The document describes a distillation system with multiple units including a feed preheater, reboiler, distillation column, bottom product cooler, top product cooler, and condenser. It provides material and energy balances for the system, including flow rates, temperatures, heat duties, and phases of the streams at each component.
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
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!
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
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.
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
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!
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
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.
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
Episode 47 : CONCEPTUAL DESIGN OF CHEMICAL PROCESSES
Chemical process design is the application of chemical engineering knowledge (chemical, physical and/or biological transformations of raw materials) into products and economics in the conceiving a chemical process plant to profitably manufacture chemicals in a reliable and safe manner without unduly affecting adversely the environment and society
Chemical process plants are by nature large capital investment projects that
are expensive to build and operate
have very long life times and
manufacture specific chemicals
Chemical process plants must be designed well to avoid large financial losses over long periods of times due to inefficient processes/poor operations
SAJJAD KHUDHUR ABBAS
Ceo , Founder & Head of SHacademy
Chemical Engineering , Al-Muthanna University, Iraq
Oil & Gas Safety and Health Professional – OSHACADEMY
Trainer of Trainers (TOT) - Canadian Center of Human
Development
Estimation of Pressure Drop in Pipe Systems
0 INTRODUCTION/PURPOSE
1 SCOPE
2 FIELD OF APPLICATION
3 DEFINITIONS
3.1 units
4 SOURCES OF DATA
5 BASIC CONCEPTS
5.1 Equation for Pressure Change in a Flowing
Fluid
5.2 Static and Stagnation Pressures
5.3 Sonic Flow
6 INCOMPRESSIBLE FLOW IN PIPES OF CONSTANT
CROSS-SECTION
6.1 Straight Circular Pipes
6.2 Ducts of Non-circular Cross-section
6.3 Coils
6.4 General Equation for Incompressible Flow
in Pipes of Constant Cross-section
7 COMPRESSIBLE FLOW IN PIPES OF CONSTANT
CROSS-SECTION
7.1 Isothermal Flow
7.2 Adiabatic Flow
7.3 Estimation of Pressure Drop for Adiabatic
Flow in Pipes of Constant Cross-section
7.4 Ratio of Isothermal to Adiabatic Pressure Drop
8 FLOW IN PIPE FITTINGS
8.1 Incompressible Flow
8.2 Compressible Flow
9 FLOW IN BENDS
9.1 Incompressible Flow in Bends
9.2 Compressible Flow in Bends
10 CHANGES IN CROSS-SECTIONAL AREA
9.1 Incompressible Flow
9.2 Compressible Flow
11 ORIFICES, NOZZLES AND VENTURIS
11.1 Incompressible Flow through an Orifice
11.2 Compressible Flow through an Orifice or Nozzle
11.3 Venturi Choke Tubes
12 VALVES
12.1 General
12.2 Incompressible Flow in Valves
12.2 Compressible Flow in Valves
13 COMBINING AND DIVIDING FLOW
9.1 Incompressible Flow
9.2 Compressible Flow
14 COMPUTER PROGRAMS FOR FLUID FLOW
15 NOMENCLATURE
16 REFERENCES
APPENDICES
A BASIC THERMODYNAMICS
B COMPRESSIBLE FLOW THROUGH ORIFICES
C THE ‘TWO-K’ METHOD FOR FITTING PRESSURE LOSS
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
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
Shortcut Methods of Distillation Design
0 INTRODUCTION/PURPOSE
