Steam tables are defined as the thermodynamic data that contain the properties of water or steam. ... Property tables list the properties from saturated water to steam
basics of ponchon savrit method to calculate no. of trays in distillation column and this could be more feasible for those who are willing to study separation processes related to their chemical engineering fields. moreover, if you find difficulty in taking lectures on YouTube, you can just click on this link and just download the slides for its study. as every student in this world in willing to study the basics of chemical engineering, this could be more beneficial for those students. also if your teacher wants any presentation slides on this specific topic, you can just download these slides from the website and can present in a better way to proceed you knowledge and journey of your education.
An Overview to the most common Industrial Mass Transfer Operations & Process Separation Technologies
Course Description
In this course we will cover the most basic processes involved in Mass Transfer Operations. This is an overview of what type of processes, methods and units are used in the industry. This is mostly an introductory course which will allow you to learn, understand and know the approach towards separation processes involving mass transfer phenomena.
It is an excellent course before any Mass Transfer Process or Unit Operation Course such as Distillations, Extractions, Leaching, Membranes, Absorption, etc...
This course is extremely recommended if you will continue with the following:
Flash Distillation, Simple Distillation, Batch Distillation
Gas Absorption, Desorption & Stripping
Binary Distillation, Fractional Distillation
Scrubbers, Gas Treating
Sprayers / Spray Towers
Bubble Columns / Sparged Vessels
Agitation Vessels
Packed Towers, Tray Towers
Membranes
Liquid Extraction
Dryers / Humidifiers
Adsorbers
Evaporators/Sublimators
Crystallizers
Centrifugations
And many other Separation Technology!
At the end of the Course:
You will be able to understand the mass transfer operations concepts. You will be able to identify Mass Transfer Unit Operations. You will be also able to ensure the type of method of separation technology used.
You will be able to apply this theory in further Unit Operations.
Theory-Based Course
This is a very theoretical course, some calculations and exercises are present, but overall, expect mostly theoretical concepts.
Feed conditions in distillation column with respect to feed plate and refluxIhsan Wassan
This document discusses feed conditions in distillation columns with respect to the feed plate and reflux. It defines key terms like distillation, relative volatility, and reflux. It explains that the condition of the feed stream determines the relation between flows above and below the feed plate. The amount of saturated liquid versus vapor in the feed is quantified by a variable q. Feed can be saturated liquid/vapor or a mixture, determining the slope of the q-line. Feed plates help separate mixtures, and more reflux improves separation efficiency, allowing fewer plates for a given separation. Total reflux passes vapor and liquid without product removal, while minimum reflux is the lowest ratio enabling separation with infinite plates.
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
Lectures on Heat Transfer - Introduction - Applications - Fundamentals - Gove...tmuliya
This file contains Introduction to Heat Transfer and Fundamental laws governing heat transfer.
The slides were prepared while teaching Heat Transfer course to the M.Tech. students in Mechanical Engineering Dept. of St. Joseph Engineering College, Vamanjoor, Mangalore, India.
This document discusses reflux ratios in distillation columns. It defines total, minimum, and optimum reflux ratios. Total reflux uses all overhead vapor as reflux, allowing calculation of minimum required plates. Minimum reflux is the maximum ratio requiring infinite plates for desired separation. Optimum reflux minimizes total costs by balancing fixed costs that decrease with higher reflux against increasing operating costs.
The document summarizes three regimes of boiling - purely convective boiling where liquid slowly rises from the heated surface, nucleate boiling where vapor bubbles form and detach from nucleation sites on the surface, and film boiling where a vapor film covers the entire surface. It also discusses two types of condensation - film wise where a continuous liquid film forms, and drop wise where small liquid droplets form randomly. Finally, it introduces heat exchangers as devices that transfer heat between two fluids through a separating solid barrier.
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: 2.1 Material balances
basics of ponchon savrit method to calculate no. of trays in distillation column and this could be more feasible for those who are willing to study separation processes related to their chemical engineering fields. moreover, if you find difficulty in taking lectures on YouTube, you can just click on this link and just download the slides for its study. as every student in this world in willing to study the basics of chemical engineering, this could be more beneficial for those students. also if your teacher wants any presentation slides on this specific topic, you can just download these slides from the website and can present in a better way to proceed you knowledge and journey of your education.
An Overview to the most common Industrial Mass Transfer Operations & Process Separation Technologies
Course Description
In this course we will cover the most basic processes involved in Mass Transfer Operations. This is an overview of what type of processes, methods and units are used in the industry. This is mostly an introductory course which will allow you to learn, understand and know the approach towards separation processes involving mass transfer phenomena.
It is an excellent course before any Mass Transfer Process or Unit Operation Course such as Distillations, Extractions, Leaching, Membranes, Absorption, etc...
This course is extremely recommended if you will continue with the following:
Flash Distillation, Simple Distillation, Batch Distillation
Gas Absorption, Desorption & Stripping
Binary Distillation, Fractional Distillation
Scrubbers, Gas Treating
Sprayers / Spray Towers
Bubble Columns / Sparged Vessels
Agitation Vessels
Packed Towers, Tray Towers
Membranes
Liquid Extraction
Dryers / Humidifiers
Adsorbers
Evaporators/Sublimators
Crystallizers
Centrifugations
And many other Separation Technology!
At the end of the Course:
You will be able to understand the mass transfer operations concepts. You will be able to identify Mass Transfer Unit Operations. You will be also able to ensure the type of method of separation technology used.
You will be able to apply this theory in further Unit Operations.
Theory-Based Course
This is a very theoretical course, some calculations and exercises are present, but overall, expect mostly theoretical concepts.
