Excess property introduction
▪ Excess volume
▪ Excess gibbs free energy
▪ Entropy of mixing
▪ what is use of Residual property and Excess property
in thermodynamics
▪ Case study
▪ Thermo-calc demo
▪ conclusion
Introduction
Concepts of Fugacity
Effect of Temperature & pressure on Fugacity
Important relation of Fugacity Coefficient
Vapour Liquid Equilibrium for pure species
Fugacity & Fugacity coefficient: Species in solution
Reference
This document discusses various activity coefficient models that are used to predict solubility, including correlative models like Wilson and UNIQUAC, and predictive models like UNIFAC and NRTL-SAC. It explains that activity coefficient models are important for calculating solubility and driving force since experimental determination of solubility can be time consuming and costly. The document then provides details on each model, their assumptions, advantages, disadvantages and applications. It concludes with discussing future work involving measuring solubility of a compound and modifying NRTL-SAC model to account for temperature effects.
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.
Excess gibbs free energy models,MARGULES EQUATION
,REDLICH-KISTER EQUATION,VAN LAAR EQUATION
,WILSON AND “NRTL” EQUATION
,UNIversal QUAsi Chemical equation
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.
In the plant, ammonia is produced from synthesis gas containing hydrogen and nitrogen in the ratio of approximately 3:1. Besides these components, the synthesis gas contains inert gases such as argon and methane to a limited extent. The source of H2 is demineralized water and the hydrocarbons in the natural gas. The source of N2 is the atmospheric air. The source of CO2 is the hydrocarbons in the natural gas feed. Product ammonia and CO2 is sent to urea plant. The present article intended the description of ammonia plant for natural gas based plants and the possible material balance of some section.
Slides for the eLearning course Separation and purification processes in biorefineries (https://open-learn.xamk.fi) in IMPRESS project.
Section: Distillation
Subject: 1.1 Vapor Liquid Equilibrium
Excess Thermodynamic Properties . Excess volume of mixing, Heat of mixing, deviation in adiabatic compressiblitgies of liquid mixtures (homogeneous and non-reacting)
Introduction
Concepts of Fugacity
Effect of Temperature & pressure on Fugacity
Important relation of Fugacity Coefficient
Vapour Liquid Equilibrium for pure species
Fugacity & Fugacity coefficient: Species in solution
Reference
This document discusses various activity coefficient models that are used to predict solubility, including correlative models like Wilson and UNIQUAC, and predictive models like UNIFAC and NRTL-SAC. It explains that activity coefficient models are important for calculating solubility and driving force since experimental determination of solubility can be time consuming and costly. The document then provides details on each model, their assumptions, advantages, disadvantages and applications. It concludes with discussing future work involving measuring solubility of a compound and modifying NRTL-SAC model to account for temperature effects.
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.
Excess gibbs free energy models,MARGULES EQUATION
,REDLICH-KISTER EQUATION,VAN LAAR EQUATION
,WILSON AND “NRTL” EQUATION
,UNIversal QUAsi Chemical equation
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.
In the plant, ammonia is produced from synthesis gas containing hydrogen and nitrogen in the ratio of approximately 3:1. Besides these components, the synthesis gas contains inert gases such as argon and methane to a limited extent. The source of H2 is demineralized water and the hydrocarbons in the natural gas. The source of N2 is the atmospheric air. The source of CO2 is the hydrocarbons in the natural gas feed. Product ammonia and CO2 is sent to urea plant. The present article intended the description of ammonia plant for natural gas based plants and the possible material balance of some section.
Slides for the eLearning course Separation and purification processes in biorefineries (https://open-learn.xamk.fi) in IMPRESS project.
