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.
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!
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
In the plant, ammonia is produced from synthesis gas containing hydrogen and nitrogen in the ratio of approximately 3:1. Besides these components, the synthesis gas contains inert gases such as argon and methane to a limited extent. The source of H2 is demineralized water and the hydrocarbons in the natural gas. The source of N2 is the atmospheric air. The source of CO2 is the hydrocarbons in the natural gas feed. Product ammonia and CO2 is sent to urea plant. The present article intended the description of ammonia plant for natural gas based plants and the possible material balance of some section.
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
Production of 66000 ton/year of Formaldehyde from Methanol using Silver catal...Engr Muhammad Zeeshan
Formaldehyde, the target product is an organic compound representing the most elementary configuration of the aldehydes. It behaves as a synthesis baseline for many other chemical compounds, including phenol formaldehyde, urea formaldehyde, melamine resin, Paints, and Glues. It is also used in medical field i.e. as a disinfectant and preservation of cell and tissues. The aim of this project is to reach 98% conversion of methanol using Silver Catalyst. Detailed calculations were performed in the report for all equipment in the plant including all expenses of the plant erection, taking into account the required process conditions to achieve a production capacity of 66000 ton/year of formaldehyde (as Formalin).
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!
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
In the plant, ammonia is produced from synthesis gas containing hydrogen and nitrogen in the ratio of approximately 3:1. Besides these components, the synthesis gas contains inert gases such as argon and methane to a limited extent. The source of H2 is demineralized water and the hydrocarbons in the natural gas. The source of N2 is the atmospheric air. The source of CO2 is the hydrocarbons in the natural gas feed. Product ammonia and CO2 is sent to urea plant. The present article intended the description of ammonia plant for natural gas based plants and the possible material balance of some section.
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
Production of 66000 ton/year of Formaldehyde from Methanol using Silver catal...Engr Muhammad Zeeshan
Formaldehyde, the target product is an organic compound representing the most elementary configuration of the aldehydes. It behaves as a synthesis baseline for many other chemical compounds, including phenol formaldehyde, urea formaldehyde, melamine resin, Paints, and Glues. It is also used in medical field i.e. as a disinfectant and preservation of cell and tissues. The aim of this project is to reach 98% conversion of methanol using Silver Catalyst. Detailed calculations were performed in the report for all equipment in the plant including all expenses of the plant erection, taking into account the required process conditions to achieve a production capacity of 66000 ton/year of formaldehyde (as Formalin).
Design of Methanol Water Distillation Column Rita EL Khoury
Methanol is an essential feed stock for the manufacture of many industrial products such as adhesives and paints and it is widely used as a solvent in many chemical reactions. Crude methanol is obtained from steam reforming of natural gas and then a purification process is needed since it contains smaller and larger degree of impurities.
The purification process consists of two steps: a topping column used to remove the low boiling impurity called the light ends; and the remaining water methanol mixture is transferred to another column called the refining column where it is constantly boiled until separation occurs. Methanol rises to the top while the water accumulates in the bottom.
This document focuses on methanol water separation. A detailed design study for the distillation column is conducted where the separation occurs at atmospheric pressure with a total condenser and a partial reboiler.
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.
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.
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
I found no good source for extractive distillation on the internet.So i decided to make one myself.This ppt discusses about the technology,its working and benefits.It compares extractive distillation side by side to azeotropic distillation and counts the advantages.
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.
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.
Design of Methanol Water Distillation Column Rita EL Khoury
Methanol is an essential feed stock for the manufacture of many industrial products such as adhesives and paints and it is widely used as a solvent in many chemical reactions. Crude methanol is obtained from steam reforming of natural gas and then a purification process is needed since it contains smaller and larger degree of impurities.
The purification process consists of two steps: a topping column used to remove the low boiling impurity called the light ends; and the remaining water methanol mixture is transferred to another column called the refining column where it is constantly boiled until separation occurs. Methanol rises to the top while the water accumulates in the bottom.
This document focuses on methanol water separation. A detailed design study for the distillation column is conducted where the separation occurs at atmospheric pressure with a total condenser and a partial reboiler.
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.
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.
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
I found no good source for extractive distillation on the internet.So i decided to make one myself.This ppt discusses about the technology,its working and benefits.It compares extractive distillation side by side to azeotropic distillation and counts the advantages.
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.
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.
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.
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.
Episode 38 : Bin and Hopper Design
< 1960s storage bins were designed by guessing
Then in 1960s A.W. Jenike changed all.- He developed theory, methods to apply, inc. the eqns. And measurement of necessary particles properties.