Feed conditions in distillation column with respect to feed plate and refluxIhsan Wassan
This document discusses feed conditions in distillation columns with respect to the feed plate and reflux. It defines key terms like distillation, relative volatility, and reflux. It explains that the condition of the feed stream determines the relation between flows above and below the feed plate. The amount of saturated liquid versus vapor in the feed is quantified by a variable q. Feed can be saturated liquid/vapor or a mixture, determining the slope of the q-line. Feed plates help separate mixtures, and more reflux improves separation efficiency, allowing fewer plates for a given separation. Total reflux passes vapor and liquid without product removal, while minimum reflux is the lowest ratio enabling separation with infinite plates.
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
Lectures on Heat Transfer - Introduction - Applications - Fundamentals - Gove...tmuliya
This file contains Introduction to Heat Transfer and Fundamental laws governing heat transfer.
The slides were prepared while teaching Heat Transfer course to the M.Tech. students in Mechanical Engineering Dept. of St. Joseph Engineering College, Vamanjoor, Mangalore, India.
This document discusses reflux ratios in distillation columns. It defines total, minimum, and optimum reflux ratios. Total reflux uses all overhead vapor as reflux, allowing calculation of minimum required plates. Minimum reflux is the maximum ratio requiring infinite plates for desired separation. Optimum reflux minimizes total costs by balancing fixed costs that decrease with higher reflux against increasing operating costs.
The document summarizes three regimes of boiling - purely convective boiling where liquid slowly rises from the heated surface, nucleate boiling where vapor bubbles form and detach from nucleation sites on the surface, and film boiling where a vapor film covers the entire surface. It also discusses two types of condensation - film wise where a continuous liquid film forms, and drop wise where small liquid droplets form randomly. Finally, it introduces heat exchangers as devices that transfer heat between two fluids through a separating solid barrier.
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: 2.1 Material balances
This document discusses boiling and condensation processes. It defines boiling as a liquid to vapor phase change and condensation as a vapor to liquid phase change. The document describes different types of boiling including nucleate, critical heat flux, transition, and film boiling. It also discusses pool boiling and flow boiling. For condensation, it covers film condensation and dropwise condensation. The key applications of boiling and condensation are in heat exchangers and refrigeration systems.
Heat exchangers transfer thermal energy between two or more fluids at different temperatures. They are classified based on their transfer process, geometry, heat transfer mechanism, and flow arrangement. Shell-and-tube heat exchangers consist of a set of tubes in a shell container and are the most important type, used across many industries. Their design involves calculating the heat transfer rate, selecting appropriate materials and geometry, and ensuring optimal fluid velocities and pressure drops within design limits.
- This document describes absorption and stripping processes using packed columns and graphical methods.
- It discusses operating lines, height of transfer units (HOG), number of transfer units (NOG), and how to calculate the height equivalent of a theoretical plate (HETP) for a packed column given mass transfer coefficients, flow rates, and equilibrium data.
- An example is provided to calculate the HETP for a specific packed column based on the mass transfer coefficients, flow rates, and equilibrium constant given.
1) Distillation is a method used to separate components of a liquid solution based on differences in how the components distribute between the vapor and liquid phases when heated to their boiling points.
2) Raoult's law describes vapor-liquid equilibrium for ideal solutions, relating the partial pressure of a component in vapor phase to its mole fraction in the liquid phase. Boiling point diagrams can be constructed using vapor pressure data.
3) Equilibrium or flash distillation involves heating a liquid mixture to partially vaporize it in a single stage, separating the vapor and liquid which approach equilibrium compositions.
This document discusses different types of boiling phenomena including pool boiling and flow boiling. It explains that pool boiling occurs when a stagnant pool of liquid is heated from below, while flow boiling occurs under bulk motion of the fluid. The document also describes the different boiling regimes that can occur during pool boiling, including nucleate boiling, boiling crisis/departure from nucleate boiling, and film boiling. It discusses bubble growth and collapse during boiling and provides diagrams to illustrate boiling heat flux versus temperature difference.
There are three main types of steam: wet steam, dry saturated steam, and superheated steam. Wet steam is a mixture of water molecules and steam at the saturation temperature. Dry saturated steam only contains steam at the saturation temperature. Superheated steam is dry saturated steam that has been heated further, raising its temperature above the saturation point. The document also defines terms like dryness fraction, wetness fraction, priming, degree of superheat, and amount of superheat as they relate to describing the properties and conditions of different types of steam.
Gas absorption is a process used to separate gases by contacting a gas mixture with a liquid solvent. The key principles are the solubility of the absorbed gas and the rate of mass transfer as the gas dissolves into the liquid. Absorption is usually carried out counter-currently in vertical columns. The solvent is fed at the top while the gas enters at the bottom, allowing the absorbed substances to be washed out in the downward flowing liquid. Proper selection of solvent considers factors like gas solubility, volatility, cost, and viscosity. Rate of absorption is determined by volumetric mass transfer coefficients, which can be calculated from operating line and equilibrium curve diagrams.
The document summarizes the process of crude oil distillation. Crude oil is heated through heat exchangers to 550°F and then further heated to 750°F in a furnace before entering the flash zone of an atmospheric fractionator. Reboilers provide heat to the bottom of distillation columns by boiling the liquid to generate vapors that drive the separation process. Temperature above 370-380°F can cause cracking and coking in atmospheric columns, so residue is sent to vacuum distillation where pressure is reduced below vapor pressure to distill the most volatile liquids.