Section: Distillation
Subject: 1.1 Vapor Liquid Equilibrium
Excess Thermodynamic Properties . Excess volume of mixing, Heat of mixing, deviation in adiabatic compressiblitgies of liquid mixtures (homogeneous and non-reacting)
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
Distillation Sequences, Complex Columns and Heat IntegrationGerard B. Hawkins
Distillation Sequences, Complex Columns and Heat Integration
0 INTRODUCTION/PURPOSE
1 SCOPE
2 FIELD OF APPLICATION
3 DEFINITIONS
4 SEQUENCING OF SIMPLE COLUMNS
4.1 Sidestream Columns
4.2 Multi-Feed Columns
5 SIMPLE COLUMN SEQUENCING AND HEAT
INTEGRATION INTERACTIONS
5.1 Energy Quantity and Quality
5.2 Heat Integration within the Total Flowsheet
6 COMPLEX COLUMN ARRANGEMENTS
6.1 Indirect Sequence with Vapor Link
6.2 Sidestream Systems
6.3 Pre-Fractionator Systems
7 COMPLEX COLUMNS AND HEAT INTEGRATION
INTERACTIONS
FIGURES
1 DIRECT AND INDIRECT SEQUENCES
2 A SINGLE SIDESTREAM COLUMN REPLACING 2
SIMPLE COLUMNS
3 A TYPICAL MULTI-FEED COLUMN
4 TYPICAL GRAND COMPOSITION CURVE
5 TYPICAL INDIRECT SEQUENCE WITH VAPOUR LINK
6 SIDESTREAM STRIPPER AND SIDESTREAM
RECTIFIER
7 SIMPLEST PRE-FRACTIONATOR SYSTEM
8 SIMPLEST PRE-FRACTIONATOR SYSTEM
9 PETLYUK COLUMN
Elementary and non elementary reaction(no-18) - copyPrawin Ddy
The document discusses the differences between elementary and non-elementary reactions. Elementary reactions occur in a single step, while non-elementary reactions occur through a series of steps. For elementary reactions, the order is the same as the stoichiometric coefficient, but for non-elementary reactions the order does not necessarily match the stoichiometry. Non-elementary reactions are represented by rate equations that may have fractional orders, unlike elementary reactions which always have integer orders.
The document describes a distillation system with multiple units including a feed preheater, reboiler, distillation column, bottom product cooler, top product cooler, and condenser. It provides material and energy balances for the system, including flow rates, temperatures, heat duties, and phases of the streams at each component.
Thermal conversion processes such as thermal cracking, visbreaking, coking, and coke calcination are used to convert heavy hydrocarbon fractions into more valuable products. Thermal cracking involves heating heavy hydrocarbons to high temperatures to crack long molecules into shorter ones. Visbreaking is a mild thermal cracking that reduces the viscosity of heavy residues. Coking uses heat to crack heavy residues into lighter fractions and petroleum coke in large drums. Coke calcination further processes petroleum coke by removing volatiles in a rotary kiln to increase the carbon ratio for uses such as anodes.
Design of Methanol Water Distillation Column Rita EL Khoury
Methanol is an essential feed stock for the manufacture of many industrial products such as adhesives and paints and it is widely used as a solvent in many chemical reactions. Crude methanol is obtained from steam reforming of natural gas and then a purification process is needed since it contains smaller and larger degree of impurities.
The purification process consists of two steps: a topping column used to remove the low boiling impurity called the light ends; and the remaining water methanol mixture is transferred to another column called the refining column where it is constantly boiled until separation occurs. Methanol rises to the top while the water accumulates in the bottom.
This document focuses on methanol water separation. A detailed design study for the distillation column is conducted where the separation occurs at atmospheric pressure with a total condenser and a partial reboiler.
The document discusses chemical processes and various unit operations and processes. It provides examples of important industrial chemical reactions like sulfonation, halogenation, nitration, esterification, hydrogenation, oxidation, hydrolysis and polymerization. It explains the reaction mechanisms, conditions, and applications of these processes. The key reactions covered include electrophilic aromatic substitution, addition reactions, oxidation, hydrolysis, and step-growth polymerization. Industrial applications in production of chemicals, polymers, and other materials are also highlighted.
Van Laar & NRTL Equation in Chemical Engineering ThermodynamicasSatish Movaliya
The document discusses various thermodynamic equations used to model liquid mixtures, including the Van Laar equation, Margules equation, and non-random two-liquid (NRTL) equation. The Van Laar equation relates activity coefficients to effective volume fractions and can be used for vapor-liquid equilibrium calculations. The Margules equation is a simplified case of the Van Laar equation when its constants A and B are equal. The NRTL equation is based on local composition concepts and adjustable parameters to model non-ideal and partially miscible systems.
This document provides information on fluid catalytic cracking (FCC), including:
1) FCC is a process that uses heat and a catalyst to break down large hydrocarbon molecules in vacuum gas oil into smaller molecules like gasoline and light olefins.
2) The catalyst, usually a zeolite, facilitates cracking reactions at lower temperatures and pressures than thermal cracking. During FCC, the catalyst is regenerated by burning off coke deposits.
3) FCC units typically produce gasoline, light olefins like ethylene and propylene, and LPG as products from cracking heavier hydrocarbon feeds.
This presentation discusses the concept of fugacity, which is a measure of a gas's tendency to escape or expand. Fugacity (f) is the effective pressure of a real gas and is related to the ideal gas pressure (P) by the fugacity coefficient (φ). The fugacity coefficient depends on temperature, pressure, and gas properties. Fugacity is important in studying phase and chemical equilibria involving gases at high pressures. The standard state of fugacity relates the molar free energy of real and ideal gases. The temperature and pressure dependence of fugacity are also derived.
