Processing of petroleum types of refluxKarnav Rana
PROCESSING OF PETROLEUM :TYPES OF REFLUX
arrangements of distillation towers
Pump back reflux and pump around reflux
Side stripping columns
process refining & petrochemicals
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.
Processing of petroleum types of refluxKarnav Rana
PROCESSING OF PETROLEUM :TYPES OF REFLUX
arrangements of distillation towers
Pump back reflux and pump around reflux
Side stripping columns
process refining & petrochemicals
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.
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: 1.2 Flash distillation.
These slides may be used for a part of Advanced level course in Chemical Reaction Engineering. I taught this course to Masters level students covering 1.5 credit hours.
Gas - Liquid Reactors
0 INTRODUCTION/PURPOSE
1 SCOPE
2 FIELD OF APPLICATION
3 DEFINITIONS
4 PRELIMINARY CONSIDERATIONS
4.1 Preliminary Equipment Selection
4.2 Equipment for Low Viscosity Liquids
4.3 Equipment for High Viscosity Liquids
5 REACTOR DESIGN
6 ESSENTIAL THEORY
6.1 Rate and Yield Determining Steps
6.2 Chemical and Physical Rates
6.3 Modification for Exothermic and Complex Reactions
6.4 Preliminary Selection of Reactor Type
7 EXPERIMENTAL DETERMINATION OF REGIME
7.1 Direct Measurement of Reaction Kinetics
7.2 Laboratory Gas-Liquid Reactor Experiments
8 EQUILIBRIUM AND DIFFUSIVITY DATA SOURCES
9 OVERALL EFFECTS
9.1 Liquid Flow Patterns
9.2 Scale of Mixing
9.3 Gas Flow Pattern : Mean Driving Force for Mass Transfer
9.4 Gas-Liquid Reactor Modeling
9.5 Heat Transfer
9.6 Materials of Construction
9.7 Foaming
10 FINAL CHOICE OF REACTOR TYPE
11 SCALE-UP AND SPECIFICATION OF GAS-LIQUID
REACTORS
11.1 Bubble Columns
11.2 Packed Columns
11.3 Trickle Beds
11.4 Plate or Tray Columns
11.5 Spray Columns
11.6 Wiped Film
11.7 Spinning Film Reactors
11.8 Stirred Vessels
11.9 Plunging Jet
11.10 Surface Aerator
11.11 Static Mixers
11.12 Ejectors, Venturis and Orifice Plates
11.13 3-Phase Fluidized Bed
12 BIBLIOGRAPHY
TABLES
1 REGIMES OF GAS-LIQUID MASS TRANSFER WITH ISOTHERMAL CHEMICAL REACTION
2 REGIMES OF GAS-LIQUID MASS TRANSFER IGNORING LARGE EXOTHERMS OR OTHER COMPLICATIONS
3 COMPARATIVE MASS TRANSFER PERFORMANCE OF CONTACTING DEVICES
4 COMPARATIVE MASS TRANSFER DATA
5 CHOICE OF GAS-LIQUID REACTOR TYPE
FIGURES
1 RATE AND YIELD DETERMINING STEPS
2 ENHANCEMENT FACTOR vs HATTA NUMBER
3 ENHANCEMENT FACTOR vs HATTA NUMBER : EFFECT OF THERMAL & OTHER FACTORS
4 REACTORS FOR LIQUID-PHASE KINETICS
MEASUREMENT
5 EXPERIMENTS TO DETERMINE THE OPERATING
REGIME
6 EXPERIMENTS DETERMINE THE OPERATING REGIME WHERE A SOLID CATALYST IS INVOLVED
7 THE MIXED ZONES IN LOOPS' MODEL FOR STIRRED REACTORS
Distillation is the basic and oldest chemical separation process used in the chemical industries and petroleum refining.
Let's recognize the difference between Packed and Plate columns in industry and the comparison of their usage!