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
Similar to Troubleshooting of Packed Distillation Column (8)
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
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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...
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Operation “Blue Star” is the only event in the history of Independent India where the state went into war with its own people. Even after about 40 years it is not clear if it was culmination of states anger over people of the region, a political game of power or start of dictatorial chapter in the democratic setup.
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11. klcenter@gmail.comKoncept Learning Center
Troubleshooting of
Distillation Column
(Packed Type)
Enhancing Visualization
Trouble may be due to
d.) Poor Erection
o Column Perpendicularity
o Liquid Distributor Leveling
o Condensor Elevation
12. klcenter@gmail.comKoncept Learning Center
Troubleshooting of
Distillation Column
(Packed Type)
Enhancing Visualization
Trouble may be due to
e.) Careless Pre-commissioning Checks
o Debris left in column
o Glass in SG/LG Missing
o Wrong Direction of Rotameter
13. klcenter@gmail.comKoncept Learning Center
Troubleshooting of
Distillation Column
(Packed Type)
Enhancing Visualization
Trouble may be due to
f.) Inexperienced Startup
o Fast Initial Heating
o No cooling water in condensor
o Higher feed rate at the start
14. klcenter@gmail.comKoncept Learning Center
Troubleshooting of
Distillation Column
(Packed Type)
Enhancing Visualization
Trouble may be due to
g.) Casual Normal Operation
o High reflux ratio (than specified)
o Low feed temperature
o Sub-cooled reflux
15. klcenter@gmail.comKoncept Learning Center
Troubleshooting of
Distillation Column
(Packed Type)
Enhancing Visualization
Trouble may be due to
h.) Careless Maintenance
o Damaging column packing
o Changed gasket material
o Relocating instrument
18. klcenter@gmail.comKoncept Learning Center
Troubleshooting of
Distillation Column
(Packed Type)
Enhancing Visualization
Know About Distillation
Here the Imperfection Starts (Man Made) which leads to Trouble
Third (Plant) Provision
Space like Packing for Heat & Mass Transfer
19. klcenter@gmail.comKoncept Learning Center
Troubleshooting of
Distillation Column
(Packed Type)
Enhancing Visualization
Know About Packed Bed Column
a.) Cylindrical Vertical Vessel with Nozzles, Manholes, etc.
Atmospheric
Pressure
Vacuum
20. klcenter@gmail.comKoncept Learning Center
Troubleshooting of
Distillation Column
(Packed Type)
Enhancing Visualization
Know About Packed Bed Column
b.) Packing
To provide space for Liquid/ Vapor direct contact
Simultaneous Heat & Mass Transfer
More Contact & Less Pressure Drop
21. klcenter@gmail.comKoncept Learning Center
Troubleshooting of
Distillation Column
(Packed Type)
Enhancing Visualization
Know About Packed Bed Column
b.) Packing
First Generation (Raschig Ring, Berl Saddle)
1895 to the 1950s
simple shapes with closed surfaces, robust
and stable design, cost-effective production
22. klcenter@gmail.comKoncept Learning Center
Troubleshooting of
Distillation Column
(Packed Type)
Enhancing Visualization
Know About Packed Bed Column
b.) Packing Second Generation (Pall Ring, Intalox Saddle)
late 1950s to the early 1970s
surfaces with cutted windows and bent tongues,
improved area distribution lowering pressure
drop and enhancing capacity
23. klcenter@gmail.comKoncept Learning Center
Troubleshooting of
Distillation Column
(Packed Type)
Enhancing Visualization
Know About Packed Bed Column
b.) Packing
Third Generation (Net/Grid Structures, IMPT Ring)
late 1970s to the 1990s
framework structure, large free cross section,
low pressure drop, high efficiency
24. klcenter@gmail.comKoncept Learning Center
Troubleshooting of
Distillation Column