1 SCOPE
2 ESTIMATIONOF PLATEAGE AND REFLUX
REQUIREMENTS
2.1 Generalized Procedure for Nmin and Rmin
2.2 Equation based Procedure for Nmin and Rmin
3 PREDICTION OF OVERALL PLATE EFFICIENCY
4 SIZING OF MAIN PLANT ITEMS
4.1 Column Diameter
4.2 Surface Area of Condensers and Reboilers
FIGURES
1 NON-IDEAL EQUILIBRIUM CURVE
2 AT A GLANCE CHART BASED ON FENSKE,
UNDERWOOD
3 PLATE EFFICIENCY CORRELATION OF O’CONNEL
Batch Distillation
1 SCOPE
2 FIELD OF APPLICATION
3 DEFINITIONS
4 BACKGROUND TO THE DESIGN
4.1 General
4.2 Choice of batch/continuous operation
4.3 Boiling point curve and cut policy
4.4 Method of design
4.5 Scope of calculations required for design
5 SIMPLE BATCH DISTILLATION
6 FRACTIONAL BATCH DISTILLATION
6.1 General
6.2 Approximate methods
6.3 Rigorous design - use of a computer model
6.4 Other factors influencing the design
6.4.1 Occupation
6.4.2 Choice of Batch Rectification or Stripping
6.4.3 Batch size
6.4.4 Initial estimate of cut policy
6.4.5 Liquid Holdup
6.4.6 Total reflux operation and heating-up time
6.4.7 Column operating pressure
6.5 Optimum Design of the Batch Still
6.6 Special design problems
7 GENERAL ASPECTS OF EQUIPMENT DESIGN
7.1 Kettle reboilers
7.2 Column Internals
7.3 Condensers and reflux split boxes
8 PROCESS CONTROL AND INSTRUMENTATION IN
BATCH DISTILLATION
9 MECHANICAL DESIGN FEATURES
10 BIBLIOGRAPHY
APPENDICES
A McCABE - THIELE METHOD - TYPICAL EXAMPLE
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
Episode 47 : CONCEPTUAL DESIGN OF CHEMICAL PROCESSES
Chemical process design is the application of chemical engineering knowledge (chemical, physical and/or biological transformations of raw materials) into products and economics in the conceiving a chemical process plant to profitably manufacture chemicals in a reliable and safe manner without unduly affecting adversely the environment and society
Chemical process plants are by nature large capital investment projects that
are expensive to build and operate
have very long life times and
manufacture specific chemicals
Chemical process plants must be designed well to avoid large financial losses over long periods of times due to inefficient processes/poor operations
SAJJAD KHUDHUR ABBAS
Ceo , Founder & Head of SHacademy
Chemical Engineering , Al-Muthanna University, Iraq
Oil & Gas Safety and Health Professional – OSHACADEMY
Trainer of Trainers (TOT) - Canadian Center of Human
Development
Estimation of Pressure Drop in Pipe Systems
0 INTRODUCTION/PURPOSE
1 SCOPE
2 FIELD OF APPLICATION
3 DEFINITIONS
3.1 units
4 SOURCES OF DATA
5 BASIC CONCEPTS
5.1 Equation for Pressure Change in a Flowing
Fluid
5.2 Static and Stagnation Pressures
5.3 Sonic Flow
6 INCOMPRESSIBLE FLOW IN PIPES OF CONSTANT
CROSS-SECTION
6.1 Straight Circular Pipes
6.2 Ducts of Non-circular Cross-section
6.3 Coils
6.4 General Equation for Incompressible Flow
in Pipes of Constant Cross-section
7 COMPRESSIBLE FLOW IN PIPES OF CONSTANT
CROSS-SECTION
7.1 Isothermal Flow
7.2 Adiabatic Flow
7.3 Estimation of Pressure Drop for Adiabatic
Flow in Pipes of Constant Cross-section
7.4 Ratio of Isothermal to Adiabatic Pressure Drop
8 FLOW IN PIPE FITTINGS
8.1 Incompressible Flow
8.2 Compressible Flow
9 FLOW IN BENDS
9.1 Incompressible Flow in Bends
9.2 Compressible Flow in Bends
10 CHANGES IN CROSS-SECTIONAL AREA
9.1 Incompressible Flow
9.2 Compressible Flow
11 ORIFICES, NOZZLES AND VENTURIS