Shell and Tube Heat Exchanger in heat TransferUsman Shah
This slide will explain you the chemical engineering terms .Al about the basics of this slide are explain in it. The basics of fluid mechanics, heat transfer, chemical engineering thermodynamics, fluid motions, newtonian fluids, are explain in this process.
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
Catalytic Reforming Process is one of the most important processes in the petroleum and petrochemical industries which produce high octane number gasoline.
The Design and Layout of Vertical Thermosyphon ReboilersGerard B. Hawkins
The Design and Layout of Vertical Thermosyphon Reboilers
0 INTRODUCTION/PURPOSE
1 SCOPE
2 FIELD OF APPLICATION
3 DEFINITIONS
4 THE DESIGN PROBLEM
5 COMPUTER PROGRAMS
6 GENERAL CONSIDERATIONS
6.1 Heating Medium Temperature
6.2 Fouling Resistance
7 DESIGN PARAMETERS
7.1 Overall Arrangement and Specifications
7.2 Geometry Elements
8 ANALYSIS OF COMMERCIALLY AVAILABLE
PROGRAM RESULTS
8.1 Main Results
8.2 Supplementary Results
8.3 Error Analysis
8.4 Adjustments to Design
9 OPERATING RANGE
10 CONTROL
10.1 Control of Condensing Heating Medium Pressure
10.2 Control of The Condensate Level
10.3 Control of Sensible Fluid Flow Rate
11 LAYOUT
11.1 Factors Influencing Design
11.2 A Standard Layout
12 BIBLIOGRAPHY
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: 1.2 Flash distillation.
These slides may be used for a part of Advanced level course in Chemical Reaction Engineering. I taught this course to Masters level students covering 1.5 credit hours.
Gas - Liquid Reactors
0 INTRODUCTION/PURPOSE
1 SCOPE
2 FIELD OF APPLICATION
3 DEFINITIONS
4 PRELIMINARY CONSIDERATIONS
4.1 Preliminary Equipment Selection
4.2 Equipment for Low Viscosity Liquids
4.3 Equipment for High Viscosity Liquids
5 REACTOR DESIGN
6 ESSENTIAL THEORY
6.1 Rate and Yield Determining Steps
6.2 Chemical and Physical Rates
6.3 Modification for Exothermic and Complex Reactions
6.4 Preliminary Selection of Reactor Type
7 EXPERIMENTAL DETERMINATION OF REGIME
7.1 Direct Measurement of Reaction Kinetics
7.2 Laboratory Gas-Liquid Reactor Experiments
8 EQUILIBRIUM AND DIFFUSIVITY DATA SOURCES
9 OVERALL EFFECTS
9.1 Liquid Flow Patterns
9.2 Scale of Mixing
9.3 Gas Flow Pattern : Mean Driving Force for Mass Transfer
9.4 Gas-Liquid Reactor Modeling
9.5 Heat Transfer
9.6 Materials of Construction
9.7 Foaming
10 FINAL CHOICE OF REACTOR TYPE
11 SCALE-UP AND SPECIFICATION OF GAS-LIQUID
REACTORS
11.1 Bubble Columns
11.2 Packed Columns
11.3 Trickle Beds
11.4 Plate or Tray Columns
11.5 Spray Columns
11.6 Wiped Film
11.7 Spinning Film Reactors
11.8 Stirred Vessels
11.9 Plunging Jet
11.10 Surface Aerator
11.11 Static Mixers
11.12 Ejectors, Venturis and Orifice Plates
11.13 3-Phase Fluidized Bed
12 BIBLIOGRAPHY
TABLES
1 REGIMES OF GAS-LIQUID MASS TRANSFER WITH ISOTHERMAL CHEMICAL REACTION
2 REGIMES OF GAS-LIQUID MASS TRANSFER IGNORING LARGE EXOTHERMS OR OTHER COMPLICATIONS
3 COMPARATIVE MASS TRANSFER PERFORMANCE OF CONTACTING DEVICES
4 COMPARATIVE MASS TRANSFER DATA
5 CHOICE OF GAS-LIQUID REACTOR TYPE
FIGURES
1 RATE AND YIELD DETERMINING STEPS
2 ENHANCEMENT FACTOR vs HATTA NUMBER
3 ENHANCEMENT FACTOR vs HATTA NUMBER : EFFECT OF THERMAL & OTHER FACTORS
4 REACTORS FOR LIQUID-PHASE KINETICS
MEASUREMENT
5 EXPERIMENTS TO DETERMINE THE OPERATING
REGIME
6 EXPERIMENTS DETERMINE THE OPERATING REGIME WHERE A SOLID CATALYST IS INVOLVED
7 THE MIXED ZONES IN LOOPS' MODEL FOR STIRRED REACTORS
Distillation is the basic and oldest chemical separation process used in the chemical industries and petroleum refining.