The document discusses heat transfer equipment and heat exchangers. It defines a heat exchanger as a device that transfers thermal energy between two or more fluids at different temperatures without mixing the fluids. Heat exchangers can be classified based on their transfer process, number of fluids, degree of surface compactness, construction, flow arrangement, and heat transfer mechanism. Common examples include shell-and-tube exchangers, radiators, condensers, evaporators, and cooling towers.
This document discusses the properties of steam. It begins by defining steam as the gaseous phase of water produced by heating water. Steam can exist in different states such as wet steam, dry saturated steam, and superheated steam. The document then discusses the enthalpy, specific volume, internal energy, and dryness fraction of different types of steam. It concludes by explaining different types of calorimeters used to measure the dryness fraction of steam, including barrel, separating, throttling, and combined separating and throttling calorimeters.
The document discusses properties of pure substances and phases of matter. It defines key terms like boiling point, melting point, saturation point, saturation pressure, saturation temperature, and triple point. It also discusses properties of steam like wet steam, dry saturated steam, superheated steam, and dryness fraction. Expressions are provided for enthalpy, internal energy, specific volume of different types of steam. Steam tables listing temperature, pressure, specific volume, enthalpy and entropy values are also included. The Rankine cycle used in steam engines is briefly explained through its four processes of heat addition, expansion, heat rejection and pumping.
This document provides an overview of power plant technology and thermodynamics concepts. It covers topics such as the first law of thermodynamics, the ideal gas law, steam power plant cycles, combustion of fuels, gas turbines, and other power generation methods. The document defines important thermodynamic terms and equations for analyzing power plant systems and their various components like boilers, turbines, condensers. It also discusses gas mixtures, ideal gas behavior, and properties of pure substances important for power plant design and operation.
This document discusses key concepts related to the specific volume and internal energy of steam. It defines specific volume as the volume occupied by 1 kg of a substance. It then defines specific volumes for saturated water, dry saturated steam, wet steam, and superheated steam. The specific volume of steam increases with temperature. It also discusses how to calculate the internal energy of dry steam, wet steam, and superheated steam using enthalpy, pressure, and specific volume. Finally, it defines internal latent heat as the difference between enthalpy of evaporation and work of evaporation.
The processing technique employing a suspension or fluidization of small solid particles in a vertically rising stream of fluid usually gas so that fluid and solid come into intimate contact. This is a tool with many applications in the petroleum and chemical process industries. Suspensions of solid particles by vertically rising liquid streams are of lesser interest in modern processing, but have been shown to be of use, particularly in liquid contacting of ion-exchange resins. However, they come in this same classification and their use involves techniques of liquid settling, both free and hindered (sedimentation), classification, and density flotation.
This document discusses the McCabe-Thiele method for designing binary distillation columns. The method uses vapor-liquid equilibrium (VLE) data to graphically determine the theoretical number of stages required for separation. Operating lines are drawn on the VLE diagram based on the desired compositions of top and bottom products. Where these lines intersect represents equilibrium stages. The number of intersections equals the number of theoretical stages. Additional trays are needed based on tray efficiency. The feed point can also be determined from its vapor-liquid condition. Overall column design requires considering additional factors like tray spacing, diameter, and heating/cooling duties through an iterative process.
ANALYSIS OF BOILING CURVE AND FORCED CONVECTION BOILINGArun Sarasan
The document analyzes boiling curves and forced convection boiling. It discusses pool boiling and flow boiling, subcooled and saturated boiling, and the various regimes that occur on the boiling curve - natural convection, nucleate boiling, transition boiling, and film boiling. Heat transfer correlations are presented for different boiling regimes, including the Rohsenow correlation for nucleate boiling and relationships for critical heat flux and minimum heat flux. Flow boiling is also examined, describing different flow patterns that can occur in two-phase flow inside a tube.
This document discusses drying of wet solids. It begins by defining drying as the removal of liquid, generally water, from a wet solid to produce a relatively dry product. Examples of industrial drying processes are provided. The various mechanisms of moisture transport within solids during drying are described, including capillary forces, liquid diffusion, and vapor diffusion. The stages of drying and how the drying rate changes over time are explained. Factors that influence the critical moisture content and equilibrium moisture content are discussed. Different types of industrial dryers used for drying solids, including tray dryers, rotary dryers, flash dryers, and drum dryers are described. Heat and mass transfer principles governing batch and continuous drying are outlined.
Shell and Tube Heat Exchanger in heat TransferUsman Shah
Shell and tube heat exchangers consist of a bundle of tubes enclosed in a cylindrical shell. Fluids flow through either the tubes or shell to facilitate heat transfer between the two fluids. They are widely used in chemical processes due to their ability to achieve a large heat transfer surface area in a compact volume. Key components include tubesheets, baffles, support rods and segmented baffles which direct fluid flow across the tube bundle for efficient heat transfer. Design considerations include allocating the more corrosive or fouling fluid to the tubeside for easier cleaning and maintenance.
This document discusses properties of pure substances. It defines a pure substance as having a fixed chemical composition throughout, such as water or nitrogen. A pure substance can exist in different phases like solid, liquid, or gas. The properties of a pure substance, like density and specific volume, depend on its phase and conditions of temperature and pressure. Phase change processes, like boiling and condensation, involve absorbing or releasing heat. Property diagrams are used to understand relationships between temperature, pressure, and phase for a pure substance. An ideal gas is defined by the ideal gas law, but real gases deviate from this behavior at high pressures.
Pure substances can exist in different phases including solid, liquid, and gas. They have a fixed chemical composition throughout. Phase changes between these states are associated with the absorption or release of latent heat. The properties of a pure substance, such as pressure, temperature, specific volume, and enthalpy are interrelated. Graphs of these properties, such as pressure-volume and temperature-entropy diagrams, can be used to determine the phase and properties of a pure substance at given conditions. Common phase change processes include vaporization, condensation, melting, and sublimation.
