The CFD study of fluid flow in the CSTR with respect to the use of different types of impellers like PBTD,PBTU,RUSHTON etc..... With the help of ANSYS Fluent
This document discusses two-phase flow models and compares different pressure drop correlation methods. It begins with an introduction to two-phase flow and important variables like liquid holdup, gas void fraction, and slip velocity. It then describes the different flow patterns or regimes that can occur, including dispersed bubble, stratified smooth, wavy, slug, annular, and spray flows. The document outlines factors that affect flow patterns and discusses how patterns vary between horizontal, upward inclined, and downward inclined pipes. It concludes that selecting the most suitable correlation is key to accurately sizing pipelines for different applications.
This document summarizes a study that determined the bio-kinetic parameters for a sequencing batch reactor (SBR) type sewage treatment plant. Five bench-scale SBRs were operated under different biomass retention times ranging from 2 to 10 days. Samples from the influent, mixed liquor, and effluent were analyzed using standard methods. The study found that the kinetic parameters, including yield coefficient, organism decay rate, BOD removal rate, half velocity constant, and maximum specific growth rate, were within normal ranges for activated sludge. A higher sludge yield and lower organism decay showed that excess sludge production was high in the plants. The biomass retention time was determined to be a useful operating parameter instead of adjusting
This document discusses the classification and selection of chemical reactors. It outlines the basic types of reactors including batch, continuous stirred-tank (CSTR), and plug flow reactors (PFR). Selection of reactors depends on factors such as the process type (batch, continuous, catalytic), phase (gas, liquid, solid), and required mass and heat transfer rates. For example, batch reactors are used for small batch production while CSTRs are common for liquid reactions requiring mixing. PFRs provide higher efficiency and are used when significant heat transfer is needed. Selection also considers whether the reaction involves single or multiple steps.
VLE Data - Selection and Use
0 INTRODUCTION/PURPOSE
1 SCOPE
2 FIELD OF APPLICATION
3 DEFINITIONS
4 DIAGRAMMATIC REPRESENTATION OF IDEAL
AND NON-IDEAL SYSTEMS
4.1 Ideal Mixtures
4.2 Non-Ideal Mixtures
5 REVIEW OF VLE MODELS
5.1 Ideal Behavior in Both Phases
5.2 Liquid Phase Non-Idealities
5.3 High Pressure Systems
5.4 Special Models
6 SETTING UP A VLE MODEL
6.1 Define Problem
6.2 Select Data
6.3 Select Correlation(s)
6.4 Produce Model
7 AVOIDING PITFALLS
7.1 Experimental Data is Better than Estimates
7.2 Check Validity of Fitted Model
7.3 Check Limitations of Estimation Methods
7.4 Know Your System
7.5 Appreciate Errors and Effects
7.6 If in Doubt – Ask
8 A CASE STUDY
8.1 The Problem
8.2 The System
8.3 Data Available
8.4 Selected Correlation
8.5 Simulation
8.6 Selection of Model
9 RECOMMENDED READING
10 VLE EXPERTS IN GBHE
APPENDICES
A USE OF EXTENDED ANTOINE EQUATION
B USE OF WILSON EQUATION
C USEFUL METHODS OF ESTIMATING
D EQUATIONS OF STATE FOR VLE CALCULATIONS
TABLES
1 SUMMARY OF VLE METHODS
2 LIST OF USEFUL REFERENCES
FIGURES
1 VAPOR-LIQUID EQUILIBRIUM - IDEAL SOLUTION
BEHAVIOR
2 VAPOR-LIQUID EQUILIBRIUM - A GENERALISED
Y-X DIAGRAM
3 VAPOR-LIQUID EQUILIBRIUM - MINIMUM BOILING
AZEOTROPE
4 VAPOR-LIQUID EQUILIBRIUM - MAXIMUM BOILING
AZEOTROPE
5 VAPOR-LIQUID EQUILIBRIUM - MINIMUM BOILING
AZEOTROPE -TWO LIQUID PHASES
6 SENSITIVITY TO ERROR IN VLE DATA (BASED ON FENSKE EQUATION)
7(a) FITTING WILSON 'A' VALUES TO VLE DATA - CASE A
7(b) FITTING WILSON 'A' VALUES TO VLE DATA - CASE B
7(c) FITTING WILSON 'A' VALUES TO VLE DATA - CASE C
Solid Catalyzed Reactions
0 INTRODUCTION/PURPOSE
1 SCOPE
2 FIELD OF APPLICATION
3 DEFINITIONS
4 GENERAL BACKGROUND
4.1 General Considerations
5 SOLID CATALYZED GAS REACTIONS
5.1 Reaction Kinetics
5.2 Tests for Transport Limitations
5.3 Building a Reaction Kinetic Equation
6 INTRAPARTICLE
6.1 Types of Pore System
6.2 The Catalyst Effectiveness Factor
6.3 The Measurement of Effective Diffusivity
7 ENHANCEMENT OF INTRAPARTICLE
8 NOMENCLATURE
8.1 Dimensionless Parameters
8.2 Greek Letters
8.3 Subscripts
9 BIBLIOGRAPHY
9.1 Further Reading
APPENDICES
A LANGMUIR - HINSHELWOOD KINETICS
FIGURES
1 EFFECTIVE RATE CONSTANT
2 ITERATIVE APPROACH TO REACTOR MODEL
DEVELOPMENT
3 COMMON LABORATORY MICROREACTORS (FLOW TYPE)
4 THE BERTY REACTOR
5 STEPS IN BUILDING A REACTION RATE EQUATION
6 A CENTRAL-COMPOSITE DESIGN FOR TWO FACTORS
7 FIRST ORDER ISOTHERMAL IRREVERSIBLE
REACTION WITHIN A CATALYST SPHERE
8 INTEGRAL YIELD vs CONVERSION SHOWING EFFECT OF PELLET DIFFUSION
9 PREDICTED AND EXPERIMENTAL EFFECTIVENESS FACTORS
10 STRUCTURAL PERMEABILITY vs PRESSURE PARAMETER Z FOR BI-MODAL SUPPORTS
11 EFFECTIVENESS FACTOR vs THIELE MODULUS AND INTRAPARTICLE PECLET NUMBER
12 RELATIVE INCREASE IN CATALYST PERFORMANCE
Catalysis and catalytic reactions involve three main steps:
1. Adsorption of reactants onto the catalyst surface
2. Reaction of the adsorbed reactants on the surface
3. Desorption of products from the surface
Catalysts lower the activation energy of reactions, increasing their rates without being consumed. Common industrial catalytic reactions include cracking, isomerization, hydrogenation, and oxidation.