11.1 Incompressible Flow through an Orifice
11.2 Compressible Flow through an Orifice or Nozzle
11.3 Venturi Choke Tubes
12 VALVES
12.1 General
12.2 Incompressible Flow in Valves
12.2 Compressible Flow in Valves
13 COMBINING AND DIVIDING FLOW
9.1 Incompressible Flow
9.2 Compressible Flow
14 COMPUTER PROGRAMS FOR FLUID FLOW
15 NOMENCLATURE
16 REFERENCES
APPENDICES
A BASIC THERMODYNAMICS
B COMPRESSIBLE FLOW THROUGH ORIFICES
C THE ‘TWO-K’ METHOD FOR FITTING PRESSURE LOSS
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
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
Shortcut Methods of Distillation Design
0 INTRODUCTION/PURPOSE
1 SCOPE
2 ESTIMATIONOF PLATEAGE AND REFLUX
REQUIREMENTS
2.1 Generalized Procedure for Nmin and Rmin
2.2 Equation based Procedure for Nmin and Rmin
3 PREDICTION OF OVERALL PLATE EFFICIENCY
4 SIZING OF MAIN PLANT ITEMS
4.1 Column Diameter
4.2 Surface Area of Condensers and Reboilers
FIGURES
1 NON-IDEAL EQUILIBRIUM CURVE
2 AT A GLANCE CHART BASED ON FENSKE,
UNDERWOOD
3 PLATE EFFICIENCY CORRELATION OF O’CONNEL
Batch Distillation
1 SCOPE
2 FIELD OF APPLICATION
3 DEFINITIONS
4 BACKGROUND TO THE DESIGN
4.1 General
4.2 Choice of batch/continuous operation
4.3 Boiling point curve and cut policy
4.4 Method of design
4.5 Scope of calculations required for design
5 SIMPLE BATCH DISTILLATION
6 FRACTIONAL BATCH DISTILLATION
6.1 General
6.2 Approximate methods
6.3 Rigorous design - use of a computer model
6.4 Other factors influencing the design
6.4.1 Occupation
6.4.2 Choice of Batch Rectification or Stripping
6.4.3 Batch size
6.4.4 Initial estimate of cut policy
6.4.5 Liquid Holdup
6.4.6 Total reflux operation and heating-up time
6.4.7 Column operating pressure
6.5 Optimum Design of the Batch Still
6.6 Special design problems
7 GENERAL ASPECTS OF EQUIPMENT DESIGN
7.1 Kettle reboilers
7.2 Column Internals
7.3 Condensers and reflux split boxes
8 PROCESS CONTROL AND INSTRUMENTATION IN
BATCH DISTILLATION
9 MECHANICAL DESIGN FEATURES
10 BIBLIOGRAPHY
APPENDICES
A McCABE - THIELE METHOD - TYPICAL EXAMPLE
Process Flow Diagram includes the equipment, major flow stream and control logic of the chemical process plants. This is the very first document prepared to meet specific plant requirements.
Para quien inicia su estudio en los balances de energia es un documento que apoya en la definicion de terminos y presenta ejemplos de como calcular las 6 diferentes formas de energia que se consideran, es un inicio para quien hace ingenieria quimica, ingenieria de procesos o biotecnologia industrial
The effect of wind speed on a 5 × 5 fan air cooled steam condenser (ACC) under windy conditions is investigated using computational fluid dynamics. It is found that cross winds significantly reduce the air flow rate that is delivered by the fans in normal conditions. The effect of wind speed is found to be varying for different fan deck heights of the air cooled condenser. It is recommended that at the initial stage of a power plant which is equipped with an air cooled condenser, the wind effects analysis is necessary and helpful in mitigating the adverse effect of winds.
Renewable Energy Systems For Building Professionals Great Lakes Brewing Com...gogeisel
A presentation delivered to Cleveland design and building professionals on April 22, 2010. This presentation highlights the design and installation of a solar thermal hot water heating system.