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.
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.
1) Material balances apply the law of conservation of mass to chemical processes, ensuring mass is neither created nor destroyed.
2) To perform a material balance, a process flow diagram is drawn with stream labels and unknowns assigned symbols. A basis is selected before writing balance equations.
3) For reactive systems, stoichiometric ratios from chemical equations are used in material balances to determine limiting reactants and calculate yields, selectivity, and conversion.
Slides for the eLearning course Separation and purification processes in biorefineries (https://open-learn.xamk.fi) in IMPRESS project (https://www.spire2030.eu/impress).
Subject: 2.4 Plate efficiencies.
This document describes a study for the production of ethylene glycol through the hydrolysis of ethylene oxide with water. It discusses the significance of ethylene glycol and its uses in various industries such as antifreeze and polyester fibers. The most common manufacturing method is described as the hydrolysis of ethylene oxide through a ring-opening reaction. A flow diagram shows the process which involves hydrating ethylene oxide in a reactor, evaporating the water-glycol mixture in multiple stages, stripping remaining water and purifying through distillation. The study aims to design a process capable of producing 100,000 tons per year of ethylene glycol.
Distillation is the basic and oldest chemical separation process used in the chemical industries and petroleum refining.
Let's recognize the difference between Packed and Plate columns in industry and the comparison of their usage!
Catalytic Reforming Process is one of the most important processes in the petroleum and petrochemical industries which produce high octane number gasoline.
Bioenergetics is the study of energy relationships and conversions in living systems. All biological transformations obey the laws of thermodynamics. A system exchanges either matter or energy or both with its surroundings and includes reactants, products, and the immediate environment. Closed systems exchange energy but not matter, while open systems exchange both. Spontaneous reactions are exergonic with a negative change in free energy, while non-spontaneous reactions are endergonic with a positive change in free energy. Cellular functions depend on endergonic reactions being coupled to exergonic reactions to make the overall process exergonic. Drug-receptor binding affinity is determined by the free energy change and can be calculated from contributions
This document discusses bioenergetics and the laws of thermodynamics. It defines bioenergetics as the quantitative study of energy transduction in living cells, including the release, storage, and use of energy along with the chemical processes underlying these changes. It describes the first and second laws of thermodynamics and how living systems are open systems that exchange both material and energy with their surroundings. It also discusses concepts like Gibbs free energy, entropy, and how cells couple endergonic reactions to exergonic ones through ATP to drive cellular processes.
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
Distillation Sequences, Complex Columns and Heat IntegrationGerard B. Hawkins
Distillation Sequences, Complex Columns and Heat Integration
0 INTRODUCTION/PURPOSE
1 SCOPE
2 FIELD OF APPLICATION
3 DEFINITIONS
4 SEQUENCING OF SIMPLE COLUMNS
4.1 Sidestream Columns
4.2 Multi-Feed Columns
5 SIMPLE COLUMN SEQUENCING AND HEAT
INTEGRATION INTERACTIONS
5.1 Energy Quantity and Quality
5.2 Heat Integration within the Total Flowsheet
6 COMPLEX COLUMN ARRANGEMENTS
6.1 Indirect Sequence with Vapor Link
6.2 Sidestream Systems
6.3 Pre-Fractionator Systems
7 COMPLEX COLUMNS AND HEAT INTEGRATION
INTERACTIONS
FIGURES
1 DIRECT AND INDIRECT SEQUENCES
2 A SINGLE SIDESTREAM COLUMN REPLACING 2
SIMPLE COLUMNS
3 A TYPICAL MULTI-FEED COLUMN
4 TYPICAL GRAND COMPOSITION CURVE
5 TYPICAL INDIRECT SEQUENCE WITH VAPOUR LINK
6 SIDESTREAM STRIPPER AND SIDESTREAM
RECTIFIER
7 SIMPLEST PRE-FRACTIONATOR SYSTEM
8 SIMPLEST PRE-FRACTIONATOR SYSTEM
9 PETLYUK COLUMN
Elementary and non elementary reaction(no-18) - copyPrawin Ddy
The document discusses the differences between elementary and non-elementary reactions. Elementary reactions occur in a single step, while non-elementary reactions occur through a series of steps. For elementary reactions, the order is the same as the stoichiometric coefficient, but for non-elementary reactions the order does not necessarily match the stoichiometry. Non-elementary reactions are represented by rate equations that may have fractional orders, unlike elementary reactions which always have integer orders.
The document describes a distillation system with multiple units including a feed preheater, reboiler, distillation column, bottom product cooler, top product cooler, and condenser. It provides material and energy balances for the system, including flow rates, temperatures, heat duties, and phases of the streams at each component.
