Solution Thermodynamics: Applications

Slides:



Advertisements
Similar presentations
Diffusion Mass Transfer
Advertisements

Fugacity of Non-Ideal Mixtures (SVNA 11.6 and 11.7)
Thermodynamic Property Methods
Property Methods In Aspen Plus
Real Solutions Lecture 7.
Chapter 07: Simple Mixtures
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
Activities in Non-Ideal Solutions
2. Solubility and Molecular Weights Polymer Solubility1.
Vapor and Liquid Equilibrium
SIMPLE MIXTURES THERMODYNAMIC DESCRIPTION OF MIXTURES ARYO ABYOGA A ( ) GERALD MAYO L ( ) LEONARD AGUSTINUS J ( )
Solid-vapor equilibrium (SVE) and Solid-liquid equilibrium (SLE)
Chemical Reaction Equilibria
Chapter 14: Phase Equilibria Applications
Separation of Water and Alcohols using 1-hexyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide 1 Alexandre Chapeaux, Luke D. Simoni, Mark A. Stadtherr,
Lecture 18Multicomponent Phase Equilibrium1 Theories of Solution The Gibbs energy of mixing is given by: And the chemical potential is: For ideal gases,
Solution thermodynamics theory—Part IV
CHEE 311J.S. Parent1 7. Liquid Phase Properties from VLE Data (11.1) The fugacity of non-ideal liquid solutions is defined as: (10.42) from which we derive.
Solution Thermodynamics: Applications
Now we introduce a new concept: fugacity
Excess Gibbs Energy Models
EGR 334 Thermodynamics Chapter 12: Sections 1-4
Diffusion Mass Transfer
SIMPLE MIXTURES Chapter 5.
Ideal Gases. Now that we know how gases behave when we manipulate P, V, and T, it’s time to start thinking about how to deal with things like moles and.
Advanced Thermodynamics Note 9 Vapor/Liquid Equilibrium: Introduction
Dicky Dermawan ITK-234 Termodinamika Teknik Kimia II Nonideal Behavior Dicky Dermawan
Advance Chemical Engineering Thermodynamics
Dr Saad Al-ShahraniChE 334: Separation Processes  Nonideal Liquid Solutions  If a molecule contains a hydrogen atom attached to a donor atom (O, N, F,
4.6 Real solution: activity of solute and solvent
Solutions and Mixtures Chapter 15 # Components > 1 Lattice Model  Thermody. Properties of Mixing (S,U,F,  )
Physical Chemistry I (TKK-2246) 14/15 Semester 2 Instructor: Rama Oktavian Office Hr.: M – F
Ch 24 pages Lecture 9 – Flexible macromolecules.
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 –
Mixing in water Solutions dominated by water (1 L=55.51 moles H 2 O) a A =k H X A where K H is Henry’s Law coefficient – where is this valid? Low concentration.
Simple Lattice Model for Fluids. Introduction In this chapter we borrow the idea of lattice structures, characteristic of crystals, and apply it to develop.
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.
Applications of Intermolecular Potentials. Example 1. A gas chromatograph is to be used to analyze CH 4 -CO 2 mixtures. To calibrate the response of the.
Thermodynamics of Associating Fluids 1. Chains of molecules Many molecules are not spherical, but could be represented as consisting of connected spherical.
Activity Coefficient Estimation Methods
Generalized van der Waals Partition Function
Solution thermodynamics theory—Part IV
Second virial coefficient
Theory of dilute electrolyte solutions and ionized gases
APPLICATIONS Applications of Raoult’s law
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.
Introduction to phase equilibrium
Solution thermodynamics theory
Ideal and Dilute Solutions 2/21/2016. Master Thermodynamics Equations.
8. Solute (1) / Solvent (2) Systems 12.7 SVNA
SOLUTION THERMODYNAMICS:
CHAPTER 9 Fugacity of a component in a mixture
Classical Thermodynamics of Solutions
1 Calculation of Radial Distribution Function (g(r)) by Molecular Dynamic.
Solution Thermodynamics: Applications Chapter 12-Part IV.
Chapter 14: Phase Equilibria Applications Part II.
Solution thermodynamics theory—Part III
Partial Properties: Thought Experiment
Prepared By Hitesh N. Panchal Assistant Professor
Solution thermodynamics theory—Part IV
Chemistry II Objectives Unit II - Chapter 2-4
Solution of Thermodynamics: Theory and applications
Classical Thermodynamics of Multicomponent Systems
Diffusion Mass Transfer
Phase Equilibrium.
Pure Substance and Two property Rule
Presentation transcript:

Solution Thermodynamics: Applications Chapter 12-Part IV

Other models for GE/RT

The Van-Laar equation

Local composition theory There are cases where the cross-parameter may be a function of composition. A12 = A12(x) So, there could be “local” compositions different than the overall “bulk” compositions. For example (if coordination number is 8) AAAAAAA AABBAAA xAB = ; xBB = “A around B” or “B around B”

examples Specific interactions such as H-bonding and polarity

Nomenclature x21 = mole fraction of “2” around “1” x11 + x21 =1 112211 111111 x12 = mole fraction of “1” around “2” x22 = mole fraction of “2” around “2” x22 + x12 =1 Local compositions are related to overall compositions: If the weighting functions are =1 random solutions

Key are the Wij weighting factors If Wij =1 => random mixture

Wilson equation Wilson assumes that the weighting functions are functions of size and energetic interactions: z is the coordination number for atom i even if eij =eji (this is not always the case), the Lij parameters may be different, why?

Intermolecular pair potential Uij eij

Wilson’s equation for a binary For infinite dilution:

NRTL (non-random, two-liquid) Actual parameters: a, b12 and b21 See Table 12.5, page 474 Renon and Prausnitz, 1968

page 474

UNIQUAC equation UNIversal QUAsi Chemical model (Abrams and Prausnitz, AIChE J. 21:116 (1975) Uses surface areas (qi) to represent shapes qi is proportional to the surface area of i z is the coordination number

UNIQUAC cont. coordination number, z = 10 qj accounts for shape, rj accounts for size Energetic parameters tji=exp-(eji-eii)/RT= exp [(-aji)/RT] Pure species molecular parameters (in tables): r1, r2, q1, q2 ri are molecular size parameters relative to –CH2-

Activity coefficients from UNIQUAC

UNIFAC (UNIQuac Functional Activity Coefficient model) The solution is made of molecular fragments (subgroups) New variables (Rk and Qk) Combinatorial part is the same as UNIQUAC where Fk and qk are the volume fractions and surface fractions

Residual part of UNIFAC is different i identify species # of subgroups k in molecule i Be careful, this q is different than the surface fraction !!

Property changes of mixing We showed that for ideal solutions: From these properties we can evaluate ME = M - Mid

Property changes of mixing Let’s define:

Property changes of mixing This means that the excess properties and the properties change of mixing can be calculated from each other What are the DM for ideal solutions?

Mixing process at T and P