31.1 Thermodynamics of Mixing of Ideal Solutions For the process where solute and solvent are mixed to form an ideal solution at constant temperature and.

Slides:



Advertisements
Similar presentations
We will call μ the Chemical Potential Right now we will think of it as the molar free energy, but we will refine this definition later… Free Energy.
Advertisements

Thermodynamic Potentials
Learning Objectives and Fundamental Questions What is thermodynamics and how are its concepts used in petrology? How can heat and mass flux be predicted.
Department of Civil & Environmental Engineering
Solutions Lecture 6. Clapeyron Equation Consider two phases - graphite & diamond–of one component, C. Under what conditions does one change into the other?
1 Mathematical Methods Physics 313 Professor Lee Carkner Lecture 22.
(Q and/or W) A closed system is one that does not exchange matter with its surroundings, although it may exchange energy. dn i = 0(i = 1, 2, …..)(1.1)
First Law of Thermodynamics
SIMPLE MIXTURES THERMODYNAMIC DESCRIPTION OF MIXTURES ARYO ABYOGA A ( ) GERALD MAYO L ( ) LEONARD AGUSTINUS J ( )
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
Observables. Molar System The ratio of two extensive variables is independent of the system size.  Denominator N as particle  Denominator N as mole.
Solution thermodynamics theory—Part IV
Mathematical Methods Physics 313 Professor Lee Carkner Lecture 20.
Spontaneity and Equilibrium in Chemical Systems
Chapter 3 Phase Transitions and Chemical Reactions.
Ch. 9 K&K: Gibbs Free Energy and Chemical Reactions Recall (ch. 8): Free energyconditions. Helmholtz F isothermal Enthalpy H constant pressure Gibbs G.
Properties of Solutions
1 Lecture 2 Summary Summary 1) The Zeroth Law: Systems that have no tendency to transfer heat are at the same temperature. 2) Work: A process which transfers.
THERMODYNAMIC PROPERTY RELATIONS
Daniel L. Reger Scott R. Goode David W. Ball Chapter 17 Chemical Thermodynamics.
Chapter 19 Chemical Thermodynamics. First Law of Thermodynamics Energy cannot be created nor destroyed. Therefore, the total energy of the universe is.
The Third Law, Absolute Entropy and Free Energy Lecture 4.
Entropy changes in irreversible Processes
1 The Second Law of Thermodynamics (II). 2 The Fundamental Equation We have shown that: dU = dq + dw plus dw rev = -pdV and dq rev = TdS We may write:
Department of Mechanical Engineering ME 322 – Mechanical Engineering Thermodynamics Lecture 17 Unsteady State (Transient) Analysis.
Chapter 19 Chemical Thermodynamics Lecture Presentation John D. Bookstaver St. Charles Community College Cottleville, MO © 2012 Pearson Education, Inc.
Dr Ku Syahidah Ku Ismail CHAPTER 5 STANDARD THERMODYNAMIC FUNCTIONS OF REACTION.
Percent by mass, mole fraction, molarity, and molality
33.1 Temperature Dependence of Gibbs’ Free Energy Methods of evaluating the temperature dependence of the Gibbs’ free energy can be developed by beginning.
1. (1.3) (1.8) (1.11) (1.14) Fundamental equations for homogeneous closed system consisting of 1 mole:
The Second Law of Thermodynamics
Partial Molar Quantities and the Chemical Potential Lecture 6.
7.6 Entropy Change in Irreversible Processes It is not possible to calculate the entropy change ΔS = S B - S A for an irreversible process between A and.
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.
1 Chapter 7. Applications of the Second Law. 2 Consider entropy changes in various reversible (!!!) processes We have: (a) Adiabatic process Hence a reversible.
Chapter 4: Applications of the First Law Different types of work: Configuration work: (reversible process) Dissipative work: (irreversible process) Adiabatic.
Solution thermodynamics theory—Part I
6. Coping with Non-Ideality SVNA 10.3
Lecture 6. NONELECTROLYTE SOLUTONS. NONELECTROLYTE SOLUTIONS SOLUTIONS – single phase homogeneous mixture of two or more components NONELECTROLYTES –
Chapter 8: The Thermodynamics of Multicomponent Mixtures
Entropy Property Relationships Chapter 7b. The T-ds relations Consider an internally reversible process occurring in a closed system.
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.
Chemical Equilibrium By Doba Jackson, Ph.D.. Outline of Chpt 5 Gibbs Energy and Helmholtz Energy Gibbs energy of a reaction mixture (Chemical Potential)
Solution thermodynamics theory—Part IV
Chapter 20 Energy and Disorder.
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
Ideal and Dilute Solutions 2/21/2016. Master Thermodynamics Equations.
Clapeyron and Clausius Clapeyron Equations
A Brief Review of Thermodynamics. Internal Energy and the First Law The infinitesimal change in the internal energy  For a general process The First.
Classical Thermodynamics of Solutions
Solutions. Definitions Solution: homogeneous mixture of 2 or more substances in a single physical state Solute: the substance dissolved in the solution.
Solution thermodynamics theory—Part III
Chapter 17 Notes1 Chapter 17 Thermodynamics: Entropy, Free Energy and Equilibrium 1. review of terms; definitions; 2. Is it spontaneous? 3. entropy; some.
11.1 1st Law of Thermodynamics A law is a statement which summarizes our experiences. Among the most fundamental laws (there are no known exceptions to.
Gibbs-Duhem and the Chemical Potential of Ideal Solutions
PHYSICAL CHEMISTRY ERT 108 Semester II 2011/2012
Solution thermodynamics theory—Part IV
Solution of Thermodynamics: Theory and applications
Thermodynamic Processes
Classical Thermodynamics of Multicomponent Systems
Mr. Kinton Honors Chemistry
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.
Partial Molar Variables, Chemical Potential, Fugacities, Activities, and Standard States Partial molar thermodynamic variables with respect to species.
Unsteady State (Transient) Analysis
Ch. 5: Applications Using Maxwell Relations & Measurable Properties
11 CHAPTER Thermodynamic Property Relations.
Chapter 19 Part 3: Free Energy.
Chapter 19 Part 3: Free Energy.
Presentation transcript:

31.1 Thermodynamics of Mixing of Ideal Solutions For the process where solute and solvent are mixed to form an ideal solution at constant temperature and pressure: T, P solute(s) + solvent > ideal solution we have already calculated the entropy of mixing for forming and ideal solution isothermally and isobarically (see the course notes on Entropy of Mixing of Ideal Solutions):  S mix = - R  X i ln X i (per mole of components) This result can be used to calculate the Gibb’s free energy of mixing of an ideal solution starting with a result we have derived earlier (see course notes on Maxwell’s Relations): dG = V dP - S dT Dividing by dT, while holding the pressure constant gives: (  G /  T) P = - S This result can be applied to the mixing process occurring at constant temperature and pressure: (  G mix /  T) P = -  S mix  = + R  X i ln X i

31.2 Separating variables and integrating this expression from 0 K to T: 0   G mix d (  G mix ) = 0  T R  X i ln X i dT Can you justify why  G mix  0 at 0 K? gives an expression for the Gibb’s free energy of mixing to form an ideal solution in an isothermal isobaric process:  G mix  = R T  X i ln X i What would a plot of  G mix  versus mole fraction of the solute look like for a binary solution? We can now use a rearrangment of the definition of Gibb’s free energy: H = G + T S to calculate the enthalpy of mixing to form an ideal solution in an isothermal isobaric process:  H mix =  G mix + T  S mix = (R T  X i ln X i ) + T (- R  X i ln X i ) = 0 When concentrated sulfuric acid is mixed with water enough heat can be generated to cause the solution to boil. Do sulfuric acid and water form an ideal solution? Can you explain why the interaction of sulfuric acid and water is so exothermic based on their molecular structures?

31.3 To calculate the volume change on mixing to form an ideal solution we begin with: dG = V dP - S dT and divide by dP, while holding the temperature constant to obtain a partial derivative indicating how the Gibbs’ free energy changes with pressure: (  G /  P) T = + V which gives for the change in volume on mixing to form an ideal solution isothermally and isobarically:  V mix = (  G mix /  P) T = (  (R T  X i ln X i ) /  P) T = 0 Why is the partial derivative of  G mix  taken while holding the temperature constant, equal to zero? When 10.0 mL of concentrated sulfuric acid is mixed with 90.0 mL water the final volume is ~ 98.0 mL. Do sulfuric acid and water form an ideal solution? Can you explain this observation in terms of the molecular structure of sulfuric acid and water?

31.4 Finally we can use a rearrangement of the definition of enthalpy: E = H - P V to calculate the internal energy change for mixing to form an ideal solution isothermally and isobarically:  E mix =  H mix - P  V mix = 0 - P (0) = 0 Could you explain why  E mix is zero based on the postulates that define an ideal solution?