Thermal conversion processes such as thermal cracking, visbreaking, coking, and coke calcination are used to convert heavy hydrocarbon fractions into more valuable products. Thermal cracking involves heating heavy hydrocarbons to high temperatures to crack long molecules into shorter ones. Visbreaking is a mild thermal cracking that reduces the viscosity of heavy residues. Coking uses heat to crack heavy residues into lighter fractions and petroleum coke in large drums. Coke calcination further processes petroleum coke by removing volatiles in a rotary kiln to increase the carbon ratio for uses such as anodes.
Design of Methanol Water Distillation Column Rita EL Khoury
Methanol is an essential feed stock for the manufacture of many industrial products such as adhesives and paints and it is widely used as a solvent in many chemical reactions. Crude methanol is obtained from steam reforming of natural gas and then a purification process is needed since it contains smaller and larger degree of impurities.
The purification process consists of two steps: a topping column used to remove the low boiling impurity called the light ends; and the remaining water methanol mixture is transferred to another column called the refining column where it is constantly boiled until separation occurs. Methanol rises to the top while the water accumulates in the bottom.
This document focuses on methanol water separation. A detailed design study for the distillation column is conducted where the separation occurs at atmospheric pressure with a total condenser and a partial reboiler.
The document discusses chemical processes and various unit operations and processes. It provides examples of important industrial chemical reactions like sulfonation, halogenation, nitration, esterification, hydrogenation, oxidation, hydrolysis and polymerization. It explains the reaction mechanisms, conditions, and applications of these processes. The key reactions covered include electrophilic aromatic substitution, addition reactions, oxidation, hydrolysis, and step-growth polymerization. Industrial applications in production of chemicals, polymers, and other materials are also highlighted.
Van Laar & NRTL Equation in Chemical Engineering ThermodynamicasSatish Movaliya
The document discusses various thermodynamic equations used to model liquid mixtures, including the Van Laar equation, Margules equation, and non-random two-liquid (NRTL) equation. The Van Laar equation relates activity coefficients to effective volume fractions and can be used for vapor-liquid equilibrium calculations. The Margules equation is a simplified case of the Van Laar equation when its constants A and B are equal. The NRTL equation is based on local composition concepts and adjustable parameters to model non-ideal and partially miscible systems.
This document provides information on fluid catalytic cracking (FCC), including:
1) FCC is a process that uses heat and a catalyst to break down large hydrocarbon molecules in vacuum gas oil into smaller molecules like gasoline and light olefins.
2) The catalyst, usually a zeolite, facilitates cracking reactions at lower temperatures and pressures than thermal cracking. During FCC, the catalyst is regenerated by burning off coke deposits.
3) FCC units typically produce gasoline, light olefins like ethylene and propylene, and LPG as products from cracking heavier hydrocarbon feeds.
This presentation discusses the concept of fugacity, which is a measure of a gas's tendency to escape or expand. Fugacity (f) is the effective pressure of a real gas and is related to the ideal gas pressure (P) by the fugacity coefficient (φ). The fugacity coefficient depends on temperature, pressure, and gas properties. Fugacity is important in studying phase and chemical equilibria involving gases at high pressures. The standard state of fugacity relates the molar free energy of real and ideal gases. The temperature and pressure dependence of fugacity are also derived.
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.
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.
1) Material balances apply the law of conservation of mass to chemical processes, ensuring mass is neither created nor destroyed.
2) To perform a material balance, a process flow diagram is drawn with stream labels and unknowns assigned symbols. A basis is selected before writing balance equations.
3) For reactive systems, stoichiometric ratios from chemical equations are used in material balances to determine limiting reactants and calculate yields, selectivity, and conversion.
Slides for the eLearning course Separation and purification processes in biorefineries (https://open-learn.xamk.fi) in IMPRESS project (https://www.spire2030.eu/impress).
Subject: 2.4 Plate efficiencies.
This document describes a study for the production of ethylene glycol through the hydrolysis of ethylene oxide with water. It discusses the significance of ethylene glycol and its uses in various industries such as antifreeze and polyester fibers. The most common manufacturing method is described as the hydrolysis of ethylene oxide through a ring-opening reaction. A flow diagram shows the process which involves hydrating ethylene oxide in a reactor, evaporating the water-glycol mixture in multiple stages, stripping remaining water and purifying through distillation. The study aims to design a process capable of producing 100,000 tons per year of ethylene glycol.
Distillation is the basic and oldest chemical separation process used in the chemical industries and petroleum refining.
Let's recognize the difference between Packed and Plate columns in industry and the comparison of their usage!