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
This document discusses two-phase flow models and compares different pressure drop correlation methods. It begins with an introduction to two-phase flow and important variables like liquid holdup, gas void fraction, and slip velocity. It then describes the different flow patterns or regimes that can occur, including dispersed bubble, stratified smooth, wavy, slug, annular, and spray flows. The document outlines factors that affect flow patterns and discusses how patterns vary between horizontal, upward inclined, and downward inclined pipes. It concludes that selecting the most suitable correlation is key to accurately sizing pipelines for different applications.
This document summarizes a study that determined the bio-kinetic parameters for a sequencing batch reactor (SBR) type sewage treatment plant. Five bench-scale SBRs were operated under different biomass retention times ranging from 2 to 10 days. Samples from the influent, mixed liquor, and effluent were analyzed using standard methods. The study found that the kinetic parameters, including yield coefficient, organism decay rate, BOD removal rate, half velocity constant, and maximum specific growth rate, were within normal ranges for activated sludge. A higher sludge yield and lower organism decay showed that excess sludge production was high in the plants. The biomass retention time was determined to be a useful operating parameter instead of adjusting
This document discusses the classification and selection of chemical reactors. It outlines the basic types of reactors including batch, continuous stirred-tank (CSTR), and plug flow reactors (PFR). Selection of reactors depends on factors such as the process type (batch, continuous, catalytic), phase (gas, liquid, solid), and required mass and heat transfer rates. For example, batch reactors are used for small batch production while CSTRs are common for liquid reactions requiring mixing. PFRs provide higher efficiency and are used when significant heat transfer is needed. Selection also considers whether the reaction involves single or multiple steps.
VLE Data - Selection and Use
0 INTRODUCTION/PURPOSE
1 SCOPE
2 FIELD OF APPLICATION
3 DEFINITIONS
4 DIAGRAMMATIC REPRESENTATION OF IDEAL
AND NON-IDEAL SYSTEMS
4.1 Ideal Mixtures
4.2 Non-Ideal Mixtures
5 REVIEW OF VLE MODELS
5.1 Ideal Behavior in Both Phases
5.2 Liquid Phase Non-Idealities
5.3 High Pressure Systems
5.4 Special Models
6 SETTING UP A VLE MODEL
6.1 Define Problem
6.2 Select Data
6.3 Select Correlation(s)
6.4 Produce Model
7 AVOIDING PITFALLS
7.1 Experimental Data is Better than Estimates
7.2 Check Validity of Fitted Model
7.3 Check Limitations of Estimation Methods
7.4 Know Your System
7.5 Appreciate Errors and Effects
7.6 If in Doubt – Ask
8 A CASE STUDY
8.1 The Problem
8.2 The System
8.3 Data Available
8.4 Selected Correlation
8.5 Simulation
8.6 Selection of Model
9 RECOMMENDED READING
10 VLE EXPERTS IN GBHE
APPENDICES
A USE OF EXTENDED ANTOINE EQUATION
B USE OF WILSON EQUATION
C USEFUL METHODS OF ESTIMATING
D EQUATIONS OF STATE FOR VLE CALCULATIONS
TABLES
1 SUMMARY OF VLE METHODS
2 LIST OF USEFUL REFERENCES
FIGURES
1 VAPOR-LIQUID EQUILIBRIUM - IDEAL SOLUTION
BEHAVIOR
2 VAPOR-LIQUID EQUILIBRIUM - A GENERALISED
Y-X DIAGRAM
3 VAPOR-LIQUID EQUILIBRIUM - MINIMUM BOILING
AZEOTROPE
4 VAPOR-LIQUID EQUILIBRIUM - MAXIMUM BOILING
AZEOTROPE
5 VAPOR-LIQUID EQUILIBRIUM - MINIMUM BOILING
AZEOTROPE -TWO LIQUID PHASES
6 SENSITIVITY TO ERROR IN VLE DATA (BASED ON FENSKE EQUATION)
7(a) FITTING WILSON 'A' VALUES TO VLE DATA - CASE A
7(b) FITTING WILSON 'A' VALUES TO VLE DATA - CASE B
7(c) FITTING WILSON 'A' VALUES TO VLE DATA - CASE C
Solid Catalyzed Reactions
0 INTRODUCTION/PURPOSE
1 SCOPE
2 FIELD OF APPLICATION
3 DEFINITIONS
4 GENERAL BACKGROUND
4.1 General Considerations
5 SOLID CATALYZED GAS REACTIONS
5.1 Reaction Kinetics
5.2 Tests for Transport Limitations
5.3 Building a Reaction Kinetic Equation
6 INTRAPARTICLE
6.1 Types of Pore System
6.2 The Catalyst Effectiveness Factor
6.3 The Measurement of Effective Diffusivity
7 ENHANCEMENT OF INTRAPARTICLE
8 NOMENCLATURE
8.1 Dimensionless Parameters
8.2 Greek Letters
8.3 Subscripts
9 BIBLIOGRAPHY
9.1 Further Reading
APPENDICES
A LANGMUIR - HINSHELWOOD KINETICS
FIGURES
1 EFFECTIVE RATE CONSTANT
2 ITERATIVE APPROACH TO REACTOR MODEL
DEVELOPMENT
3 COMMON LABORATORY MICROREACTORS (FLOW TYPE)
4 THE BERTY REACTOR
5 STEPS IN BUILDING A REACTION RATE EQUATION
6 A CENTRAL-COMPOSITE DESIGN FOR TWO FACTORS
7 FIRST ORDER ISOTHERMAL IRREVERSIBLE
REACTION WITHIN A CATALYST SPHERE
8 INTEGRAL YIELD vs CONVERSION SHOWING EFFECT OF PELLET DIFFUSION
9 PREDICTED AND EXPERIMENTAL EFFECTIVENESS FACTORS
10 STRUCTURAL PERMEABILITY vs PRESSURE PARAMETER Z FOR BI-MODAL SUPPORTS
11 EFFECTIVENESS FACTOR vs THIELE MODULUS AND INTRAPARTICLE PECLET NUMBER
12 RELATIVE INCREASE IN CATALYST PERFORMANCE
Catalysis and catalytic reactions involve three main steps:
1. Adsorption of reactants onto the catalyst surface
2. Reaction of the adsorbed reactants on the surface
3. Desorption of products from the surface
Catalysts lower the activation energy of reactions, increasing their rates without being consumed. Common industrial catalytic reactions include cracking, isomerization, hydrogenation, and oxidation.
