V T for n & P = constant

Similar documents
Review of Classical Thermodynamics

Introduction to Statistical Methods

3-1 Introduction: 3-2 Spontaneous (Natural) Process:

Thermodynamics General

Appendix II Summary of Important Equations

Chemical Equilibrium. Chapter 6 Spontaneity of Reactive Mixtures (gases) Taking into account there are many types of work that a sysem can perform

Energy, Entropy, and Availability Balances Phase Equilibria. Nonideal Thermodynamic Property Models. Selecting an Appropriate Model

Lecture. Polymer Thermodynamics 0331 L Chemical Potential

Chapter 5 rd Law of Thermodynamics

...Thermodynamics. If Clausius Clapeyron fails. l T (v 2 v 1 ) = 0/0 Second order phase transition ( S, v = 0)

#64. ΔS for Isothermal Mixing of Ideal Gases

Introduction to Vapor/Liquid Equilibrium, part 2. Raoult s Law:

Chapter 18, Part 1. Fundamentals of Atmospheric Modeling

Chemistry 163B Free Energy and Equilibrium E&R ( ch 6)

Thermodynamics II. Department of Chemical Engineering. Prof. Kim, Jong Hak

between standard Gibbs free energies of formation for products and reactants, ΔG! R = ν i ΔG f,i, we

If two volatile and miscible liquids are combined to form a solution, Raoult s law is not obeyed. Use the experimental data in Table 9.

Problem Set #6 solution, Chem 340, Fall 2013 Due Friday, Oct 11, 2013 Please show all work for credit

A quote of the week (or camel of the week): There is no expedience to which a man will not go to avoid the labor of thinking. Thomas A.

NAME and Section No. it is found that 0.6 mol of O

Gasometric Determination of NaHCO 3 in a Mixture

Outline. Unit Eight Calculations with Entropy. The Second Law. Second Law Notes. Uses of Entropy. Entropy is a Property.

Open Systems: Chemical Potential and Partial Molar Quantities Chemical Potential

Solution Thermodynamics

3. Be able to derive the chemical equilibrium constants from statistical mechanics.

( ) 1/ 2. ( P SO2 )( P O2 ) 1/ 2.

NAME and Section No.

Supplementary Notes for Chapter 9 Mixture Thermodynamics

Name: SID: Discussion Session:

University of Washington Department of Chemistry Chemistry 452/456 Summer Quarter 2014

CHEMICAL REACTIONS AND DIFFUSION

General Formulas applicable to ALL processes in an Ideal Gas:

Physical Chemistry I for Biochemists. Chem340. Lecture 16 (2/18/11)

Thermodynamics Second Law Entropy

Thermodynamics and Gases

Irreversibility of Processes in Closed System

Einstein Classes, Unit No. 102, 103, Vardhman Ring Road Plaza, Vikas Puri Extn., Outer Ring Road New Delhi , Ph. : ,

Assignment 4. Adsorption Isotherms

2. Introduction to Thermodynamics

G4023 Mid-Term Exam #1 Solutions

Mass Transfer Processes

Physics 240: Worksheet 30 Name:

Topic 3 : Thermodynamics

Chapter 3 Thermochemistry of Fuel Air Mixtures

The ChemSep Book. Harry A. Kooijman Consultant. Ross Taylor Clarkson University, Potsdam, New York University of Twente, Enschede, The Netherlands

Name ID # For relatively dilute aqueous solutions the molality and molarity are approximately equal.

Exercises of Fundamentals of Chemical Processes

Temperature. Chapter Heat Engine

Lecture 3 Examples and Problems

Homework Chapter 21 Solutions!!

First Law CML 100, IIT Delhi SS. The total energy of the system. Contribution from translation + rotation + vibrations.

Solution Thermodynamics

Envr 210, Chapter 3, Intermolecular forces and partitioning Free energies and equilibrium partitioning chemical potential fugacity activity coef.

General Thermodynamics for Process Simulation. Dr. Jungho Cho, Professor Department of Chemical Engineering Dong Yang University

and Statistical Mechanics Material Properties

PETE 310 Lectures # 24 & 25 Chapter 12 Gas Liquid Equilibrium

Non-Ideality Through Fugacity and Activity

PART I: MULTIPLE CHOICE (32 questions, each multiple choice question has a 2-point value, 64 points total).

Homework Week 8 G = H T S. Given that G = H T S, using the first and second laws we can write,

a for save as PDF Chemistry 163B Introduction to Multicomponent Systems and Partial Molar Quantities

Equation of State Modeling of Phase Equilibrium in the Low-Density Polyethylene Process

Chapter One Mixture of Ideal Gases

University of Washington Department of Chemistry Chemistry 452/456 Summer Quarter 2014

Physics 3 (PHYF144) Chap 2: Heat and the First Law of Thermodynamics System. Quantity Positive Negative

3) Thermodynamic equation to characterize interfaces

ME 300 Exam 2 November 18, :30 p.m. to 7:30 p.m.