Catalytic Reforming Process is one of the most important processes in the petroleum and petrochemical industries which produce high octane number gasoline.
Bioenergetics is the study of energy relationships and conversions in living systems. All biological transformations obey the laws of thermodynamics. A system exchanges either matter or energy or both with its surroundings and includes reactants, products, and the immediate environment. Closed systems exchange energy but not matter, while open systems exchange both. Spontaneous reactions are exergonic with a negative change in free energy, while non-spontaneous reactions are endergonic with a positive change in free energy. Cellular functions depend on endergonic reactions being coupled to exergonic reactions to make the overall process exergonic. Drug-receptor binding affinity is determined by the free energy change and can be calculated from contributions
This document discusses bioenergetics and the laws of thermodynamics. It defines bioenergetics as the quantitative study of energy transduction in living cells, including the release, storage, and use of energy along with the chemical processes underlying these changes. It describes the first and second laws of thermodynamics and how living systems are open systems that exchange both material and energy with their surroundings. It also discusses concepts like Gibbs free energy, entropy, and how cells couple endergonic reactions to exergonic ones through ATP to drive cellular processes.
This chapter discusses entropy and the second law of thermodynamics. It introduces the concept of entropy and explains that entropy is a measure of disorder in a system. The chapter defines the second law of thermodynamics as stating that the total entropy of the universe increases for any spontaneous process. It provides examples of calculating entropy changes using standard entropy values and explains how entropy can be used to predict spontaneity based on the sign of the change in Gibbs free energy.
1) Bioenergetics is the quantitative study of energy transduction and storage in living cells, along with the chemical processes underlying energy changes.
2) The first law of thermodynamics states that energy is conserved, while the second law states that entropy increases over time as energy spreads out.
3) Living organisms are open systems that maintain internal order by taking in free energy from nutrients or sunlight and releasing entropy as heat to the environment.
1) Thermodynamics describes how changes in temperature, pressure, and composition affect equilibrium in rock systems. It allows prediction of mineral stability and interpretation of mineral compositions.
2) Thermodynamic models use concepts like internal energy, enthalpy, entropy, and Gibbs free energy to describe equilibrium and the direction of spontaneous processes.
3) Phase diagrams visualize thermodynamic stability by showing pressure-temperature-composition conditions where minerals are stable. However, kinetic effects can cause disequilibrium.
1) The document discusses concepts related to thermodynamics including work, heat, entropy, and thermochemical equations.
2) It explains that work and heat are not state functions as their values depend on the path taken, while entropy provides a measure of disorder in a system.
3) Formulas are provided for calculating entropy change during different processes like phase changes, mixing of gases, and chemical reactions.
This document provides definitions and concepts related to physical chemistry and thermodynamics. It begins with an introduction to physical chemistry and its goal of understanding material systems. It then defines key concepts such as macroscopic and microscopic systems, state variables, state functions, and path functions. The document also defines work, heat, processes, and reservoirs. It introduces gas laws such as the ideal gas law and discusses real gases, their behavior compared to ideal gases, and equations of state like the van der Waals equation. It concludes by defining terms like compressibility factor which account for deviations of real gases from ideal gas behavior.
This document provides an overview of key concepts in chemical energetics, including:
1. Enthalpy change (ΔH) describes the energy stored in or released by a chemical reaction. Exothermic reactions (negative ΔH) release energy while endothermic reactions (positive ΔH) absorb energy.
2. Standard enthalpy changes (ΔH°) are used to calculate the enthalpy change of a reaction using Hess's law and reaction pathways.
3. Entropy (ΔS) describes the disorder of a system, which increases in state changes from solid to liquid to gas. Reactions favoring more gaseous products have a positive ΔS.
4. Gibbs
This document provides information about the CYL110 Physical Chemistry course offered at IIT Delhi. It includes details about instructors, grading criteria, recommended textbooks, course contents covering topics in chemical thermodynamics, and descriptions of concepts like the ideal gas model, van der Waals equation of state, and supercritical fluids. The key topics covered are physical chemistry concepts, the gas laws, and thermodynamic properties and processes.
This document discusses bioenergetics and the role of ATP in living systems. It explains that ATP stores and transports chemical energy within cells, which is released through its hydrolysis into ADP and phosphate. The hydrolysis of ATP is highly exergonic, with a large negative standard free energy change of -30.5 kJ/mol. This energy from ATP hydrolysis drives endergonic biochemical reactions and processes, such as the synthesis of glucose-6-phosphate from glucose and phosphate. The energy from ATP hydrolysis is efficiently coupled to these endergonic reactions through a cyclic process of ATP synthesis and breakdown.