Let's recognize the difference between Packed and Plate columns in industry and the comparison of their usage!
Shell and Tube Heat Exchanger in heat TransferUsman Shah
This slide will explain you the chemical engineering terms .Al about the basics of this slide are explain in it. The basics of fluid mechanics, heat transfer, chemical engineering thermodynamics, fluid motions, newtonian fluids, are explain in this process.
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
Catalytic Reforming Process is one of the most important processes in the petroleum and petrochemical industries which produce high octane number gasoline.
The Design and Layout of Vertical Thermosyphon ReboilersGerard B. Hawkins
The Design and Layout of Vertical Thermosyphon Reboilers
0 INTRODUCTION/PURPOSE
1 SCOPE
2 FIELD OF APPLICATION
3 DEFINITIONS
4 THE DESIGN PROBLEM
5 COMPUTER PROGRAMS
6 GENERAL CONSIDERATIONS
6.1 Heating Medium Temperature
6.2 Fouling Resistance
7 DESIGN PARAMETERS
7.1 Overall Arrangement and Specifications
7.2 Geometry Elements
8 ANALYSIS OF COMMERCIALLY AVAILABLE
PROGRAM RESULTS
8.1 Main Results
8.2 Supplementary Results
8.3 Error Analysis
8.4 Adjustments to Design
9 OPERATING RANGE
10 CONTROL
10.1 Control of Condensing Heating Medium Pressure
10.2 Control of The Condensate Level
10.3 Control of Sensible Fluid Flow Rate
11 LAYOUT
11.1 Factors Influencing Design
11.2 A Standard Layout
12 BIBLIOGRAPHY
We have been recently Certified by Engineers India Limited ( EIL) for the Shell & Tube Waste Heat Recovery Boilers WHRB are fire tube industrial boilers equipped with advanced instrumentation to deliver maximum possible heat recovery.
Internally heat integrated distillation column for close boiling mixure Shahbaz khan
an example of process intensification in chemical industries, where distillation is widely used seperation process , HIDiC emprove themodynamic efficiency of distillation process
Design and Fabrication of Vapour Absorption Refrigeration System [Libr-H20]IJMER
Most of the energies are utilized by the industries due to depletion of fossil fuels and
increasing the fuel price to exploit the maximum presented energy from the waste heat source. The
industry which utilizes steam turbine exhaust carries a considerable amount of thermal energy. This
energy can be set in to positive use as a heat source for vapour absorption system to serves as cooling
system. This paper illustrates the thermal and fiscal advantages of using single effect lithium bromide
water absorption by means of waste heat. The objective of this work is to hypothetical design of lithium
bromide water absorption Refrigeration system using waste heat from any industry steam turbine
exhaust
A Systemic Optimization Approach for the Design of Natural Gas Dehydration PlantIJRES Journal
In designing dehydration units for natural gas, several critical parameters exist which can be varied to achieve a specified dew point depression. This paper studies the effects of varying number of trays in the contactor, glycol circulation rate through the contactor, temperature of the reboiler in the regenerator, amount of stripping gas used and operating pressure of the regenerator on the water content of the gas in a glycol dehydration unit. The effect of incorporating free water knock out (FWKO) tank before the absorber is also presented. An offshore platform in the Arctic region was chosen as the base case of this simulation and was modeled by using ASPEN HYSYS. Results show that the incorporation of FWKOT does not affect the TEG circulation rate required to approach equilibrium.