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
Absorption & indusrial absorber,Gas Absorption,Equipments,Absorption in chemical Reaction,Absorption in Packed Tower,Absorption for counter current,Choice of Solvent,Continuous Contact Equipment,Height Equivalent to Theoretical Plate,HETP
Selection of Heat Exchanger Types
0 INTRODUCTION/PURPOSE
1 SCOPE
2 FIELD OF APPLICATION
3 DEFINITIONS
4 BACKGROUND
5 FACTORS INFLUENCING SELECTION
5.1 Type of Duty
5.2 Temperatures and Pressures
5.3 Materials of Construction 5.4 Fouling
5.5 Safety and Reliability
5.6 Repairs
5.7 Design Methods
5.8 Dimensions and Weight
5.9 Cost
5.10 GBHE Experience
6 TYPES OF EXCHANGER
6.1 Shell and Tube Exchangers
6.2 Cylindrical Graphite Block Heat Exchangers
6.3 Cubic Graphite Block Heat Exchangers
6.4 Air Cooled Heat Exchangers
6.5 Gasketed Plate and Frame
6.6 Spiral Plate
6.7 Tube in Duct
6.8 Plate-fin
6.9 Printed Circuit Heat Exchanger (PCHE)
6.10 Scraped Surface/Wiped Film Exchangers
6.11 Welded or Brazed Plate
6.12 Double Pipe
6.13 Electric Heaters
6.14 Fired Process Heaters
TABLE
(1) ADVANTAGES AND DISADVANTAGES OF DIFFERENT SHELL AND TUBE DESIGNS
FIGURES
1 ESTIMATED MAIN PLANT ITEM COSTS
2 ESTIMATED INSTALLED COSTS
3 TEMA HEAT EXCHANGER NOMENCLATURE
4 F ‘CORRECTION FACTORS' : TEMA E SHELL WITH EVEN NUMBER OF PASSE
5 SHELL AND TUBE HEAT EXCHANGER HEAD TYPES
6 GENERAL ARRANGEMENT OF A CYLINDRICAL GRAPHITE BLOCK HEAT EXCHANGER
7 EXPLODED VIEW OF A CUBIC GRAPHITE BLOCK
HEAT EXCHANGER
8 TYPICAL AIR COOLED HEAT EXCHANGER
9 GENERAL VIEW OF ONE END OF A 3-STREAM
PLATE-FIN HEAT EXCHANGER
10 TYPICAL PCHE PLATE
11 VICARB ‘COMPABLOC' EXCHANGER
12 ‘BROWN FINTUBE' MULTITUBE HEAT EXCHANGER
13 FIRED HEATER : SCHEMATICS AND NOMENCLATURE
Design and Simulation of Continuous Distillation ColumnsGerard B. Hawkins
Design and Simulation of Continuous Distillation Columns
0 INTRODUCTION/PURPOSE
1 SCOPE
2 FIELD OF APPLICATION
3 DEFINITIONS
4 FRACTIONAL DISTILLATION
5 ROUGH METHOD OF COLUMN DESIGN
5.1 Sharp Separations
5.2 Sloppy Separations
6 DETAIL DESIGN USING THE CHEMCAD DISTILLATION PROGRAM
6.1 Sharp Separations
6.2 Sloppy Separations
7 COMPLEX COLUMNS
7.1 Multiple Feeds
7.2 Sidestream Take-Offs
8 DESIGN USING A LABORATORY COLUMN
SIMULATION
9 DESIGN USING ACTUAL PLANT DATA
9.1 Uprating or Debottlenecking Exercises
10 REFERENCES
APPENDICES
A WORKED EXAMPLE
B SLOPPY SEPARATIONS
C SIMULATION USING PLANT DATA : CASE HISTORIES
TABLES
Biomass gasification for hydrogen productionMd Tanvir Alam
Biomass gasification can be used to produce hydrogen fuel through thermal conversion processes. Gasification involves heating biomass with limited oxygen to produce syngas containing hydrogen, carbon monoxide, and other gases. Several pathways exist to convert biomass to hydrogen through gasification. Research has demonstrated hydrogen yields of up to 60% by volume from biomass gasification using fluidized beds and catalysts. Economic analyses show biomass gasification can competitively produce hydrogen compared to natural gas reforming. With environmental and economic benefits, biomass gasification is a promising option for renewable hydrogen production.
BY AMIT SHAH & SOHAM MULE, F.Y.B. PHARM, KMKCP.
PTC (PHASE TRANSFER CATALYSIS) A SMALL TOPIC IN 2ND SEMESTER OF B.PHARM IN POC - 1 UNDER THE TOPIC SN REACTIONS. PTC FAVOURS SN2 REACTIONS.
The McCabe-Thiele method is a graphical technique for determining the minimum number of stages required for distillation. It involves plotting the equilibrium relationship between liquid and vapor phases on a diagram and constructing operating lines to represent the mass balances in the rectifying and stripping sections. Intersections between the lines indicate the number of ideal stages. The method was developed in 1925 and remains useful for preliminary column design. Key considerations include the feed composition and enthalpy, reflux ratio, and use of partial condensers or reboilers.
This document discusses various types of chemical reactors. It begins by defining a reactor as a vessel designed to contain chemical reactions. It then covers basic design principles like reaction type and factors influencing reaction rate. It describes several reactor types classified by mode of operation (batch, continuous, semi-batch), end use application (polymerization, bio, electrochemical), number of phases, and whether a catalyst is used. Specific reactor types covered include CSTR, plug flow, tubular flow, and fixed bed. The document also discusses catalysis, including homogeneous vs heterogeneous catalysts and common catalyst types.
Hydrogenation Reactors
Stirred Vessels
Loop Reactors
Other reactor types
Appendix
- List of contact details for suppliers
- Information from supplier’s websites
1. The document derives a general differential equation for fluid flow problems in rectangular Cartesian coordinates using a shell momentum balance.
2. It considers flow between parallel plates where the velocity depends only on the x-coordinate and derives expressions for the shear stress distribution, velocity profile, maximum velocity, average velocity, and mass flow rate for a Newtonian fluid.