(Packed Type)
Enhancing Visualization
Know About Packed Bed Column
b.) Packing Fourth Generation (Raschig Super-Ring)
late 1990s until present
lower pressure drop and better mass transfer
efficiency
27. klcenter@gmail.comKoncept Learning Center
Troubleshooting of
Distillation Column
(Packed Type)
Enhancing Visualization
Know About Packed Bed Column
d.) Liquid Distributor
1. Gravitational Types
i. Orifice Type
ii. Weir Type
2. Pressure Drop Types
i. Spray Nozzle Type
ii. Perforated Pipe Type
28. klcenter@gmail.comKoncept Learning Center
Troubleshooting of
Distillation Column
(Packed Type)
Enhancing Visualization
Know Distillation System
Feed Preheater
Reboiler
Distillation
Column
Bottom Product
Cooler
Top Product
Cooler
Condenser
A + B
A
B
Steam
Steam
Cooling Water
Cooling
Water
Cooling
Water
Feed
Top Vapors
Reflux
Top
Product
Bottom
Product
29. klcenter@gmail.comKoncept Learning Center
Troubleshooting of
Distillation Column
(Packed Type)
Enhancing Visualization
Know Distillation System
Feed Preheater
Reboiler
Distillation
Column
Bottom Product
Cooler
Top Product
Cooler
Condenser
A + B
A
B
Steam
Steam
Cooling Water
Cooling
Water
Cooling
Water
Feed
Top Vapors
Reflux
Top
Product
Bottom
Product
a.) Feeding
• Gravity/ Pump
• Pre-heating
30. klcenter@gmail.comKoncept Learning Center
Troubleshooting of
Distillation Column
(Packed Type)
Enhancing Visualization
Know Distillation System
Feed Preheater
Reboiler
Distillation
Column
Bottom Product
Cooler
Top Product
Cooler
Condenser
A + B
A
B
Steam
Steam
Cooling Water
Cooling
Water
Cooling
Water
Feed
Top Vapors
Reflux
Top
Product
Bottom
Product
b.) Vapor Condensation/ Reflux
• Condensor – Horizontal/Vertical
• Partial vs. Total Condensation
• Reflux – Gravity / Pump
31. klcenter@gmail.comKoncept Learning Center
Troubleshooting of
Distillation Column
(Packed Type)
Enhancing Visualization
Know Distillation System
Feed Preheater
Reboiler
Distillation
Column
Bottom Product
Cooler
Top Product
Cooler
Condenser
A + B
A
B
Steam
Steam
Cooling Water
Cooling
Water
Cooling
Water
Feed
Top Vapors
Reflux
Top
Product
Bottom
Product
c.) Heat Supply
• Direct / Indirect
• Reboiler – Thermosiphon, Forced, Kettle
32. klcenter@gmail.comKoncept Learning Center
Troubleshooting of
Distillation Column
(Packed Type)
Enhancing Visualization
Design of Distillation (Packed Column)
a.) Height of Packing
Theoretical Stages x HETP
Based on Feed Condition & Reflux Ratio
Based on Packing Type
33. klcenter@gmail.comKoncept Learning Center
Troubleshooting of
Distillation Column
(Packed Type)
Enhancing Visualization
Design of Distillation (Packed Column)
b.) Material & Energy Balance
Overall Material Balance
A=10 t
B=90 t
T =100 t
A=9.99 t
B=0.01 t
T=10 t
A=0.01 t
B=99.99 t
T=90 t
34. klcenter@gmail.comKoncept Learning Center
Troubleshooting of
Distillation Column
(Packed Type)
Enhancing Visualization
Design of Distillation (Packed Column)
b.) Material & Energy Balance
At Reflux Ratio = 4
Reflux Flow = 40 t
Vapor Flow = 50 t
A=10 t
B=90 t
T =100 t
A=9.99 t
B=0.01 t
T=10 t
A=0.01 t
B=99.99 t
T=90 t
35. klcenter@gmail.comKoncept Learning Center
Troubleshooting of
Distillation Column
(Packed Type)
Enhancing Visualization
Design of Distillation (Packed Column)
b.) Material & Energy Balance
Energy Balance
•for Condensor Load
•for Reboiler Load
A=10 t
B=90 t
T =100 t
A=9.99 t
B=0.01 t
T=10 t
A=0.01 t
B=99.99 t
T=90 t
36. klcenter@gmail.comKoncept Learning Center
Troubleshooting of
Distillation Column
(Packed Type)
Enhancing Visualization
Design of Distillation (Packed Column)
c.) Column Diameter
Tower Area = Vapor Mass Rate / Vapor Mass Velocity
37. klcenter@gmail.comKoncept Learning Center
Troubleshooting of
Distillation Column
(Packed Type)
Enhancing Visualization
Variation Analysis (in Designed Column)
A.) Feed
a.) Feed Flow Rate
a.1) Expected = 100 TPH Actual = 50 TPH