The Kinetic Model Theory in Chemical Engineeringctonsierolf
The kinetic model assumes gases are composed of rigid particles in constant random motion that may collide with each other or container walls. The temperature is proportional to average kinetic energy. The ideal gas model neglects interparticle forces and volumes at high temperatures and low pressures. Dalton's law states the total pressure of a gas mixture is the sum of its partial pressures. Real gases deviate from ideality due to intermolecular forces, modeled using equations of state, compressibility factors, and fugacity coefficients. The behavior of a gas depends on whether attractive or repulsive forces dominate.
1) Heat is a form of energy that is transferred between objects at different temperatures. Heat transfer occurs when samples are in contact and energy moves from the higher temperature sample to the lower temperature sample.
2) Enthalpy is a measurement of the total energy of a system and includes both the internal energy and pressure-volume work term. The enthalpy change of a reaction can be determined from standard enthalpies of formation values.
3) Hess's law states that the enthalpy change of an overall chemical process is equal to the sum of the enthalpy changes of the individual steps in that process.
This slide completely describes you about the stuff include in it and also everything about chemical engineeringThis slide completely describes you about the stuff include in it and also everything about chemical engineering. Fluid Mechanics. Thermodynamics. Mass Transfer Chemical Engineering. Energy Engineering, Mass Transfer 2, Heat Transfer,
This document provides an overview of key concepts and equations related to gases in chemistry. It defines gas laws and the kinetic molecular theory, including assumptions like molecules having negligible volume. Common gas laws are described, such as Boyle's, Charles', Dalton's and the combined gas law. Equations are provided for ideal and real gases. The document also covers gas stoichiometry, effusion, diffusion, and Graham's laws relating molecular mass to rates of effusion and diffusion. Strategies are suggested for attacking gas law problems by identifying quantities, writing knowns and unknowns symbolically, choosing the appropriate equation, and solving.
UNIT 8 CHEMICAL KINETICS.pptxUNIT 8 CHEMICAL KINETICS.pptxfatema220366
This document provides an overview of chemical kinetics and key concepts related to reaction rates. It discusses representation of reaction rates, factors that affect reaction rates like concentration, temperature, and catalysts. Activation energy and the activated complex are explained. Different order reactions and molecularity are defined. Rate laws, rate constants, and half-life are also covered. Examples of zero order, first order and second order reactions are given to illustrate concepts.
The document provides an overview of a course on fundamentals of electrochemistry. It includes the lecture topics, instructors, course evaluation details involving assignments and exams. It also covers various electrochemical concepts like energy levels, band structure, Fermi levels, junction potentials, electrochemical thermodynamics using chemical and electrochemical potentials, Gibbs free energy, standard reference states, activity, reaction quotient, Nernst equation and examples of electrochemical cells like Weston cell, Daniell cell.
The document provides an overview of a course on fundamentals of electrochemistry. It includes the lecture topics, instructors, evaluation criteria, and concepts that will be covered over the course such as thermodynamics, electrode kinetics, voltammetric methods, and industrial applications. The course will involve assignments and a final exam. Key concepts that will be discussed include electrochemical potentials, activity, the Nernst equation, and examples of galvanic and electrolytic cells.
This document summarizes Chapter 20 from the textbook "General Chemistry: Principles and Modern Applications" by Petrucci, Harwood, and Herring. The chapter discusses spontaneous change, entropy, free energy, and criteria for spontaneity. It defines key concepts like entropy, the second law of thermodynamics, standard free energy change, and how free energy relates to chemical equilibrium. The chapter also examines how these principles apply to temperature dependence of equilibrium constants and coupled chemical reactions.
The document discusses exergy analysis of thermal systems. Exergy analysis is based on the conservation of mass, conservation of energy, and the second law of thermodynamics. Exergy analysis can be used to design thermal systems, reduce inefficiencies in existing systems, and evaluate system economics. Exergy, unlike energy, is not conserved and can be destroyed by irreversibilities as a system approaches equilibrium with its environment. The document provides examples of calculating the specific exergy of systems.
AI in customer support Use cases solutions development and implementation.pdfmahaffeycheryld
AI in customer support will integrate with emerging technologies such as augmented reality (AR) and virtual reality (VR) to enhance service delivery. AR-enabled smart glasses or VR environments will provide immersive support experiences, allowing customers to visualize solutions, receive step-by-step guidance, and interact with virtual support agents in real-time. These technologies will bridge the gap between physical and digital experiences, offering innovative ways to resolve issues, demonstrate products, and deliver personalized training and support.
https://www.leewayhertz.com/ai-in-customer-support/#How-does-AI-work-in-customer-support
Supermarket Management System Project Report.pdfKamal Acharya
Supermarket management is a stand-alone J2EE using Eclipse Juno program.