3. The shear stress is found to be linearly proportional to x, the velocity profile parabolic, the maximum velocity occurs at the center, and the average velocity is 2/3 of the maximum velocity.
The document discusses the McCabe-Thiele design method for distillation column design using vapor-liquid equilibrium (VLE) data. It explains that the McCabe-Thiele method uses a graphical approach to determine the theoretical number of stages required for a binary separation based on the VLE plot. Operating lines are drawn on the VLE diagram to define the mass balance relationships between the liquid and vapor phases. The operating line for the rectification section is constructed by drawing a line with slope R/(R+1) from the desired top product composition point, where R is the reflux ratio. The operating line for the stripping section has a slope of Ls/Vs, where Ls and Vs are the liquid and
Common poisons include
Sulfur
Chlorides and other halides
Metals including arsenic, vanadium, mercury, alkali metals (including potassium)
Phosphates
Organo-metalics
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.
The document discusses key concepts in multicomponent distillation including:
- Key components are chosen to indicate separation and are always distributed between products.
- The Fenske equation is used to determine minimum number of stages assuming constant relative volatility, while the Underwood method determines minimum reflux ratio.
- The Gilliland correlation estimates actual number of stages given operating reflux from minimum values.
Packed columns are used for distillation, gas absorption, and liquid-liquid extraction. They have continuous gas-liquid contact through a packed bed, unlike plate columns which have stage-wise contact. Packed columns depend on good liquid and gas distribution, and have lower holdup but higher pressure drop than plate columns. This document provides details on packed column components, design procedures such as selecting packing and determining height, and examples of absorption and stripping processes in packed columns.
Chemical reaction engineering is that engineering activity which is concerned with the exploitation of chemical reactions on commercial scale.
The areas of different fields of science like:
Oil Refining
Pharmaceuticals
Biotechnology
Chemical Industries
Sustainable Development
L09-Separations and Column Simulation.pptxKAhmedRehman
This document provides an overview of distillation columns and separation train design. It discusses different types of distillation columns including plate columns with bubble cap trays and sieve trays, and packed columns. It also covers concepts like equilibrium lines, operating lines, minimum reflux ratio, and McCabe-Thiele diagrams. The document discusses methods for determining the number of columns needed, possible sequences, and how to evaluate sequences using the marginal vapor rate method. Finally, it provides heuristics for sequencing separation points in a distillation train.
Selection and Design of Condensers
0 INTRODUCTION/PURPOSE
1 SCOPE
2 FIELD OF APPLICATION
3 DEFINITIONS
4 CHOICE OF COOLANT
5 LAYOUT CONSIDERATIONS
5.1 Distillation Column Condensers
5.2 Other Process Condensers
6 CONTROL
6.1 Distillation Columns
6.2 Water Cooled Condensers
6.3 Refrigerant Condensers
7 GENERAL DESIGN CONSIDERATIONS
7.1 Heat Transfer Resistances
7.2 Pressure Drop
7.3 Handling of Inerts
7.4 Vapor Inlet Design
7.5 Drainage of Condensate
8 SUMMARY OF TYPES AVAILABLE
8.1 Direct Contact Condensers
8.2 Shell and Tube Exchangers
8.3 Air Cooled Heat Exchangers
8.4 Spiral Plate Heat Exchangers
8.5 Internal Condensers
8.6 Plate Heat Exchangers
8.7 Plate-Fin Heat Exchangers
8.8 Other Compact Designs
9 BIBLIOGRAPHY
FIGURES
1 DIRECT CONTACT CONDENSER WITH INDIRECT COOLER FOR RECYCLED CONDENSATE
2 SPRAY CONDENSER
3 TRAY TYPE CONDENSER
4 THREE PASS TUBE SIDE CONDENSER WITH INTERPASS LUTING FOR CONDENSATE DRAINAGE
5 CROSS FLOW CONDENSER WITH SINGLE PASS COOLANT
This document provides an overview of sour water stripping, including sources and characteristics of sour water from various industrial processes like sour gas processing, oil refining, gasification, and Claus tail gas treating. It discusses sour water from each of these processes and common approaches to sour water management, including stripping, feed preparation, and offgas disposal. Key aspects covered include produced water vs condensed water in sour gas processing, challenges with different contaminants in refinery sour water, integrated sour water stripping with tail gas units, and ammonia removal processes from coal gasification sour water.
International Journal of Engineering Research and Applications (IJERA) is a team of researchers not publication services or private publications running the journals for monetary benefits, we are association of scientists and academia who focus only on supporting authors who want to publish their work. The articles published in our journal can be accessed online, all the articles will be archived for real time access.
Our journal system primarily aims to bring out the research talent and the works done by sciaentists, academia, engineers, practitioners, scholars, post graduate students of engineering and science. This journal aims to cover the scientific research in a broader sense and not publishing a niche area of research facilitating researchers from various verticals to publish their papers. It is also aimed to provide a platform for the researchers to publish in a shorter of time, enabling them to continue further All articles published are freely available to scientific researchers in the Government agencies,educators and the general public. We are taking serious efforts to promote our journal across the globe in various ways, we are sure that our journal will act as a scientific platform for all researchers to publish their works online.
IRJET-A Review on Advances in the Design and Analysis of Draft Tube for React...IRJET Journal
This document reviews research on the design and analysis of draft tubes for reaction turbines. It discusses how computational fluid dynamics (CFD) has been used by researchers to optimize draft tube design and predict turbine performance. The document outlines several studies that have used CFD to simulate draft tube flow and analyze the effects of design parameters like length and angle on performance. It concludes that CFD is an effective tool for draft tube analysis that can save resources and time compared to physical testing during the design phase.