This document discusses boiling and condensation processes. It defines boiling as a liquid to vapor phase change and condensation as a vapor to liquid phase change. The document describes different types of boiling including nucleate, critical heat flux, transition, and film boiling. It also discusses pool boiling and flow boiling. For condensation, it covers film condensation and dropwise condensation. The key applications of boiling and condensation are in heat exchangers and refrigeration systems.
Heat exchangers transfer thermal energy between two or more fluids at different temperatures. They are classified based on their transfer process, geometry, heat transfer mechanism, and flow arrangement. Shell-and-tube heat exchangers consist of a set of tubes in a shell container and are the most important type, used across many industries. Their design involves calculating the heat transfer rate, selecting appropriate materials and geometry, and ensuring optimal fluid velocities and pressure drops within design limits.
- This document describes absorption and stripping processes using packed columns and graphical methods.
- It discusses operating lines, height of transfer units (HOG), number of transfer units (NOG), and how to calculate the height equivalent of a theoretical plate (HETP) for a packed column given mass transfer coefficients, flow rates, and equilibrium data.
- An example is provided to calculate the HETP for a specific packed column based on the mass transfer coefficients, flow rates, and equilibrium constant given.
1) Distillation is a method used to separate components of a liquid solution based on differences in how the components distribute between the vapor and liquid phases when heated to their boiling points.
2) Raoult's law describes vapor-liquid equilibrium for ideal solutions, relating the partial pressure of a component in vapor phase to its mole fraction in the liquid phase. Boiling point diagrams can be constructed using vapor pressure data.
3) Equilibrium or flash distillation involves heating a liquid mixture to partially vaporize it in a single stage, separating the vapor and liquid which approach equilibrium compositions.
This document discusses different types of boiling phenomena including pool boiling and flow boiling. It explains that pool boiling occurs when a stagnant pool of liquid is heated from below, while flow boiling occurs under bulk motion of the fluid. The document also describes the different boiling regimes that can occur during pool boiling, including nucleate boiling, boiling crisis/departure from nucleate boiling, and film boiling. It discusses bubble growth and collapse during boiling and provides diagrams to illustrate boiling heat flux versus temperature difference.
There are three main types of steam: wet steam, dry saturated steam, and superheated steam. Wet steam is a mixture of water molecules and steam at the saturation temperature. Dry saturated steam only contains steam at the saturation temperature. Superheated steam is dry saturated steam that has been heated further, raising its temperature above the saturation point. The document also defines terms like dryness fraction, wetness fraction, priming, degree of superheat, and amount of superheat as they relate to describing the properties and conditions of different types of steam.
Gas absorption is a process used to separate gases by contacting a gas mixture with a liquid solvent. The key principles are the solubility of the absorbed gas and the rate of mass transfer as the gas dissolves into the liquid. Absorption is usually carried out counter-currently in vertical columns. The solvent is fed at the top while the gas enters at the bottom, allowing the absorbed substances to be washed out in the downward flowing liquid. Proper selection of solvent considers factors like gas solubility, volatility, cost, and viscosity. Rate of absorption is determined by volumetric mass transfer coefficients, which can be calculated from operating line and equilibrium curve diagrams.
The document summarizes the process of crude oil distillation. Crude oil is heated through heat exchangers to 550°F and then further heated to 750°F in a furnace before entering the flash zone of an atmospheric fractionator. Reboilers provide heat to the bottom of distillation columns by boiling the liquid to generate vapors that drive the separation process. Temperature above 370-380°F can cause cracking and coking in atmospheric columns, so residue is sent to vacuum distillation where pressure is reduced below vapor pressure to distill the most volatile liquids.
The document discusses heat transfer equipment and heat exchangers. It defines a heat exchanger as a device that transfers thermal energy between two or more fluids at different temperatures without mixing the fluids. Heat exchangers can be classified based on their transfer process, number of fluids, degree of surface compactness, construction, flow arrangement, and heat transfer mechanism. Common examples include shell-and-tube exchangers, radiators, condensers, evaporators, and cooling towers.
This document discusses the properties of steam. It begins by defining steam as the gaseous phase of water produced by heating water. Steam can exist in different states such as wet steam, dry saturated steam, and superheated steam. The document then discusses the enthalpy, specific volume, internal energy, and dryness fraction of different types of steam. It concludes by explaining different types of calorimeters used to measure the dryness fraction of steam, including barrel, separating, throttling, and combined separating and throttling calorimeters.
The document discusses properties of pure substances and phases of matter. It defines key terms like boiling point, melting point, saturation point, saturation pressure, saturation temperature, and triple point. It also discusses properties of steam like wet steam, dry saturated steam, superheated steam, and dryness fraction. Expressions are provided for enthalpy, internal energy, specific volume of different types of steam. Steam tables listing temperature, pressure, specific volume, enthalpy and entropy values are also included. The Rankine cycle used in steam engines is briefly explained through its four processes of heat addition, expansion, heat rejection and pumping.
This document provides an overview of power plant technology and thermodynamics concepts. It covers topics such as the first law of thermodynamics, the ideal gas law, steam power plant cycles, combustion of fuels, gas turbines, and other power generation methods. The document defines important thermodynamic terms and equations for analyzing power plant systems and their various components like boilers, turbines, condensers. It also discusses gas mixtures, ideal gas behavior, and properties of pure substances important for power plant design and operation.