Concepts of Distillation are covered in the presentation. Though it provides the outlines only, but reader can develop more from this presentation. Distillation is one of the majorly used separation technique in the chemical process industries. It is suitable for two or more miscible liquids with different volatility.
With a properly applied condensing heat recovery system, thermal efficiencies nearing 100% can be achieved. Even if your site is unable to achieve this level of efficiency, improvements in energy efficiency can be realized through condensing heat recovery. Typically, 5 to 20 percent fuel savings can be practically and economically realized. Given all that, it makes sense to learn more about condensing heat recovery technologies.
Air flow configuration is an important consideration in the design of a rotary kiln. This presentation looks at the different types of air flow available, and the benefits each has to offer.
This presentation outlines the key considerations necessary for selecting appropriately sized CHPWH systems. It also showcases Ecotope's new Ecosizer tool.
Distillation is one of the widely used separation method in most of the Chemical Process Industries. Improper design/ operation & maintenance leads to various troubles like reduced plant capacity, poor quality of separated products, high energy consumption, etc. This presentation is for learning about the troubleshooting of distillation systems. Through conceptual aspects of the overall distillation system, reader can easily identify the various causes of probable troubles and will be able to suggest their remedial measures.
Distillation is one of the widely used separation method in most of the Chemical Process Industries. Improper design/ operation & maintenance leads to various troubles like reduced plant capacity, poor quality of separated products, high energy consumption, etc. This presentation is for learning about the troubleshooting of packed type distillation systems. Through conceptual aspects of the overall distillation system, reader can easily identify the various causes of probable troubles and will be able to suggest their remedial measures.
Our Green Mission أهدافنا خضراء تقليل هدر الطاقة فى منظومتي التكييف والتهوية و تجويد أجواء الحياة الداخلية تقديرا لقيمة أمنا «الأرض»
To efficiently reduce energy wastage in HVAC Industry and improve the quality of indoor environment with high regards to our mother “Earth”.
Cleaver Brooks - To Condense or Not to Condense - How to Choose the Correct B...FMA Summits
We will cover non-condensing boilers, condensing boilers, and various technologies within each boiler type. With different boiler types understood, we will focus on when to apply condensing or non-condensing boilers in different system for the best application of each type.
Centrifugal Pumps - Concept E-Learning Program - Study MaterialPankaj Khandelwal
Study Material of Koncept Learning Center's Concept E-Learning Program on Distillation .
The course is directed by Mr. Pankaj Khandelwal
Centrifugal pump is one of the widely used liquid transportation rotary equipment in most of the industries either for the chemical transfer or utilities circulation.
Like any pumps, it also increases fluid energy due to which liquid is transferred from its low energy source to high energy destination. Impeller plays a major role for this purpose. Impeller is driven by the suitable drive either by the electric motor or diesel engine set.
Centrifugal pump supplier’s have their own pump designs while users have vary much varied applications from low flow & high differential pressure to high flow & low differential pressure. Thus the selection of centrifugal pumps is critical. This is done by matching duty point determined by the user and the characteristics curves supplied by the suppliers.
Contents:
1) Why Pump is required?
2) Pumping System
3) Industrial applications
4) Parts of Pumps
5) MWC Concepts
6) Fluid Energy Concepts
7) Cavitation Concepts
8) Characteristics Curves
9) Hydraulic Calculations
10) Pump Selection
For course details - klcenter@gmail.com / www.konceptlearningcenter.com
Call / Whatsapp - 8237829150 or 9371121220
Prithviraj Khandelwal
Distillation - Concept E-Learning Program - Study MaterialPankaj Khandelwal
Study Material of Koncept Learning Center's Concept E-Learning Program on Distillation .