Absorption & indusrial absorber,Gas Absorption,Equipments,Absorption in chemical Reaction,Absorption in Packed Tower,Absorption for counter current,Choice of Solvent,Continuous Contact Equipment,Height Equivalent to Theoretical Plate,HETP
Selection of Heat Exchanger Types
0 INTRODUCTION/PURPOSE
1 SCOPE
2 FIELD OF APPLICATION
3 DEFINITIONS
4 BACKGROUND
5 FACTORS INFLUENCING SELECTION
5.1 Type of Duty
5.2 Temperatures and Pressures
5.3 Materials of Construction 5.4 Fouling
5.5 Safety and Reliability
5.6 Repairs
5.7 Design Methods
5.8 Dimensions and Weight
5.9 Cost
5.10 GBHE Experience
6 TYPES OF EXCHANGER
6.1 Shell and Tube Exchangers
6.2 Cylindrical Graphite Block Heat Exchangers
6.3 Cubic Graphite Block Heat Exchangers
6.4 Air Cooled Heat Exchangers
6.5 Gasketed Plate and Frame
6.6 Spiral Plate
6.7 Tube in Duct
6.8 Plate-fin
6.9 Printed Circuit Heat Exchanger (PCHE)
6.10 Scraped Surface/Wiped Film Exchangers
6.11 Welded or Brazed Plate
6.12 Double Pipe
6.13 Electric Heaters
6.14 Fired Process Heaters
TABLE
(1) ADVANTAGES AND DISADVANTAGES OF DIFFERENT SHELL AND TUBE DESIGNS
FIGURES
1 ESTIMATED MAIN PLANT ITEM COSTS
2 ESTIMATED INSTALLED COSTS
3 TEMA HEAT EXCHANGER NOMENCLATURE
4 F ‘CORRECTION FACTORS' : TEMA E SHELL WITH EVEN NUMBER OF PASSE
5 SHELL AND TUBE HEAT EXCHANGER HEAD TYPES
6 GENERAL ARRANGEMENT OF A CYLINDRICAL GRAPHITE BLOCK HEAT EXCHANGER
7 EXPLODED VIEW OF A CUBIC GRAPHITE BLOCK
HEAT EXCHANGER
8 TYPICAL AIR COOLED HEAT EXCHANGER
9 GENERAL VIEW OF ONE END OF A 3-STREAM
PLATE-FIN HEAT EXCHANGER
10 TYPICAL PCHE PLATE
11 VICARB ‘COMPABLOC' EXCHANGER
12 ‘BROWN FINTUBE' MULTITUBE HEAT EXCHANGER
13 FIRED HEATER : SCHEMATICS AND NOMENCLATURE
Design and Simulation of Continuous Distillation ColumnsGerard B. Hawkins
Design and Simulation of Continuous Distillation Columns
0 INTRODUCTION/PURPOSE
1 SCOPE
2 FIELD OF APPLICATION
3 DEFINITIONS
4 FRACTIONAL DISTILLATION
5 ROUGH METHOD OF COLUMN DESIGN
5.1 Sharp Separations
5.2 Sloppy Separations
6 DETAIL DESIGN USING THE CHEMCAD DISTILLATION PROGRAM
6.1 Sharp Separations
6.2 Sloppy Separations
7 COMPLEX COLUMNS
7.1 Multiple Feeds
7.2 Sidestream Take-Offs
8 DESIGN USING A LABORATORY COLUMN
SIMULATION
9 DESIGN USING ACTUAL PLANT DATA
9.1 Uprating or Debottlenecking Exercises
10 REFERENCES
APPENDICES
A WORKED EXAMPLE
B SLOPPY SEPARATIONS
C SIMULATION USING PLANT DATA : CASE HISTORIES
TABLES
Biomass gasification for hydrogen productionMd Tanvir Alam
Biomass gasification can be used to produce hydrogen fuel through thermal conversion processes. Gasification involves heating biomass with limited oxygen to produce syngas containing hydrogen, carbon monoxide, and other gases. Several pathways exist to convert biomass to hydrogen through gasification. Research has demonstrated hydrogen yields of up to 60% by volume from biomass gasification using fluidized beds and catalysts. Economic analyses show biomass gasification can competitively produce hydrogen compared to natural gas reforming. With environmental and economic benefits, biomass gasification is a promising option for renewable hydrogen production.
BY AMIT SHAH & SOHAM MULE, F.Y.B. PHARM, KMKCP.
PTC (PHASE TRANSFER CATALYSIS) A SMALL TOPIC IN 2ND SEMESTER OF B.PHARM IN POC - 1 UNDER THE TOPIC SN REACTIONS. PTC FAVOURS SN2 REACTIONS.
The McCabe-Thiele method is a graphical technique for determining the minimum number of stages required for distillation. It involves plotting the equilibrium relationship between liquid and vapor phases on a diagram and constructing operating lines to represent the mass balances in the rectifying and stripping sections. Intersections between the lines indicate the number of ideal stages. The method was developed in 1925 and remains useful for preliminary column design. Key considerations include the feed composition and enthalpy, reflux ratio, and use of partial condensers or reboilers.
This document discusses various types of chemical reactors. It begins by defining a reactor as a vessel designed to contain chemical reactions. It then covers basic design principles like reaction type and factors influencing reaction rate. It describes several reactor types classified by mode of operation (batch, continuous, semi-batch), end use application (polymerization, bio, electrochemical), number of phases, and whether a catalyst is used. Specific reactor types covered include CSTR, plug flow, tubular flow, and fixed bed. The document also discusses catalysis, including homogeneous vs heterogeneous catalysts and common catalyst types.
Hydrogenation Reactors
Stirred Vessels
Loop Reactors
Other reactor types
Appendix
- List of contact details for suppliers
- Information from supplier’s websites
1. The document derives a general differential equation for fluid flow problems in rectangular Cartesian coordinates using a shell momentum balance.
2. It considers flow between parallel plates where the velocity depends only on the x-coordinate and derives expressions for the shear stress distribution, velocity profile, maximum velocity, average velocity, and mass flow rate for a Newtonian fluid.
3. The shear stress is found to be linearly proportional to x, the velocity profile parabolic, the maximum velocity occurs at the center, and the average velocity is 2/3 of the maximum velocity.
The document discusses the McCabe-Thiele design method for distillation column design using vapor-liquid equilibrium (VLE) data. It explains that the McCabe-Thiele method uses a graphical approach to determine the theoretical number of stages required for a binary separation based on the VLE plot. Operating lines are drawn on the VLE diagram to define the mass balance relationships between the liquid and vapor phases. The operating line for the rectification section is constructed by drawing a line with slope R/(R+1) from the desired top product composition point, where R is the reflux ratio. The operating line for the stripping section has a slope of Ls/Vs, where Ls and Vs are the liquid and
Common poisons include
Sulfur
Chlorides and other halides
Metals including arsenic, vanadium, mercury, alkali metals (including potassium)
Phosphates
Organo-metalics
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.
