-WS
17. • Based on the Redlich – Kwong - Aspen equation-
of-state model.
• An extension of Redlich - Kwong-Soave.
• Similar to RKS-BM.(Redlich-Kwong-Soave
(RKS) cubic equation of state with Boston-
Mathias alpha function for all thermodynamic
properties.)
RK-ASPEN
Property Method
Introduction
18. Equations
Equation-of-state is the basis for the RK-ASPEN property method.
The equation is the same as Redlich-Kwong-Soave:
A quadratic mixing rule is maintained for:
An interaction parameter is introduced in the mixing rule for:
19. For ai an extra polar parameter is used:
The interaction parameters are temperature-dependent:
For best results, binary parameters kij must be determined from phase-equilibrium
data regression, such as VLE data.
20. RK-ASPEN allows temperature-dependent binary parameters.
Mixture Types
Range
• You can use the RK-ASPEN property method for mixtures of nonpolar and
slightly polar compounds, in combination with light gases.
• It is especially suited for combinations of small and large molecules, such
as nitrogen with n-Decane, or hydrogen-rich systems.
RK-ASPEN - Equation-of-state model.
• You can use the RK-ASPEN property method up to high temperatures
and pressures.
• You can expect reasonable results at any condition, but results are least
accurate close to the critical point.
21. Parameters Required for the RK-ASPEN
Property Method
Thermodynamic
Properties
Models Parameter
Requirements
Fugacity coefficient,
Density
Redlich-Kwong-Aspen TCRKA, PCRKA,
OMEGARKA UFGRP,
GMUFR, GMUFQ
Enthalpy, Entropy,
Gibbs energy
Ideal heat capacity,
Redlich-Kwong-Aspen
(CPIG or CPIGDP) and
TCRKA, PCRKA,
OMEGARKA
Vapor and liquid mixture
22.
23. RK-ASPEN
Applies to nonpolar and polar components such
as alcohols and water
Mixture Types
Combinations of small and large molecules, such
as nitrogen with n-Decane, or hydrogen-rich
systems.
Temperature-dependent binary parameters
Range
High temperatures and pressures.
RKS-BM
Nonpolar or mildly polar mixtures
1. Requires polar Parameters
2. Regression of experimental vapor pressure
data using DRS.
Mixture Types
Hydrocarbons and light gases, such as carbon
dioxide, hydrogen sulfide, and hydrogen
Range
All temperatures and pressures
24. Application
It can be used for hydrocarbon processing applications.
It is also used for more polar components and mixtures of
hydrocarbons, and for light gases at medium to high
pressures.