This document discusses key concepts related to the specific volume and internal energy of steam. It defines specific volume as the volume occupied by 1 kg of a substance. It then defines specific volumes for saturated water, dry saturated steam, wet steam, and superheated steam. The specific volume of steam increases with temperature. It also discusses how to calculate the internal energy of dry steam, wet steam, and superheated steam using enthalpy, pressure, and specific volume. Finally, it defines internal latent heat as the difference between enthalpy of evaporation and work of evaporation.
The processing technique employing a suspension or fluidization of small solid particles in a vertically rising stream of fluid usually gas so that fluid and solid come into intimate contact. This is a tool with many applications in the petroleum and chemical process industries. Suspensions of solid particles by vertically rising liquid streams are of lesser interest in modern processing, but have been shown to be of use, particularly in liquid contacting of ion-exchange resins. However, they come in this same classification and their use involves techniques of liquid settling, both free and hindered (sedimentation), classification, and density flotation.
This document discusses the McCabe-Thiele method for designing binary distillation columns. The method uses vapor-liquid equilibrium (VLE) data to graphically determine the theoretical number of stages required for separation. Operating lines are drawn on the VLE diagram based on the desired compositions of top and bottom products. Where these lines intersect represents equilibrium stages. The number of intersections equals the number of theoretical stages. Additional trays are needed based on tray efficiency. The feed point can also be determined from its vapor-liquid condition. Overall column design requires considering additional factors like tray spacing, diameter, and heating/cooling duties through an iterative process.
ANALYSIS OF BOILING CURVE AND FORCED CONVECTION BOILINGArun Sarasan
The document analyzes boiling curves and forced convection boiling. It discusses pool boiling and flow boiling, subcooled and saturated boiling, and the various regimes that occur on the boiling curve - natural convection, nucleate boiling, transition boiling, and film boiling. Heat transfer correlations are presented for different boiling regimes, including the Rohsenow correlation for nucleate boiling and relationships for critical heat flux and minimum heat flux. Flow boiling is also examined, describing different flow patterns that can occur in two-phase flow inside a tube.
This document discusses drying of wet solids. It begins by defining drying as the removal of liquid, generally water, from a wet solid to produce a relatively dry product. Examples of industrial drying processes are provided. The various mechanisms of moisture transport within solids during drying are described, including capillary forces, liquid diffusion, and vapor diffusion. The stages of drying and how the drying rate changes over time are explained. Factors that influence the critical moisture content and equilibrium moisture content are discussed. Different types of industrial dryers used for drying solids, including tray dryers, rotary dryers, flash dryers, and drum dryers are described. Heat and mass transfer principles governing batch and continuous drying are outlined.
Shell and Tube Heat Exchanger in heat TransferUsman Shah
Shell and tube heat exchangers consist of a bundle of tubes enclosed in a cylindrical shell. Fluids flow through either the tubes or shell to facilitate heat transfer between the two fluids. They are widely used in chemical processes due to their ability to achieve a large heat transfer surface area in a compact volume. Key components include tubesheets, baffles, support rods and segmented baffles which direct fluid flow across the tube bundle for efficient heat transfer. Design considerations include allocating the more corrosive or fouling fluid to the tubeside for easier cleaning and maintenance.
This document discusses properties of pure substances. It defines a pure substance as having a fixed chemical composition throughout, such as water or nitrogen. A pure substance can exist in different phases like solid, liquid, or gas. The properties of a pure substance, like density and specific volume, depend on its phase and conditions of temperature and pressure. Phase change processes, like boiling and condensation, involve absorbing or releasing heat. Property diagrams are used to understand relationships between temperature, pressure, and phase for a pure substance. An ideal gas is defined by the ideal gas law, but real gases deviate from this behavior at high pressures.
Pure substances can exist in different phases including solid, liquid, and gas. They have a fixed chemical composition throughout. Phase changes between these states are associated with the absorption or release of latent heat. The properties of a pure substance, such as pressure, temperature, specific volume, and enthalpy are interrelated. Graphs of these properties, such as pressure-volume and temperature-entropy diagrams, can be used to determine the phase and properties of a pure substance at given conditions. Common phase change processes include vaporization, condensation, melting, and sublimation.
Thermody Properties of Pure Substance (1).pptethiouniverse
- A pure substance has a fixed chemical composition regardless of phase. Water can exist as ice, liquid water, or water vapor while maintaining the same molecular formula.
- A pure substance can change between solid, liquid, and gas phases depending on temperature and pressure. The phase change occurs at the saturation temperature and pressure.
- During a phase change, energy is absorbed or released in the form of latent heat. The latent heat of fusion is released during freezing and the latent heat of vaporization is released during condensation.
Propiedades termodinámicas de las sustancias purasNorman Rivera
1. Thermodynamics properties of pure substances include phases (solid, liquid, gas), phase change processes, and property diagrams.
2. Key points in the phase change of water include compressed liquid, saturated liquid, saturated liquid-vapor mixture, saturated vapor, and superheated vapor.
3. Important thermodynamic concepts are saturation temperature and pressure, which define the conditions for phase changes, and the critical point where liquid and gas phases cannot be distinguished.
This document discusses properties of pure substances and phase changes. It defines a pure substance as having a fixed chemical composition and describes the three common phases as solid, liquid, and gas. Phase changes between these three states are explained, including saturated and supersaturated states. Key concepts introduced are the saturation temperature and pressure, which define conditions for phase changes. Diagrams are presented to illustrate phase equilibria, including temperature-volume, pressure-volume, and pressure-temperature diagrams. Common thermodynamic properties like latent heat and reference states are also defined. Ideal gas behavior is discussed along with limitations of the ideal gas model.