The document discusses key concepts in multicomponent distillation including:
- Key components are chosen to indicate separation and are always distributed between products.
- The Fenske equation is used to determine minimum number of stages assuming constant relative volatility, while the Underwood method determines minimum reflux ratio.
- The Gilliland correlation estimates actual number of stages given operating reflux from minimum values.
Packed columns are used for distillation, gas absorption, and liquid-liquid extraction. They have continuous gas-liquid contact through a packed bed, unlike plate columns which have stage-wise contact. Packed columns depend on good liquid and gas distribution, and have lower holdup but higher pressure drop than plate columns. This document provides details on packed column components, design procedures such as selecting packing and determining height, and examples of absorption and stripping processes in packed columns.
Chemical reaction engineering is that engineering activity which is concerned with the exploitation of chemical reactions on commercial scale.
The areas of different fields of science like:
Oil Refining
Pharmaceuticals
Biotechnology
Chemical Industries
Sustainable Development
L09-Separations and Column Simulation.pptxKAhmedRehman
This document provides an overview of distillation columns and separation train design. It discusses different types of distillation columns including plate columns with bubble cap trays and sieve trays, and packed columns. It also covers concepts like equilibrium lines, operating lines, minimum reflux ratio, and McCabe-Thiele diagrams. The document discusses methods for determining the number of columns needed, possible sequences, and how to evaluate sequences using the marginal vapor rate method. Finally, it provides heuristics for sequencing separation points in a distillation train.
Selection and Design of Condensers
0 INTRODUCTION/PURPOSE
1 SCOPE
2 FIELD OF APPLICATION
3 DEFINITIONS
4 CHOICE OF COOLANT
5 LAYOUT CONSIDERATIONS
5.1 Distillation Column Condensers
5.2 Other Process Condensers
6 CONTROL
6.1 Distillation Columns
6.2 Water Cooled Condensers
6.3 Refrigerant Condensers
7 GENERAL DESIGN CONSIDERATIONS
7.1 Heat Transfer Resistances
7.2 Pressure Drop
7.3 Handling of Inerts
7.4 Vapor Inlet Design
7.5 Drainage of Condensate
8 SUMMARY OF TYPES AVAILABLE
8.1 Direct Contact Condensers
8.2 Shell and Tube Exchangers
8.3 Air Cooled Heat Exchangers
8.4 Spiral Plate Heat Exchangers
8.5 Internal Condensers
8.6 Plate Heat Exchangers
8.7 Plate-Fin Heat Exchangers
8.8 Other Compact Designs
9 BIBLIOGRAPHY
FIGURES
1 DIRECT CONTACT CONDENSER WITH INDIRECT COOLER FOR RECYCLED CONDENSATE
2 SPRAY CONDENSER
3 TRAY TYPE CONDENSER
4 THREE PASS TUBE SIDE CONDENSER WITH INTERPASS LUTING FOR CONDENSATE DRAINAGE
5 CROSS FLOW CONDENSER WITH SINGLE PASS COOLANT
This document provides an overview of sour water stripping, including sources and characteristics of sour water from various industrial processes like sour gas processing, oil refining, gasification, and Claus tail gas treating. It discusses sour water from each of these processes and common approaches to sour water management, including stripping, feed preparation, and offgas disposal. Key aspects covered include produced water vs condensed water in sour gas processing, challenges with different contaminants in refinery sour water, integrated sour water stripping with tail gas units, and ammonia removal processes from coal gasification sour water.
International Journal of Engineering Research and Applications (IJERA) is a team of researchers not publication services or private publications running the journals for monetary benefits, we are association of scientists and academia who focus only on supporting authors who want to publish their work. The articles published in our journal can be accessed online, all the articles will be archived for real time access.
Our journal system primarily aims to bring out the research talent and the works done by sciaentists, academia, engineers, practitioners, scholars, post graduate students of engineering and science. This journal aims to cover the scientific research in a broader sense and not publishing a niche area of research facilitating researchers from various verticals to publish their papers. It is also aimed to provide a platform for the researchers to publish in a shorter of time, enabling them to continue further All articles published are freely available to scientific researchers in the Government agencies,educators and the general public. We are taking serious efforts to promote our journal across the globe in various ways, we are sure that our journal will act as a scientific platform for all researchers to publish their works online.
IRJET-A Review on Advances in the Design and Analysis of Draft Tube for React...IRJET Journal
This document reviews research on the design and analysis of draft tubes for reaction turbines. It discusses how computational fluid dynamics (CFD) has been used by researchers to optimize draft tube design and predict turbine performance. The document outlines several studies that have used CFD to simulate draft tube flow and analyze the effects of design parameters like length and angle on performance. It concludes that CFD is an effective tool for draft tube analysis that can save resources and time compared to physical testing during the design phase.
Review on Recent Advances in Pulse Detonation EnginesBBIT Kolkata
Pulse detonation engines (PDEs) are new exciting propulsion technologies for future propulsion applications. The operating cycles
of PDE consist of fuel-air mixture, combustion, blowdown, and purging. The combustion process in pulse detonation engine is the
most important phenomenon as it produces reliable and repeatable detonation waves.The detonation wave initiation in detonation
tube in practical system is a combination of multistage combustion phenomena. Detonation combustion causes rapid burning of
fuel-air mixture, which is a thousand times faster than deflagration mode of combustion process. PDE utilizes repetitive detonation
wave to produce propulsion thrust. In the present paper, detailed review of various experimental studies and computational analysis
addressing the detonation mode of combustion in pulse detonation engines are discussed. The effect of different parameters on
the improvement of propulsion performance of pulse detonation engine has been presented in detail in this research paper. It is
observed that the design of detonation wave flow path in detonation tube, ejectors at exit section of detonation tube, and operating
parameters such as Mach numbers aremainly responsible for improving the propulsion performance of PDE. In the present review
work, further scope of research in this area has also been suggested.
2018 - CFD simulation of fluid dynamic and biokinetic processes within activa...WALEBUBLÉ
This document describes a CFD simulation of fluid dynamics and biokinetic processes within an activated sludge reactor (ASR) operating under intermittent aeration. The CFD model considers fluid dynamics, oxygen transfer, and biological processes described by Activated Sludge Model No. 1 (ASM1). The model is used to evaluate two different aeration system configurations for an ASR in terms of their ability to satisfy effluent requirements with minimum energy consumption. Results show that modifying the air diffuser layout can improve energy consumption by 2.8%, and reducing the air flow rate per diffuser improves energy consumption by 14.5%. The model provides insight into aeration inefficiencies within ASRs.