This project contains all the necessary required information about maintaining
the supermarket billing system.
The core idea of this project to minimize the paper work and centralize the
data. Here all the communication is taken in secure manner. That is, in this
application the information will be stored in client itself. For further security the
data base is stored in the back-end oracle and so no intruders can access it.
Prediction of Electrical Energy Efficiency Using Information on Consumer's Ac...PriyankaKilaniya
Energy efficiency has been important since the latter part of the last century. The main object of this survey is to determine the energy efficiency knowledge among consumers. Two separate districts in Bangladesh are selected to conduct the survey on households and showrooms about the energy and seller also. The survey uses the data to find some regression equations from which it is easy to predict energy efficiency knowledge. The data is analyzed and calculated based on five important criteria. The initial target was to find some factors that help predict a person's energy efficiency knowledge. From the survey, it is found that the energy efficiency awareness among the people of our country is very low. Relationships between household energy use behaviors are estimated using a unique dataset of about 40 households and 20 showrooms in Bangladesh's Chapainawabganj and Bagerhat districts. Knowledge of energy consumption and energy efficiency technology options is found to be associated with household use of energy conservation practices. Household characteristics also influence household energy use behavior. Younger household cohorts are more likely to adopt energy-efficient technologies and energy conservation practices and place primary importance on energy saving for environmental reasons. Education also influences attitudes toward energy conservation in Bangladesh. Low-education households indicate they primarily save electricity for the environment while high-education households indicate they are motivated by environmental concerns.
We have designed & manufacture the Lubi Valves LBF series type of Butterfly Valves for General Utility Water applications as well as for HVAC applications.
A high-Speed Communication System is based on the Design of a Bi-NoC Router, ...DharmaBanothu
The Network on Chip (NoC) has emerged as an effective
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Excess property determination
1. charitable Trust’s
vishwakarma institute of
technology ,pune
Name Of Students: Rucha Lokhande ,Rucha
Dhavale , Prajakta Kulal , Isha Meshram
Under Guidance Of Dr.Tanushree
Bhattacharjee
1
3. contents
▪ Excess property introduction
▪ Excess volume
▪ Excess gibbs free energy
▪ Entropy of mixing
▪ what is use of Residual property and Excess property
in thermodynamics
▪ Case study
▪ Thermo-calc demo
▪ conclusion
3
11. Entropy of mixing
▪ Consider that a number of ideal gases are separated which are present in a
vessel. Let ni be the number of moles of each gas and Vi is the volume it
occupies. The total entropy
S1 =∑ni (Cv ln T + R ln(Vi + Si) 1
▪ The increase in entropy in mixture: S 2 – S1 = – ∑ ni R ln Xi
▪ Entropy of mixing of 1 mole of the ideal gas:
∆ S m = – R ∑ ni/n ln Xi = –R ∑ Xi ln X
▪ The fraction Xi is less than unity in all cases, the logarithm is negative and
thus ∆ S m is always positive. Thus mixing of gases, always results in
increase in entropy.
11
12. ▷ Entropy and disorder
-The diffusion of initially separated gases
result in an increase in entropy.
- The process has increased the random
distribution of molecules. Spontaneous
conduction of heat results in the random
distribution of kinetic energy of the
atoms.
-Thus spontaneous processes increase
randomness, at the same time increases
entropy
▷ Entropy And Randomness
-This definition of entropy, that it is a
measure of randomness, is one of great
value.
-A measure of entropy changes gives an
indication of structural changes.
-The process of fusion involves
increase in disorder and therefore, the
entropy increase. Greater the disorder,
greater the entropy increase.
-heat of fusion of ice and benzene are
5.26 and 8.27 cal/deg/mol.
12
13. “
▪ In Thermodynamics A Residual Property Is Defined As The
Difference Between A Real Gas Property And An Idea
Gas Property, Both Considered At The
Same Pressure, Temperature, And Composition.
▪ Excess Property Is Difference Between The Value Of The Property
In A Real Mixture And The Value That Would Exist In An Ideal
Solution Under The Same Conditions.
13
Excess property & residual property relationship
14. what is use of Residual property and Excess property
in thermodynamics ?
❑ Excess properties are
usually used with
liquid solutions, or
when we want to
measure deviations
from a non-ideal
solution.
❑ A Residual property is
measure the deviation
from an ideal gas at the
same conditions.
❑ MR = M – Mig
❑ ME = M - Mid
14
15. Excess Chemical Potential
▪ The excess chemical potential is defined as the
difference between the chemical potential of a
given species and that of an ideal gas under the
same conditions.