The course is directed by Mr. Pankaj Khandelwal
For course details - klcenter@gmail.com / www.konceptlearningcenter.com
Call / Whatsapp - 8237829150 or 9371121220
Prithviraj Khandelwal
Life Concept Program - "Ownership - Doing Things Own Way" by Pankaj Khandelwal & Prithviraj Khandelwal (Koncept Learning Center)
In-house corporate training program for Leadership Development.
A motivational program to bring about a sense of Ownership in individuals
Program Objective - To bring out Ownership in every individual working in the organizations.
Whether an individual’s way of solving any problem is right or wrong, it can be judged by the ultimate result of success or failure. Surely, they will be fully satisfied with their approach.
Owners do things their own way without worrying much about success or failure. Success brings happiness while failure adds new experience.
Fear of failures often stops an individual to take any risky initiatives. Owners are “Risk Takers” & also believe on “First to Start” approach. Looking at the problem, they deeply involve themselves to find out its solution. They are good at judging and timely evaluating the probable returns of their efforts and are flexible to alter the methodology adapted earlier. They always look for improved versions through their creative minds.
Often owners are impatient to grow, which many times brings imbalance in their lives. They need to learn to “Grow with Happiness”.
This booklet contains mainly the concepts of distillation which are required by the plant designers as well as plant operational teams. This will help readers to get more of insight of distillation column understanding.
This presentation is developed for working managers who want to transform self as mentors...Different roles of managers, teachers are combined to mentor. Why to become mentor, Mentor's desired qualities and how to become mentor, etc. are covered here...
This presentation is for transforming Consumers to Creators. As high degree of consumerism often blocks the person's creative behavior despite born as creator. This also highlights Conceptual Approach for Innovative Solutions which are perfect in nature.
This presentation includes applications of filtration, filtration processing steps, different filtration conditions, affect of fluid characteristics on filtration, classification and scale up of filters.
This presentation outlines about Evaporation and different types of evaporators...Various industrial applications, different types of solutions, material & energy balance, concept of steam economy, system pressure conditions, feeding pattern, etc. are covered.
Concepts of Heat Exchanger from its applications, heat transfer theory, parts of shell & tube heat exchanger, types of heat exchangers are included here
Conceptual Approach for Trouble Shooting of Chemical Process Industry. Proper design and trained operating manpower ensures trouble free plant operation.
Industrial Training at Shahjalal Fertilizer Company Limited (SFCL)MdTanvirMahtab2
This presentation is about the working procedure of Shahjalal Fertilizer Company Limited (SFCL). A Govt. owned Company of Bangladesh Chemical Industries Corporation under Ministry of Industries.
TECHNICAL TRAINING MANUAL GENERAL FAMILIARIZATION COURSEDuvanRamosGarzon1
AIRCRAFT GENERAL
The Single Aisle is the most advanced family aircraft in service today, with fly-by-wire flight controls.
The A318, A319, A320 and A321 are twin-engine subsonic medium range aircraft.
The family offers a choice of engines
Event Management System Vb Net Project Report.pdfKamal Acharya
In present era, the scopes of information technology growing with a very fast .We do not see any are untouched from this industry. The scope of information technology has become wider includes: Business and industry. Household Business, Communication, Education, Entertainment, Science, Medicine, Engineering, Distance Learning, Weather Forecasting. Carrier Searching and so on.
My project named “Event Management System” is software that store and maintained all events coordinated in college. It also helpful to print related reports. My project will help to record the events coordinated by faculties with their Name, Event subject, date & details in an efficient & effective ways.
In my system we have to make a system by which a user can record all events coordinated by a particular faculty. In our proposed system some more featured are added which differs it from the existing system such as security.
Automobile Management System Project Report.pdfKamal Acharya
The proposed project is developed to manage the automobile in the automobile dealer company. The main module in this project is login, automobile management, customer management, sales, complaints and reports. The first module is the login. The automobile showroom owner should login to the project for usage. The username and password are verified and if it is correct, next form opens. If the username and password are not correct, it shows the error message.