This document reports on a numerical investigation of a jet pump with twisted tapes. Water and air were used as the primary and secondary fluids, respectively. Computational fluid dynamics software was used to simulate flow through nozzles with diameters of 4mm and 6mm, both with and without single or double twisted tapes. Results found that double twisted tapes increased efficiency the most by enhancing momentum exchange and pressure drop after the nozzle through increased vorticity. Velocity, turbulent kinetic energy, and vorticity profiles along the length supported these findings. The maximum 10% efficiency increase was with a double twisted tape compared to no tape.
The effect of rotational speed variation on the velocity vectors in the singl...IOSR Journals
This document summarizes a study that uses computational fluid dynamics (CFD) to simulate the internal flow in a centrifugal pump with varying rotational speeds. The study models a single blade passage of a five-bladed centrifugal pump impeller to accurately predict velocity vectors on the blade, hub, and shroud. Results show that at higher rotational speeds above the design point, velocity vectors increase more gradually until reaching a maximum value at the leading edge of the blade. The analysis concludes that velocity vectors in the suction side remain approximately constant, but increase to a higher maximum at the leading edge as rotational speed increases, especially above the design point.
This document summarizes a numerical study on the effect of discharge coefficient on the performance of a six jet Pelton turbine model. Computational fluid dynamics (CFD) was used to analyze the turbine's performance at design and off-design discharge conditions. The CFD results for efficiency were compared to available model test data and found to be in close agreement. Pressure distribution, water velocity, and water distribution within the turbine were also obtained from the CFD simulations and discussed. The study aims to provide a cost-effective tool for detailed flow analysis and performance evaluation of Pelton turbines at different operating conditions.
Experiments and numerical simulations were conducted to study the flow field of an array of axial-flow marine hydrokinetic turbines operating in a flume. Particle image velocimetry and rotor torque measurements were collected from the experiments and compared to computational fluid dynamics simulations using Reynolds-averaged Navier-Stokes and large eddy simulation models. The simulations captured some wake characteristics accurately but differed from particle image velocimetry in their representation of the near wake and nacelle effects. Adding turbulent inflow to the large eddy simulation improved the realism of the wake behavior observed in experiments and other studies.
8-Characterization of Tidal Current Turbine Dynamics Using Fluid Structure In...UMAIRKHALID118334
This document summarizes research on characterizing the dynamics of tidal current turbines (TCT) using fluid structure interaction (FSI) modeling. A 3-bladed horizontal axis TCT was modeled and analyzed using computational fluid dynamics (CFD) to model the fluid flow. Blade element momentum (BEM) modeling was used to design the turbine blades. FSI was used to transfer pressure loads from CFD to a finite element model (FEM) to analyze the structural response. Modal, pre-stressed vibration, and forced vibration analyses were performed on the FEM to investigate the structural response and dynamic behavior of the TCT under operating conditions. The results from CFD and BEM showed good agreement. Modal
Design & Analysis of a Helical Cross Flow TurbineAnish Anand
We investigate the flow past a cross flow hydrokinetic turbine (CFHT)in which a helical blade turns around a shaft perpendicular to the free stream under the hydrodynamic forces exerted by the flow. The ability of a cross flow turbine to rotate in the same direction independent of the water flow direction gives an advantage for hydrokinetic applications.
This type of turbine, while very different from the classical horizontal axis turbine commonly used in the wind energy field, presents advantages in the context of hydro kinetic energy harvesting, such as independence from current direction, including reversibility, stacking, and self-starting without complex pitch mechanisms.
This document discusses a numerical study on the effect of jet shape on the flow and torque characteristics of a Pelton turbine runner. Four different jet shapes - circular, triangular, square and elliptical - were simulated using computational fluid dynamics (CFD) software, keeping the cross-sectional area of the jets constant. The results showed that the circular jet produced the highest hydraulic efficiency of 88.03%, distributing water most uniformly across the buckets. The triangular and square jets did not allow complete emptying of buckets before the next jet arrived, reducing efficiency. The elliptical jet had the lowest efficiency of 77.80%. In conclusion, circular jets were found to be most efficient for Pelton turbines.
IJRET : International Journal of Research in Engineering and Technology is an international peer reviewed, online journal published by eSAT Publishing House for the enhancement of research in various disciplines of Engineering and Technology. The aim and scope of the journal is to provide an academic medium and an important reference for the advancement and dissemination of research results that support high-level learning, teaching and research in the fields of Engineering and Technology. We bring together Scientists, Academician, Field Engineers, Scholars and Students of related fields of Engineering and Technology
This document summarizes research on the numerical and experimental study of the effect of impeller design on the performance of submerged turbines. A Gorlov helical water turbine was designed, fabricated, and tested both theoretically using computational fluid dynamics software and experimentally in an open channel. The experimental results showed that power increased with water velocity, reaching 4.621 W at a velocity of 1.81 m/s. CFD modeling using Fluent agreed well with experimental results. The study evaluated turbine performance at various water velocities to optimize power extraction based on impeller design.
The document discusses preliminary studies evaluating oscillatory flow technology (OFT) in miniaturized channels with diameters around 1mm. Theoretical analysis predicts increased Nusselt numbers, a measure of heat transfer, for OFT in minichannels compared to smooth pipes at equivalent energy dissipation. Experimental testing of a newly constructed system will evaluate momentum, heat, and mass transfer performance of OFT in minichannels relative to both smooth pipes and other minifluidic devices. Future work will design mini-fluidic channels optimized for oscillatory flow and test them experimentally.
IRJET - Kinetic Model on the Performance of an Anaerobic Baffled Reactor for ...IRJET Journal
The document describes a study that evaluated the performance of an anaerobic baffled reactor (ABR) in treating textile wastewater at different hydraulic retention times (HRTs). Three kinetic models - first order, cubic polynomial, and quadratic polynomial - were applied to determine the substrate removal kinetics in the ABR. The cubic polynomial model provided the best fit with the experimental data, accurately predicting the chemical oxygen demand (COD) concentrations with correlation coefficients ranging from 0.9543 to 0.9999. This shows that the cubic polynomial model is suitable for describing organic removal kinetics in an ABR system treating real textile dye wastewater.