SiGNa's ActiveEOR® and ActiveSand® products are a new class of green chemicals that increase recovery from oil & gas reservoirs. SiGNa’s oil & gas products combine the benefits of chemical, immiscible gas, and thermal flooding techniques to give producers the advantages three oil recovery techniques from one easy-to-use, pumpable chemical. Silicides can be used as a standalone chemical or injected alongside other EOR techniques. Usable at any depth and with any viscosity, silicides generate heat, pressure, and silicates downhole, within the formation. No heat is lost on the surface and only minimal losses to the wellbore casing and tubing strings. These green chemicals produce only benign by-products and deliver cleaner wastewater, causing less impact on the environment.
SiGNa Oilfield Canada is a subsidiary of SiGNa Chemistry, a US-based manufacturer of stabilized alkali metals. Based in Calgary, SiGNa Oilfield Canada is committed to bringing innovative new chemical technologies to Canada's heavy oil market.
NO1 Uk best vashikaran specialist in delhi vashikaran baba near me online vas...Amil Baba Dawood bangali
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Forklift Classes Overview by Intella PartsIntella Parts
Discover the different forklift classes and their specific applications. Learn how to choose the right forklift for your needs to ensure safety, efficiency, and compliance in your operations.
For more technical information, visit our website https://intellaparts.com
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.
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.
6th International Conference on Machine Learning & Applications (CMLA 2024)ClaraZara1
6th International Conference on Machine Learning & Applications (CMLA 2024) will provide an excellent international forum for sharing knowledge and results in theory, methodology and applications of on Machine Learning & Applications.
Online aptitude test management system project report.pdfKamal Acharya
The purpose of on-line aptitude test system is to take online test in an efficient manner and no time wasting for checking the paper. The main objective of on-line aptitude test system is to efficiently evaluate the candidate thoroughly through a fully automated system that not only saves lot of time but also gives fast results. For students they give papers according to their convenience and time and there is no need of using extra thing like paper, pen etc. This can be used in educational institutions as well as in corporate world. Can be used anywhere any time as it is a web based application (user Location doesn’t matter). No restriction that examiner has to be present when the candidate takes the test.
Every time when lecturers/professors need to conduct examinations they have to sit down think about the questions and then create a whole new set of questions for each and every exam. In some cases the professor may want to give an open book online exam that is the student can take the exam any time anywhere, but the student might have to answer the questions in a limited time period. The professor may want to change the sequence of questions for every student. The problem that a student has is whenever a date for the exam is declared the student has to take it and there is no way he can take it at some other time. This project will create an interface for the examiner to create and store questions in a repository. It will also create an interface for the student to take examinations at his convenience and the questions and/or exams may be timed. Thereby creating an application which can be used by examiners and examinee’s simultaneously.
Examination System is very useful for Teachers/Professors. As in the teaching profession, you are responsible for writing question papers. In the conventional method, you write the question paper on paper, keep question papers separate from answers and all this information you have to keep in a locker to avoid unauthorized access. Using the Examination System you can create a question paper and everything will be written to a single exam file in encrypted format. You can set the General and Administrator password to avoid unauthorized access to your question paper. Every time you start the examination, the program shuffles all the questions and selects them randomly from the database, which reduces the chances of memorizing the questions.
Online aptitude test management system project report.pdf
reboiler in process industry.