This document discusses the properties of pure substances and their phase changes. Some key points:
1) A pure substance has a fixed chemical composition throughout and may exist in different phases including solid, liquid, and gas.
2) The molecular arrangements and bonding strengths differ between phases, with solids having the strongest bonds and gases having the weakest.
3) A pure substance undergoes phase changes as it is heated or cooled, passing through solid, liquid, and gas states depending on the temperature and pressure conditions. Phase change diagrams depict these relationships.
4) Properties of saturated liquid-vapor mixtures are averages based on the fraction of each phase present. Superheated vapors and compressed liquids
This document provides an overview of thermodynamic concepts related to pure substances, including:
- Phases of pure substances can exist as solids, liquids, or gases, depending on temperature and pressure. Phase changes between these states occur at characteristic saturation temperatures and pressures.
- Property diagrams like temperature-volume (T-V), pressure-volume (P-V), and pressure-temperature (P-T) diagrams are used to illustrate phase changes and relationships between intensive and extensive properties.
- During phase changes, pure substances absorb or release a characteristic amount of energy known as latent heat of fusion or vaporization.
- Mixtures of vapor and liquid phases at saturation conditions are defined by quality, the
This document provides an overview of Chapter 3 from a thermodynamics textbook. It discusses volumetric properties of pure fluids. The chapter describes phase change processes and diagrams for pure substances. It also discusses property tables that list internal energy, enthalpy, and entropy values for substances, as these relationships are too complex to express through simple equations. Examples are provided on using property tables to determine pressure, temperature, volume changes, and energy changes during phase change processes like vaporization of water.
This document discusses pure substances and the phases of pure substances. Some key points include:
- A pure substance has a fixed chemical composition throughout and can exist in different phases like solid, liquid, and gas.
- Pure substances can undergo phase changes through processes like melting, vaporization, and condensation.
- The properties of a pure substance depend on its phase and conditions like temperature and pressure.
- Mixtures of substances qualify as pure substances as long as they are homogeneous. Examples include liquid water and water vapor mixtures.
The document then discusses concepts like saturation, latent heat, quality, and moisture content which are important for understanding phase equilibria of pure substances.
This document provides an overview of properties of pure substances and phase change processes. It introduces key concepts such as pure substances, phases of matter, phase change diagrams, property tables, and the ideal gas law. Specific topics covered include saturated liquids and vapors, phase change temperatures and pressures, property diagrams, determining properties from tables, and using the ideal gas equation of state to model real gases. The document uses water as an example pure substance to illustrate these concepts through diagrams and examples.
This document discusses thermodynamic properties of pure substances. It introduces pure substances and their phases of solid, liquid, and gas. Phase change processes are described, including saturated liquid, vapor, and superheated regions. T-V, P-V, and P-T diagrams are presented to illustrate the relationships between these properties. Key concepts covered include saturation temperature/pressure, latent heats of fusion and vaporization, the p-v-T surface, and how substances' behaviors differ when expanding or contracting during phase changes. Objectives are listed for understanding pure substance thermodynamics and properties.
States of Matter and properties of matter: State of matter, changes in the state of matter, latent heats, vapour pressure, sublimation critical point, eutectic mixtures, gases, aerosols – inhalers, relative humidity, liquid complexes, liquid crystals, glassy states, solid- crystalline, amorphous & polymorphism.
Physicochemical properties of drug molecules: Refractive index, optical rotation, dielectric constant, dipole moment, dissociation constant, determinations and applications
States of Matter and properties of matter: State of matter, changes in the state of matter, latent heats, vapour pressure, sublimation critical point, eutectic mixtures, gases, aerosols – inhalers, relative humidity, liquid complexes, liquid crystals, glassy states, solid- crystalline, amorphous & polymorphism.
Physicochemical properties of drug molecules: Refractive index, optical rotation, dielectric constant, dipole moment, dissociation constant, determinations and applications
1. The chapter discusses the properties of pure substances and how they exist in different phases - solid, liquid, gas - depending on temperature and pressure conditions.
2. Phase change processes like vaporization, melting and sublimation occur at characteristic saturation temperatures and pressures and can be illustrated using pressure-volume-temperature diagrams.
3. The diagrams show the relationship between pressure, volume and temperature for different phases of a pure substance, including saturation lines and the critical point where liquid and gas phases become indistinguishable.
Bab 3 Thermodynamic of Engineering ApproachIbnu Hasan
This document discusses properties of pure substances and phase changes. It introduces concepts like saturated liquid, saturated vapor, and phase diagrams. Properties are presented in tables that show how quantities like enthalpy and temperature vary with pressure and phase for substances like water. The ideal gas law is presented as a simple equation of state to model gas behavior.
This document discusses properties of pure substances and uses water as an example. It describes:
- Property diagrams like pressure-volume (P-V), pressure-temperature (P-T), temperature-entropy (T-S), and enthalpy-entropy (h-s) diagrams that show the behavior of pure substances under different conditions.
- Key points on these diagrams like triple point, critical point, saturation lines, and phases.
- How steam tables contain thermodynamic property data for water/steam in different phases and conditions.
This document defines key terms related to steam formation and describes processes involved. It discusses:
- Terms like saturated liquid, saturated vapor, superheated vapor etc.
- Temperature and pressure where a substance changes phase (saturation temperature and pressure)
- Graphs like P-V and h-s diagrams that represent steam formation processes
- Quantities of heat absorbed during heating, vaporization (latent heat) and superheating of steam
- Measurement of dryness fraction (quality) of wet steam using throttling or electric calorimeters.