▪ Ui= U Ideal + U Excess
▪ Useful for homogeneous & non-homogeneous
system 15
16. Experimental method to
determine excess property
• Measurement of density of
liquid & liquid mixture by
densimeter or by RD bottle.
• Measurement of heat of mixture
by calorimeter.
• Ultrasonic velocity by
interferometry.
• Vapor pressure by isoteniscope
16
17. Intermolecular Forces
Dipole-Dipole Interaction
❑ Dipole-dipole
interaction occurs
whenever two polar
molecules get near each
other.
❑ The positively charged
portion of one molecule
is attracted to the
negatively charged
portion of another
molecule.
Ion-Dipole Interaction
❑ Ion-dipole interaction
occurs when an ion
encounters a polar
molecule.
❑ A cation or positive
ion would be attracted
to the negative part of
a molecule and
repelled by the
positive part.
London Dispersion Force
❑ The force between two
nonpolar molecules, is
the weakest of the
intermolecular forces.
❑ The electrons of one
molecule are attracted
to the nucleus of the
other molecule, while
repelled by the other
molecule's electrons.
17
18. 18
Excess property
behavior
✔ Excess properties
are available is
various signs.
✔ Useful to predict
solution
behavior.
✔ Data available at
ambient
temperature 25
degree c.
19. Excess property & property change of mixing
▷ Observe excess property behavior
▷ Mixing process observe the behavior of enthalpy.
Applications:
✔ Predict the data of temperature & composition.
✔ Predict deviation from non ideal behavior.
✔ It inform about the type molecular interactions
19
24. • The HE and VE results
for each mixture were
expressed as a function
of the mole fraction x
of cycloalkanol by the
polynomials
• The values of
coefficients A, and the
standard deviations
o(HE) and a( VE)
obtained by the method
of least squares, with
all points weighted
equally 24
36. Overview
BENIFITS
Thermo-Calc can be used to understand
many different phases in the life-cycle of
a material, such as:
• Alloy and materials development
• Metallurgical extraction and refining
• Additive Manufacturing
• Casting
• Forging/Hot rolling
• Heat treatment
• Joining/Welding/Soldering
• Quality control
• Materials selection
• Corrosion
• Underlying causes of failure
• Waste and recycling
APPLICATION
• Reduce costly, time-consuming
experiments and testing.
• Increase the value of experiments
• Optimize and define safe processing
windows.
• Shorten development time Build and
safeguard intellectual knowledge
• Improve the quality and consistency of
products through deeper understanding
• Make predictions that are difficult
CALCULATION
• Stable and meta-stable
• Amounts of phases and
their compositions
• Phase transformation
• Phase diagrams
• Thermochemical data
• Driving force for phase
transformations
• Solidification
• Thermodynamic properties
• Pourbaix diagrams
36
37. Phase Daigram
• The term phase diagram
often means a T-x type of
diagram for binary systems
but the term is used here for
any type of diagram with
two or more independent
state variables used as axis
variables.
• Phase diagram gives
information about the state
of a system for any value of
the state variables.
Property Daigram
• A property diagram plots
the value of a dependent
property against an
independent variable, such
as the carbon activity
versus temperature in
steels.
• In multicomponent
systems, property diagrams
are often more useful than
phase diagrams.
Plotting
• A phase diagram is
calculated with the POLY
module using the MAP
command. At least two
axis variables should be
set in the POLY module.
• A property diagram is
calculated with the POLY
module using the STEP
command. Only one axis
variable should be set in
the POLY module. 37
40. Conclusion
In Detailed
Theoretical Study of
Excess Property
Determination of excess
property can se done by
both Experimental and
Simulation Method
•• Experimental Method is
bite costly and time
Consumping
•• Simulation is easy to
understand , and time
saving
Overview of
Thermo-Cal is been
Studied
•• Various
Thermodynamic
Property Diagram can
be easily Plotted.
•• Predication which are
difficult can also be
easily Solve
40
41. Reference
▷ www.wikipedia.com
▷ Anping Liu & Rakesh Govind (1995) Determination of Thermodynamic Excess Properties of Mixtures
from Computer Simulation, Molecular Simulation, 15:1, 47-55, DOI: 10.1080/08927029508022328
▷ Elliott, J. Richard; Lira, Carl T. (2012). Introductory Chemical Engineering
Thermodynamics. Upper Saddle River, New Jersey: Prentice Hall. ISBN 978-0-13-606854-9.
▷ Frenkel, Daan; Smit, Berend (2001). Understanding Molecular Simulation : from algorithms to
applications. San Diego, California: Academic Press. ISBN 978-0-12-267351-1
41