This document provides a course plan for a class on Gas Dynamics and Jet Propulsion taught by Mr. R. Deepak at KIT-Kalaignar Karunanidhi Institute of Technology. The course covers 5 units: basic concepts and isentropic flows, flow through ducts, normal and oblique shocks, jet propulsion, and space propulsion. The course aims to help students understand compressible flow, shock waves, and jet and rocket propulsion. It includes learning objectives, outcomes, assignments, exams, reference materials and an evaluation plan following Anna University guidelines.
The effect of rotational speed variation on the static pressure in the centri...IOSR Journals
1) A numerical simulation was conducted to examine the effect of rotational speed variation on static pressure in a centrifugal pump.
2) Contours of static pressure on the blade, hub, and shroud were generated at rotational speeds of 1800 rpm to 2400 rpm.
3) The results show that static pressure is lowest on the suction side and increases towards the leading edge of the blade. Negative static pressure occurs at high rotational speeds over design limits, risking cavitation.
i. Introduction:
ii. Definition of Turbo machine,
iii. Parts of Turbo machines,
iv. Comparison with positive displacement machines,
v. Classification of Turbo machine,
vi. Dimensionless parameters and their significance,
vii. Unit and specific quantities,
viii. Model studies and its numerical.
(Note: Since dimensional analysis is covered in Fluid Mechanics subject, questions on dimensional analysis may not be given. However, dimensional parameters and model studies may be given more weightage.)
Simple Numerical; on Model Analysis.
previous year question papers solved
Runner profile optimisation of gravitational vortex water turbine IJECEIAES
This study discusses the numerical optimisation and performance testing of the turbine runner profile for the designed gravitational water vortex turbine. The initial design of the turbine runner is optimised using a surface vorticity algorithm coded in MATLAB to obtain the optimal stagger angle. Design validation is carried out using computational fluid dynamics (CFD) Ansys CFX to determine the performance of the turbine runner with the turbulent shear stress transport model. The CFD analysis shows that by optimising the design, the water turbine efficiency increases by about 2.6%. The prototype of the vortex turbine runner is made using a 3D printing machine with resin material. It is later tested in a laboratory-scale experiment that measures the shaft power, shaft torque and turbine efficiency in correspondence with rotational speeds varying from 150 to 650 rpm. Experiment results validate that the optimised runner has an efficiency of 45.3% or about 14% greater than the initial design runner, which has an efficiency of 39.7%.
The need for high pump performance and efficiency continue to encourage the study of flow between two parallel co-rotating discs in multiple discs pump or turbine. Therefore, this study entails the design, construction and CFD simulation of a 3D Tesla pump model axisymmetric swirling flow in order to enhance the understanding of Tesla pump for future development.
Method of solution entails designing and construction of a small prototype tesla pump and then using the design geometry and parameters to design and perform numerical simulation. The results of the numerical simulation were then analyzed.
The result obtained indicates static pressure to have minimum value of -4.7791Pa at the outlet and 13.777Pa at the pump inlet and with velocity magnitude having minimum velocity of 0.00m/s and maximum velocity of 4.12m/s. The strength of the velocity was seen to be very high at the pump outlet. The analysis radial velocity showed minimum value of -0.508m/s and maximum value of 3.981m/s with the radial velocity vector being concentrated at the discs periphery and outlet.
Model simulation results exhibited smooth pressure and velocity profiles. With the 3D simulation all flow variables are able to be predicted.
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1) The document outlines a CFD study of different impellers - PBTD, PBTU, and Rushton turbine - in a continuous stirred tank reactor (CSTR) with and without baffles.
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This document discusses conducting polymers. It describes two types of conducting polymers: intrinsically conducting polymers which have conjugation in their backbone providing conductivity, and extrinsically conducting polymers which require external ingredients like carbon black to become conductive. Doping can increase the conductivity of polymers by removing or inserting electrons. Conducting polymers have applications in anti-static coatings, corrosion inhibition, capacitors, smart windows, transistors, LEDs and solar cells. While manufacturing costs are high, conducting polymers could enable flexible transparent displays and be used in biomedical applications if issues like toxicity and processing are addressed.
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Atomic absorption spectroscopy is a technique for detecting metals and metalloids in samples. It works by atomizing the sample using a flame or graphite furnace and measuring the absorption of light from a hollow cathode lamp containing the element being analyzed. A calibration curve relating the absorption measurements to known standards is used to determine the concentration of the element in samples. The technique is simple, reliable, and can analyze over 62 different elements.
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Cfd study of cstr for different impellers
1. PICE 2017
Hosted at Department of Chemical Engineering
AISSMS COE, Pune-1
26 March 2017
Justin K George ,Dr. Vivek Vitankar, Dr. Kanhaiya R Jethani
Department of Chemical Engineering
AISSMS COE, Pune-1
2. Contents
Introduction
Objective
PBTD Impeller Without Baffle
PBTD impeller With Baffle
Comparative Study of PBTD With & Without Baffle
PBTU Impeller
Rushton Turbine
Conclusions
References
3. Fluid flows are governed by partial differential equations
CFD is the art of replacing PDE systems by a set of algebraic
equations
CFD provides a qualitative (and quantitative) prediction of fluid
flows by
• mathematical modeling (partial differential equations)
• numerical methods ( discretization and solution techniques)
• software tools (solvers ,pre-and post processing utilities)
Introduction
4. Objective
• Detailed study of flow in
PBTD Impeller Vessel without baffle
PBTD impeller with baffle
Role of baffle in Mixing
PBTU Impeller Vessel
Rushton Turbine Vessel
with the help of CFD .
5. Parameters Dimensions
Tank diameter, T 0.5 m
Impeller diameter, D 0.17 m
Clearance, C 0.165 m
Height of liquid, H 0.5 m
Baffle width, Bw 0.05 m
Baffle thickness, BT 0.0045 m
Dimensions of the Vessel
Impeller Speed = 468.6 rpm
48. Conclusion
CFD helps to study the fluid flow inside the system.
MFR model is implemented to simulate the agitated impeller
involving rotating blades in CSTR
Baffles helps to convert the tangential velocity into radial &
axial velocity components.
The flow changes by changing the impeller in the same vessel
& with same speed.
49. References1. T. Kumaresan, Jyeshtharaj B. Joshi (2005). Effect of impeller design on the flow pattern and mixing in stirred tanks,
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