Pure Substance Pure substance is a chemically homogenous s.docxamrit47
Pure Substance
Pure substance is a chemically homogenous substance and invariable in chemical
composition. The chemical composition in a pure substance is in a fixed ratio throughout
the system and does not change during any process. A fixed relationship between the
pressure and temperature of the pure substance can be determined when two phases of a
pure substance are in equilibrium. The pure substance which used in this experiment is
water. Water has a freezing point of 0
o
C and a boiling point of 100
o
C. Besides, it can
exist in three different states which are solid, liquid and gaseous states.
Steam Properties
There are several steam properties and saturation temperature is one of the steam
properties. Saturation is the condition which the mixture of liquid and vapour can exist
together at a given temperature and pressure. Saturation temperature is the equilibrium
temperature during phase change and the temperature where the evaporation or the
condensation process of the pure substance starts to occur in a given system pressure.
Besides, saturation pressure is the equilibrium pressure in a given system temperature.
Property diagram is a diagram which shows the phases of a substance and the
relationships between its properties. There are two common property diagram which are
P-V property diagram and T-V property diagram. Figure 1 below shows the T-V property
diagram which could clearly describe the property of the pure substance during phase
change in this experiment.
Figure 1: Property Diagram
Based on Figure 1, when the saturation temperature is higher than the liquid
temperature, it is fallen into the sub-cooled liquid region. The liquid in this region is
known as sub-cooled liquid or compressed liquid. Next, when the heat is continually
supplied to the liquid, the temperature of the liquid will rise gradually. The liquid will
reach saturation when it reaches the saturation temperature and it is also known as
saturated liquid. Vaporization occurs when further heat is applied and the phase of the
pure substance is starting to change. In this phase, liquid and vapour exist together and
the temperature is in equilibrium. It is known as saturated wet vapour as the vapour
fraction in the mixture is increasing. When the liquid has evaporated fully into vapour
state and the temperature is still remained at saturation temperature, it is known as dry
saturated vapour. Lastly, when the vapour temperature is higher than the saturation
temperature, it is categorized in superheated region and known as superheated vapour.
Enthalpy is one of the steam properties and it is the total sum of internal energy
plus the product of the pressure and volume as shown in the Equation 1 below.
H = U + P * V (Equation 1)
where,
H = Enthalpy (J)
U = Internal Energy (J)
P = Pressure (Pa)
V = Volume (m
3
)
The formula in Equation 1 can be expressed in term o ...
The document discusses properties of pure substances, including their phases of vapor, liquid, and solid and how they relate on a pressure-temperature diagram. It explains concepts like saturation temperature and pressure, triple points, and that the state of a pure substance is determined by two independent properties. Tables of thermodynamic properties are commonly available for many pure substances.
Similar to Steam properties and phase diagram (20)
Using recycled concrete aggregates (RCA) for pavements is crucial to achieving sustainability. Implementing RCA for new pavement can minimize carbon footprint, conserve natural resources, reduce harmful emissions, and lower life cycle costs. Compared to natural aggregate (NA), RCA pavement has fewer comprehensive studies and sustainability assessments.
Low power architecture of logic gates using adiabatic techniquesnooriasukmaningtyas
The growing significance of portable systems to limit power consumption in ultra-large-scale-integration chips of very high density, has recently led to rapid and inventive progresses in low-power design. The most effective technique is adiabatic logic circuit design in energy-efficient hardware. This paper presents two adiabatic approaches for the design of low power circuits, modified positive feedback adiabatic logic (modified PFAL) and the other is direct current diode based positive feedback adiabatic logic (DC-DB PFAL). Logic gates are the preliminary components in any digital circuit design. By improving the performance of basic gates, one can improvise the whole system performance. In this paper proposed circuit design of the low power architecture of OR/NOR, AND/NAND, and XOR/XNOR gates are presented using the said approaches and their results are analyzed for powerdissipation, delay, power-delay-product and rise time and compared with the other adiabatic techniques along with the conventional complementary metal oxide semiconductor (CMOS) designs reported in the literature. It has been found that the designs with DC-DB PFAL technique outperform with the percentage improvement of 65% for NOR gate and 7% for NAND gate and 34% for XNOR gate over the modified PFAL techniques at 10 MHz respectively.
Harnessing WebAssembly for Real-time Stateless Streaming PipelinesChristina Lin
Traditionally, dealing with real-time data pipelines has involved significant overhead, even for straightforward tasks like data transformation or masking. However, in this talk, we’ll venture into the dynamic realm of WebAssembly (WASM) and discover how it can revolutionize the creation of stateless streaming pipelines within a Kafka (Redpanda) broker. These pipelines are adept at managing low-latency, high-data-volume scenarios.
ACEP Magazine edition 4th launched on 05.06.2024Rahul
This document provides information about the third edition of the magazine "Sthapatya" published by the Association of Civil Engineers (Practicing) Aurangabad. It includes messages from current and past presidents of ACEP, memories and photos from past ACEP events, information on life time achievement awards given by ACEP, and a technical article on concrete maintenance, repairs and strengthening. The document highlights activities of ACEP and provides a technical educational article for members.
We have compiled the most important slides from each speaker's presentation. This year’s compilation, available for free, captures the key insights and contributions shared during the DfMAy 2024 conference.