a.2) Expected = 100 TPH Actual = 150 TPH
Vapor / Liquid Load
38. klcenter@gmail.comKoncept Learning Center
Troubleshooting of
Distillation Column
(Packed Type)
Enhancing Visualization
Variation Analysis (in Designed Column)
A.) Feed
b.) Feed Composition
b.1) Expected : 10% w/w ‘A’ Actual : 5 % w/w ‘A’
b.2) Expected : 10% w/w ‘A’ Actual : 20 % w/w ‘A’
Change of Feed Nozzle
39. klcenter@gmail.comKoncept Learning Center
Troubleshooting of
Distillation Column
(Packed Type)
Enhancing Visualization
Variation Analysis (in Designed Column)
A.) Feed
c.) Feed Temperature/ Condition
c.1) Expected : 900C Liquid Actual : 600C Liquid
c.2) Expected : 900C Liquid Actual : 900C Vapor
Heat Load to Reboiler
40. klcenter@gmail.comKoncept Learning Center
Troubleshooting of
Distillation Column
(Packed Type)
Enhancing Visualization
Variation Analysis (in Designed Column)
B.) Reflux
a.) Flow Rate
a.1) Expected : 50 TPH Actual : 25 TPH
a.2) Expected : 50 TPH Actual : 100 TPH
42. klcenter@gmail.comKoncept Learning Center
Troubleshooting of
Distillation Column
(Packed Type)
Enhancing Visualization
Variation Analysis (in Designed Column)
C.) Steam in Reboiler
a.) Flow Rate
b.) Pressure
c.) Quality : Dry, Wet, Superheated
44. klcenter@gmail.comKoncept Learning Center
Troubleshooting of
Distillation Column
(Packed Type)
Enhancing Visualization
Trouble Identification
a.) By Operating Parameter Study
Pressure, Temperature, Composition at different locations
Bottom Pressure Expected : 2.5 kg/cm2(g) Actual : 2.6 kg/cm2(g)
Bottom Temperature Expected : 105oC Actual : 104oC
Bottom Composition Expected : 0.01%w/w ‘A’ Actual : 0.1%w/w ‘A’
45. klcenter@gmail.comKoncept Learning Center
Troubleshooting of
Distillation Column
(Packed Type)
Enhancing Visualization
Trouble Identification
b.) By Visual Inspection
During Operation : Flooding through SG/LG
On Column Opening : Choked Liquid Distributor
46. klcenter@gmail.comKoncept Learning Center
Troubleshooting of
Distillation Column
(Packed Type)
Enhancing Visualization
Trouble Identification
c.) By Advanced Tools
•Simulation Models
•Gamma Scanning
•X-Ray Analysis
•Video Camera
49. klcenter@gmail.comKoncept Learning Center
Troubleshooting of
Distillation Column
(Packed Type)
Enhancing Visualization
Troubles within Column
b.) Hardware Specific
•Packing : Size, Type, Broken/Damaged Packing
•Liquid Distributor : Choked holes, Tilted, Under/Over sized
•Vapor Supply : Sheath
50. klcenter@gmail.comKoncept Learning Center
Troubleshooting of
Distillation Column
(Packed Type)
Enhancing Visualization
Other Hardware Affecting Distillation
a.) Equipment other than Distillation Column
a.1) Heat Exchanger
•Feed Pre-heater
•Condensor
•Reboiler
•Coolers
•Heat Transfer Area – Less / More
•Orientation – Horizontal / Vertical
•Location - Elevation
51. klcenter@gmail.comKoncept Learning Center
Troubleshooting of
Distillation Column
(Packed Type)
Enhancing Visualization
Other Hardware Affecting Distillation
a.) Equipment other than Distillation Column
a.2) Pump
•Feed Pump
•Reflux Pump
•Product Draw Pump
•Flow Rate vs. Head
•NPSH (Required) vs. NPSH (Available)
52. klcenter@gmail.comKoncept Learning Center
Troubleshooting of
Distillation Column
(Packed Type)
Enhancing Visualization
Other Hardware Affecting Distillation
b.) Pipe Line
•Reflux Line with Loop
•Thermo-siphon Reboiler Piping
•Utility Piping – Steam, Cooling Water
•Vacuum Line
•Pump Suction Line
53. klcenter@gmail.comKoncept Learning Center
Troubleshooting of
Distillation Column
(Packed Type)
Enhancing Visualization
Other Hardware Affecting Distillation
c.) Instrument
•Wrong Calibration
•Control Valve Operation
•Wrong Placement/Installation
54. Koncept Learning Center
9371121220 klcenter@gmail.com
8237829150
9623232500
9371121220
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Enhancing Visualization
Since 2001