When a customer search for a automobile, if the automobile is available, they will be taken to a page that shows the details of the automobile including automobile name, automobile ID, quantity, price etc. “Automobile Management System” is useful for maintaining automobiles, customers effectively and hence helps for establishing good relation between customer and automobile organization. It contains various customized modules for effectively maintaining automobiles and stock information accurately and safely.
When the automobile is sold to the customer, stock will be reduced automatically. When a new purchase is made, stock will be increased automatically. While selecting automobiles for sale, the proposed software will automatically check for total number of available stock of that particular item, if the total stock of that particular item is less than 5, software will notify the user to purchase the particular item.
Also when the user tries to sale items which are not in stock, the system will prompt the user that the stock is not enough. Customers of this system can search for a automobile; can purchase a automobile easily by selecting fast. On the other hand the stock of automobiles can be maintained perfectly by the automobile shop manager overcoming the drawbacks of existing system.
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.
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A 10 kgs/hr
B 90 kgs/hr
Total 100 kgs/hr
Temp. 30 oC
Phase Liquid -
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A 10 kgs/hr
B 90 kgs/hr
Total 100 kgs/hr
Temp. 90 oC
Phase Liquid -
2
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A 9.5 kgs/hr
B 0.5 kgs/hr
Total 10 kgs/hr
Temp. 30 oC
Phase Liquid -
2
3
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3
A 0.5 kgs/hr
B 89.5 kgs/hr
Total 90 kgs/hr
Temp. 30 oC
Phase Liquid -
4
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4
A 9.5 kgs/hr
B 0.5 kgs/hr
Total 10 kgs/hr
Temp. 80 oC
Phase Liquid -
5
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1 2
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4
5
A 38 kgs/hr
B 2 kgs/hr
Total 40 kgs/hr
Temp. 80 oC
Phase Liquid -
6
Reflux Ratio = 4
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1 2
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4
5
A 47.5 kgs/hr
B 2.5 kgs/hr
Total 50 kgs/hr
Temp. 80 oC
Phase Liquid -
6
7
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A 47.5 kgs/hr
B 2.5 kgs/hr
Total 50 kgs/hr
Temp. 80 oC
Phase Vapor -
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A 0.5 kgs/hr
B 89.5 kgs/hr
Total 90 kgs/hr
Temp. 105 oC
Phase Liquid -
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cA = 0.8 kcal/kg.oC
cB = 1.0 kcal/kg.oC
LA = 225 kcal/kg
LB = 540 kcal/kg
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Water
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Product
1 2
3
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9
10
A 147.8 kgs/hr
B 26462.2 kgs/hr
Total 26610 kgs/hr
Temp. 105 oC
Phase Liquid -
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Product
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Product
1 2
3
4
5
6
7
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9
10
A 147.8 kgs/hr
B 26462.2 kgs/hr
Total 26610 kgs/hr
Temp. 105.5 oC
Phase Liquid -
11
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3
4
5
6
7
8
9
10
11
HFPH=5880 kcal/hr
HCON=12037.5 kcal/hr
HTPC=405 kcal/hr
HBPC=6742.5 kcal/hrHREB=13305 kcal/hr
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3
4
5
6
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HFPH=5880 kcal/hr
HCON=12037.5 kcal/hr
HTPC=405 kcal/hr