A SYSTEMATIC RISK ASSESSMENT APPROACH FOR SECURING THE SMART IRRIGATION SYSTEMSIJNSA Journal
The smart irrigation system represents an innovative approach to optimize water usage in agricultural and landscaping practices. The integration of cutting-edge technologies, including sensors, actuators, and data analysis, empowers this system to provide accurate monitoring and control of irrigation processes by leveraging real-time environmental conditions. The main objective of a smart irrigation system is to optimize water efficiency, minimize expenses, and foster the adoption of sustainable water management methods. This paper conducts a systematic risk assessment by exploring the key components/assets and their functionalities in the smart irrigation system. The crucial role of sensors in gathering data on soil moisture, weather patterns, and plant well-being is emphasized in this system. These sensors enable intelligent decision-making in irrigation scheduling and water distribution, leading to enhanced water efficiency and sustainable water management practices. Actuators enable automated control of irrigation devices, ensuring precise and targeted water delivery to plants. Additionally, the paper addresses the potential threat and vulnerabilities associated with smart irrigation systems. It discusses limitations of the system, such as power constraints and computational capabilities, and calculates the potential security risks. The paper suggests possible risk treatment methods for effective secure system operation. In conclusion, the paper emphasizes the significant benefits of implementing smart irrigation systems, including improved water conservation, increased crop yield, and reduced environmental impact. Additionally, based on the security analysis conducted, the paper recommends the implementation of countermeasures and security approaches to address vulnerabilities and ensure the integrity and reliability of the system. By incorporating these measures, smart irrigation technology can revolutionize water management practices in agriculture, promoting sustainability, resource efficiency, and safeguarding against potential security threats.
Embedded machine learning-based road conditions and driving behavior monitoringIJECEIAES
Car accident rates have increased in recent years, resulting in losses in human lives, properties, and other financial costs. An embedded machine learning-based system is developed to address this critical issue. The system can monitor road conditions, detect driving patterns, and identify aggressive driving behaviors. The system is based on neural networks trained on a comprehensive dataset of driving events, driving styles, and road conditions. The system effectively detects potential risks and helps mitigate the frequency and impact of accidents. The primary goal is to ensure the safety of drivers and vehicles. Collecting data involved gathering information on three key road events: normal street and normal drive, speed bumps, circular yellow speed bumps, and three aggressive driving actions: sudden start, sudden stop, and sudden entry. The gathered data is processed and analyzed using a machine learning system designed for limited power and memory devices. The developed system resulted in 91.9% accuracy, 93.6% precision, and 92% recall. The achieved inference time on an Arduino Nano 33 BLE Sense with a 32-bit CPU running at 64 MHz is 34 ms and requires 2.6 kB peak RAM and 139.9 kB program flash memory, making it suitable for resource-constrained embedded systems.
2. Pure Substance
A substance that has a constant chemical composition
throughout its mass is called a pure substance. It is one
component system. It may exist in one or more phases.
e.g. Water, Air
Phases of a Pure Substances:
Solid
Liquid
Gas or Vapour
3. 4’
4’’1’’ 2’’ 3’’
1’ 2’ 3’
2 3 4 5 61
Phase Diagram
P
v
5’ 6’
5’’ 6’’
Solid
Solid starts melting
Solid changes into liquid
Liquid starts vapourizing
Liquid changes into vapour
8. Property Tables
Saturated Liquid and Saturated Vapour State:
f = properties of saturated liquid
g = properties of saturated vapour
vf = Specific volume of saturated liquid
vg = Specific volume of saturated vapour
vfg = Difference between vf and vg
11. 11
o Critical point - the temperature and pressure above which there
is no distinction between the liquid and vapor phases.
o Triple point - the temperature and pressure at which all three
phases can exist in equilibrium.
o Sublimation - change of phase from solid to vapor.
o Vaporization - change of phase from liquid to vapor.
o Condensation - change of phase from vapor to liquid.
o Fusion or melting - change of phase from solid to liquid.
Important Definition
12. 12
o Saturation is defined as a condition in which a mixture
of vapor and liquid can exist together at a given
temperature and pressure.
o Saturation pressure is the pressure at which the liquid
and vapor phases are in equilibrium at a given
temperature
For a pure substance there is a definite relationship
between saturation pressure and saturation temperature. The
higher the pressure, the higher the saturation temperature
13. 13
o Latent heat: The amount of energy absorbed or
released during a phase-change process.
o Latent heat of fusion: The amount of energy absorbed
during melting. It is equivalent to the amount of energy
released during freezing.
o Latent heat of vaporization: The amount of energy
absorbed during vaporization and it is equivalent to the
energy released during condensation.
At 1 atm pressure, the latent heat of fusion of water
is 333.7 kJ/kg and the latent heat of vaporization is
2256.5 kJ/kg.
14. 14
o When a substance exists as part liquid and part vapor at
saturation conditions, its quality (x) is defined as the
ratio of the mass of the vapor to the total mass of both
vapor and liquid.
o The quality is zero for the saturated liquid and one for
the saturated vapor (0 ≤ x ≤ 1)
o For example, if the mass of vapor is 0.2 g and the mass
of the liquid is 0.8 g, then the quality is 0.2 or 20%.
x
mass
mass
m
m m
saturated vapor
total
g
f g
15. 15
Example 1.1
Determine the saturated pressure, specific volume, internal energy
and enthalpy for saturated vapor at 45oC and 50oC.
16. Example 1.2
Determine the saturated pressure, specific volume, internal energy
and enthalpy for saturated water vapor at 47⁰ C .
17. 17
Solution:
Extract data from steam table
T Psat v u h
45 9.5953 15.251 2436.1 2582.4
47 Psat v u h
50 12.352 12.026 2442.7 2591.3
Interpolation Scheme for Psat
Interpolation for Psat
@47
9.5953 47 45
12.352 9.5953 50 45
10.698
sat
sat
P
P kPa
Do the same principal to
others!!!!