1. REBOILERS IN PROCESS INDUSTRIES
Presented By:
Jay Jawalge (11920039)
Rupali Kadam (11920081)
Karthik Iyer (11810069)
Payal Khandagale (11920014)
Arjun Phad (11920021)
Group 7 1
2. Content
• Reboiler
• Types of reboiler
• Choice of type
• Selection factors of reboiler type
• Variables influence boiler design
• Advantages & disadvantages
• Case study
• Conclusion
• References
Group 7 2
3. REBOILER: Heat Exchanger
• Used with distillation columns to vaporise a
fraction of the bottom product
• Provide vapor flow up a column and acts as an
additional theoretical stage below the
trays/packing
Group 7 3
4. Fig. 2, Industrial reboiler, Ref. [2]
Fig. 1, Schematic of industrial reboiler, Ref. [1]
Group 7 4
Continued…
5. Types of reboilers
• Forced circulation
• Natural circulation (Thermosyphon)
• Kettle Type
Group 7 5
Fig. 3, Classification of reboiler
6. Forced Circulation Reboiler
• Designed to operate liquid
full
• Flashing occur as the liquid
crosses the control valve
• Valve should be located
close to the column shell
• Offer greater flexibility than
thermosyphons
• Elevation is less critical due
to pump and control valve Group 7 6
Fig. 4, Vertical Forced circulation reboiler
8. Thermosyphon reboilers
• Return piping to the
column must be sized for
two-phase flow
• Operates on
thermodynamic
principles, rather than
gravity
• Design detail is important
• Operation is simple, but
difficult to design for a
wide operating range
• Proper elevation is critical
Group 7 8
Fig. 6, Vertical thermosyphon reboiler
10. Kettle Type reboilers
• Vapor-Liquid disengagement
occurs in the vapor space,
therefore return piping is
sized for all-vapor flow.
• Proper elevation is critical
to kettle reboiler operation.
• Kettles have a large
footprint, but require less
elevation than a
thermosyphon.
• Works by gravity, rather
than thermodynamics.
Group 7 10
Fig. 9, Kettle reboilerc
11. Internal reboiler
• Boiling takes place in the
pool of liquid at the bottom
of the tower
• Boiler in conventional
distillation column
• Distillation column size gives
the limitations
• Part of every distillation
column
Group 7 11Fig. 10, Internal reboilercc
16. Case Study: Evaluation of reboiler temperature
retention time on MEG degradation products at
varying MEG concentrations
Paper specification
Year of publication: 31
July 2020
Journal: Journal of
Petroleum Science and
Engineering
Key words
MEG: Mono Ethylene
Glycol
Thermodynamic hydrate
inhibitor
Group 7 16
17. Problem statement
• MEG thermal degradation process can occur due to
dissociation to organic acids including glycolic, acetic
and formic acids.
Group 7 17
Fig. 12, Ref[6] Proposed dissociation products of ethylene glycol within oxygen
contamination under high temperature conditions
18. Methodology
1. Stock solution preparation
2. Distillation system
3. MEG concentration measurement (Refractometer)
4. Distillation calculations (9 internal configuration)
Group 7 18
20. Result and discussion
1. Effect of the reboiler temperature retention time on MEG
degradation products
Group 7 20
MEG degradation product increase percentage for different MEG concentrations
21. Continued…
2. Effect of the reboiler temperature on the total organic
acids accumulation
Group 7 21
22. Conclusion
• Operating the reboiler at higher temperatures to
achieve better separation by removing surplus water
and produce high purity lean MEG for offshore
recycling and reinjection at the wellhead
• However, this process results in an increase of
degraded MEG and will require further new
quantities of MEG to compensate the degraded MEG
Group 7 22
23. Reference
[1] Parisher, R. A., & Rhea, R. A. (2012). Mechanical
Equipment. Pipe Drafting and Design, 112–133.
doi:10.1016/b978-0-12-384700-3.00006-2
[2]https://www.arab-oil-naturalgas.com/what-are-reboiler-
types/
[3] wp.auburn.edu
[4] doi: 10.1615/AtoZ.r.reboilers
[5] doi:https://doi.org/10.1016/j.petrol.2020.107735
Group 7 23
24. [6] ROSSITER JR, W. J., BROWN, P. W. & GODETTE, M.
1983. The determination of acidic degradationproducts
in aqueous ethylene glycol and propylene glycol
solutions using ion chromatography. Solar Energy
Materials, 9, 267-279.
Group 7 24
Continued…