HBPC=6742.5 kcal/hrHREB=13305 kcal/hr
W 10.8 kgs/hr
Temp. 120 oC
Phase Vapor -
12
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Product
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Product
1 2
3
4
5
6
7
8
9
10
11
HFPH=5880 kcal/hr
HCON=12037.5 kcal/hr
HTPC=405 kcal/hr
HBPC=6742.5 kcal/hrHREB=13305 kcal/hr
W 10.8 kgs/hr
Temp. 120 oC
Phase Liquid -
12
13
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1 2
3
4
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HFPH=5880 kcal/hr
HCON=12037.5 kcal/hr
HTPC=405 kcal/hr
HBPC=6742.5 kcal/hrHREB=13305 kcal/hr
W 1203.7 kgs/hr
Temp. 25 oC
Phase Liquid -
12
13
14
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1 2
3
4
5
6
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10
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HFPH=5880 kcal/hr
HCON=12037.5 kcal/hr
HTPC=405 kcal/hr
HBPC=6742.5 kcal/hrHREB=13305 kcal/hr
W 1203.7 kgs/hr
Temp. 35 oC
Phase Liquid -
12
13
14
15
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3
4
5
6
7
8
9
10
11
HFPH=5880 kcal/hr
HCON=12037.5 kcal/hr
HTPC=405 kcal/hr
HBPC=6742.5 kcal/hrHREB=13305 kcal/hr
W 202.5 kgs/hr
Temp. 25 oC
Phase Liquid -
12
13
14
15
16
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Product
1 2
3
4
5
6
7
8
9
10
11
HFPH=5880 kcal/hr
HCON=12037.5 kcal/hr
HTPC=405 kcal/hr
HBPC=6742.5 kcal/hrHREB=13305 kcal/hr
W 202.5 kgs/hr
Temp. 27 oC
Phase Liquid -
12
13
14
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16
17
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1 2
3
4
5
6
7
8
9
10
11
HFPH=5880 kcal/hr
HCON=12037.5 kcal/hr
HTPC=405 kcal/hr
HBPC=6742.5 kcal/hrHREB=13305 kcal/hr
W 3371.2 kgs/hr
Temp. 25 oC
Phase Liquid -
12
13
14
15
16
17
18
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3
4
5
6
7
8
9
10
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HFPH=5880 kcal/hr
HCON=12037.5 kcal/hr
HTPC=405 kcal/hr
HBPC=6742.5 kcal/hrHREB=13305 kcal/hr
W 3371.2 kgs/hr
Temp. 27 oC
Phase Liquid -
12
13
14
15
16
17
18
19
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3
4
5
6
7
8
9
10
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HFPH=5880 kcal/hr
HCON=12037.5 kcal/hr
HTPC=405 kcal/hr
HBPC=6742.5 kcal/hrHREB=13305 kcal/hr
12
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20
W 24.6 kgs/hr
Temp. 120 oC
Phase Vapor -
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3
4
5
6
7
8
9
10
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HFPH=5880 kcal/hr
HCON=12037.5 kcal/hr
HTPC=405 kcal/hr
HBPC=6742.5 kcal/hrHREB=13305 kcal/hr
12
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20
W 24.6 kgs/hr
Temp. 120 oC
Phase Liquid -
21
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Stream> 1 2 3 4 5 6 7 8 9 10 11
A 10 10 9.5 0.5 9.5 38 47.5 47.5 0.5 147.8 147.8
B 90 90 0.5 89.5 0.5 2 2.5 2.5 89.5 26462.2 26462.2
W - - - - - - - - - - -
T 100 100 10 90 10 40 50 50 90 26610 26610
Temp. 30 90 80 30 80 80 80 80 105 105 105.5
Phase Liquid Liquid Liquid Liquid Liquid Liquid Liquid Vapor Liquid Liquid Liquid
A,B,W & T : kgs/hr
Temp. : oC
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Cooling Water
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Water
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Top
Product
Bottom
Product
1 2
3
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Stream> 12 13 14 15 16 17 18 19 20 21
A - - - - - - - - - -
B - - - - - - - - - -
W 10.8 10.8 1203.7 1203.7 202.5 202.5 3371.2 3371.2 24.6 24.6
T 10.8 10.8 1203.7 1203.7 202.5 202.5 3371.2 3371.2 24.6 24.6
Temp. 120 120 25 35 25 27 25 27 120 120
Phase Vapor Liquid Liquid Liquid Liquid Liquid Liquid Liquid Vapor Liquid
A,B,W & T : kgs/hr
Temp. : oC