Thermodynamic Consistency

Slides:



Advertisements
Similar presentations
The theoretical background of
Advertisements

CHEE 311Lecture 161 Correlation of Liquid Phase Data SVNA 12.1 Purpose of this lecture: To show how activity coefficients can be calculated by means of.
Advanced Thermodynamics Note 11 Solution Thermodynamics: Applications
Solution thermodynamics theory—Part I
SIMPLE MIXTURES THERMODYNAMIC DESCRIPTION OF MIXTURES ARYO ABYOGA A ( ) GERALD MAYO L ( ) LEONARD AGUSTINUS J ( )
Chem Ch 23/#2 Today’s To Do List
Chapter 14-Part VII Applications of VLLE.
Solution Thermodynamics: Applications
Lecture 18Multicomponent Phase Equilibrium1 Theories of Solution The Gibbs energy of mixing is given by: And the chemical potential is: For ideal gases,
Thermodynamic Property Relations
The Advanced Chemical Engineering Thermodynamics The variables (thermodynamic properties) and the equations in thermodynamics Q&A -2- 9/22/2005(2) Ji-Sheng.
Solution thermodynamics theory—Part IV
Now we introduce a new concept: fugacity
Excess Gibbs Energy Models
Implicit Differentiation. Objectives Students will be able to Calculate derivative of function defined implicitly. Determine the slope of the tangent.
Faculty Instructor Prof. J.Ballare Lab TA’s M.V. Ramesh (M.Tech) D.Sateesh (PhD ) TH 206 Vapor Liquid Equilibrium.
7.1 Graphing Linear Systems
Notation convention Let G' stand for total free energy and in a similar fashion S', V', H', etc. Then we will let = G'/n represent the free energy per.
Error Analysis, Statistics, Graphing and Excel Necessary skills for Chem V01BL.
Sec 1.5 Scatter Plots and Least Squares Lines Come in & plot your height (x-axis) and shoe size (y-axis) on the graph. Add your coordinate point to the.
VAPOR/LIQUID EQUILIBRIUM- Introduction
1. (1.3) (1.8) (1.11) (1.14) Fundamental equations for homogeneous closed system consisting of 1 mole:
Thermodynamics Properties of Fluids
3.1 Solving equations by Graphing System of equations Consistent vs. Inconsistent Independent vs. Dependent.
32.1 Pressure Dependence of Gibbs’ Free Energy Methods of evaluating the pressure dependence of the Gibbs’ free energy can be developed by beginning with.
Summary Part 1 Measured Value = True Value + Errors = True Value + Errors Errors = Random Errors + Systematic Errors How to minimize RE and SE: (a)RE –
Solution thermodynamics theory—Part I
CHEE 311J.S. Parent1 4. Chemical Potential in Mixtures When we add dn moles of a component to n moles of itself, we will observe (?) a change in Gibbs.
Multi-component Homogeneous System: Solution Thermodynamics
Solution thermodynamics theory—Part IV
ACTIVITY AND ACTIVITY COEFFICIENT
42C.1 Non-Ideal Solutions This development is patterned after that found in Molecular Themodynamics by D. A. McQuarrie and John D. Simon. Consider a molecular.
Solution thermodynamics theory
Error Analysis, Statistics, Graphing and Excel Necessary skills for Chem V01BL.
SOLUTION THERMODYNAMICS:
Residual Properties Team Members: Sergio Luna Ain Lockman Kimberly Cagle Harisimran Jakhar.
Classical Thermodynamics of Solutions
$100 $200 $300 $400 $500 $100 $200 $300 $400 $500 $100 $200 $300 $400 $500 $100 $200 $300 $400 $500 $100 $200 $300 $400 $500 $100 $200 $300.
Chemical Engineering Thermodynamics-II Topic: Excess Gibbs Free Energy, Data Reduction, Thermodynamic Consistency Prepatred by:- Patel Nirav ( )
G.H.PATEL COLLEGE OF ENGINEERING AND TECHNOLOGY Chemical Engineering Thermodynamics-2 Code – Topic:-Fugacity and Fugacity coefficient for pure.
Solution thermodynamics theory—Part III
Students should be able to: 1. Use the equilibrium constant expressed in terms of partial pressures (Kp) and relate Kp to Kc. 2. Describe heterogeneous.
Shroff S.R. Rotary Institute of Chemical Technology Chemical Engineering Chemical Engineering Thermodynamics-II 1.
Vapor – Liquid Equilibrium
Exam #3 1. You should know from memory:
Prepared By Hitesh N. Panchal Assistant Professor
Solution thermodynamics theory—Part IV
Warm Up Determine for y2 + xy + 3x = 9.
SUBJECT:-CHEMICAL ENGINEERING THERMODYNAMICS 2 TOPIC:- DISCUSS GIBSS DUHEM EQUATION. - CALCULATION OF PARTIAL PROPERTIES FROM.
Chem. Eng. Thermodynamics (TKK-2137)
Solution of Thermodynamics: Theory and applications
공정 열역학 Chapter 6. Thermodynamic Properties of Fluids
Ch.3. Thermodynamics for Geochemistry
Faulty of engineering, technology & research
G.H. Patel College of Engineering and Technology
} C = 1 F = 2 P = 1 Gibbs phase rule F = C – P + 2
Classical Thermodynamics of Multicomponent Systems
Classification of Differential Equations
THERMODYNAMIC PROPERTIES OF FLUIDS
Don’t be in a such a hurry to condemn a person because he doesn’t do what you do, or think as you think. There was a time when you didn’t know what you.
The theoretical background of
Modified by Jed Macosko
Applied Geochemistry & Lab Ch.2 Thermodynamics of Solutions
7.2 Solving Systems of Equations Algebraically
Partial Derivatives and associated relations SMES1202 khkwek.
Ch. 5: Applications Using Maxwell Relations & Measurable Properties
Phase diagrams and phase transitions of unary systems
11 CHAPTER Thermodynamic Property Relations.
SYSTEM OF LINEAR EQUATIONS
Presentation transcript:

Thermodynamic Consistency Avi Vegda (130990105062) Ankit Vashi(130990105061) Parth Patel(120990105001) Guided By Janki Tailor

Thermodynamic Consistency The Gibbs/Duhem Equation imposes a constraint on activity coefficient that may not be satisfied by a set of experimental values derived from P-xy data. The experimental values of ln γ1 and ln γ2 combine by (excess Gibbs free energy) to give values of GE/RT. This addition process is independent of the Gibbs/Duhem Equation.

Nor can a P-xy correlation Calculated by modify Roults low be consistent with experimental values. If the experimental data are inconsistent with the Gibbs/Duhem equation , they are necessarily incorrect as the result of systematic error in the data. Because correlating equations for GE/RT impose consistency on derived activity coefficients, no such correlation exists that can precisely reproduce P-xy data that are inconsistent. Our purpose now is to develop a simple test for the consistency with respect to the Gibbs/Duhem equation of a P-xy data set.

 

 

 

Using slope in curve Gibb’s- duhem eqn

To verify consistancy exit or not plot, graph

Using Mid-Point Data In Van- Laar eqn. put

at

Redlich/ Kister method Diff … w.r.t x1

Now , In between x1=0 to x2=1

at Plot Vs

Using coexistence equation:- Modified Raoult’s law consider vap. Phase is ideal gas Gibbs/Duhem equation

at const T. by Antion eqn.

(5) Using Partial pressure data [ low pressure system] Gibbs/Duhem equation

Thank You…