Electrochemical Equilibrium Electromotive Force

4.2 Chemical Driving Force

Estimation of the composition of the liquid and vapor streams exiting a flash unit with a supercritical component

University of Washington Department of Chemistry Chemistry 453 Winter Quarter 2015

y i x P vap 10 A T SOLUTION TO HOMEWORK #7 #Problem

Transfer Functions. Convenient representation of a linear, dynamic model. A transfer function (TF) relates one input and one output: ( ) system

2. Under conditions of constant pressure and entropy, what thermodynamic state function reaches an extremum? i

Module 3: The Whole-Process Perspective for Thermochemical Hydrogen

Determination of Structure and Formation Conditions of Gas Hydrate by Using TPD Method and Flash Calculations

I wish to publish my paper on The International Journal of Thermophysics. A Practical Method to Calculate Partial Properties from Equation of State

Outlet temperature of a WGS reactor (Stage I) for the conversion of CO, applied for the abatement of CO to a fixed value.

10.34 Numerical Methods Applied to Chemical Engineering Fall Homework #3: Systems of Nonlinear Equations and Optimization

Computation of Phase Equilibrium and Phase Envelopes

Gouy-Chapman model (1910) The double layer is not as compact as in Helmholtz rigid layer.

THERMODYNAMICS CONTENTS

CinChE Problem-Solving Strategy Chapter 4 Development of a Mathematical Model. formulation. procedure

Chapters 18 & 19: Themodynamics review. All macroscopic (i.e., human scale) quantities must ultimately be explained on the microscopic scale.

CHEMICAL ENGINEERING

Chemical Reaction Engineering

Physics 115. Molecular motion and temperature Phase equilibrium, evaporation

Lecture 8. Chapter 7. - Thermodynamic Web - Departure Functions - Review Equations of state (chapter 4, briefly)

Chapter 6 : Gibbs Free Energy

CHAPTER 6. LAGRANGE S EQUATIONS (Analytical Mechanics)

Physics 607 Exam 1. ( ) = 1, Γ( z +1) = zγ( z) x n e x2 dx = 1. e x2

Pressure Volume Work 2

Physical Chemistry I for Biochemists. Lecture 18 (2/23/11) Announcement

ESCI 341 Atmospheric Thermodynamics Lesson 6 Thermodynamic Processes

Lecture 2 Grand Canonical Ensemble GCE

Chap.5 Statistical Thermodynamics

Chemical Engineering Department University of Washington

Exam 2 Solutions. for a gas obeying the equation of state. Z = PV m RT = 1 + BP + CP 2,

CHEMISTRY Midterm #2 answer key October 25, 2005

Lecture 5. Stoichiometry Dimensionless Parameters. Moshe Matalon N X. 00 i. i M i. i=1. i=1

CHAPTER 7 ENERGY BALANCES SYSTEM SYSTEM. * What is energy? * Forms of Energy. - Kinetic energy (KE) - Potential energy (PE) PE = mgz

Transcription:

Pchem 365: hermodynamcs -SUMMARY- Uwe Burghaus, Fargo, 5 9 Mnmum requrements for underneath of your pllow. However, wrte your own summary! You need to know the story behnd the equatons : Pressure : olume n: partcle number trp : temperature of trple pont of water R: Gas constant α: phase of a system? : standard value of a therm. functon ( bar, and typcally at room temperature X: mole fracton P c : pressure at crtcal pont Be aware of typos. IDEAL GAS (no nteractons no volume of the speces (More realstc equatons such as the van der Waals equaton nclude the nteracton of the partcles and there volume. Boyl s law P for n & constant for n & P constant Gay-Lussac & Charles laws R S p for n & constant Avogadro s law n for P & constant Equal volumes of dfferent gases have equal numbers of partcles f and p are constant. Or, p,, const (.e. are the same for two dfferent gases than the number of partcles n s the same. General deal gas equaton P nr Dalton s law Ptot P + P + P+ 3... A reversble process s one where a system s always nfntesmally close to equlbrum, and an nfntesmal change n condtons can reverse the process to restore both system and surroundngs to ther ntal states. Extensve propertes are equal to the sum of ther values (e.g. volume, mass, heat, c p. Intensve propertes do not depend on the amount of matter (e.g. temperature, densty.

HERMODYNAMIC FUNCIONS mechancal work pressure work heat capactes Enthalpy adabatc expanson (Joule-homson, Lnde apparatus for lquefyng ar, fast expanson of a gas, open suddenly a gas cylnder wthout a regulator don t do that at home z r r w F( dr L r r z z w dw Pd tot L L c dq dq ( ; c ( d d P P const const H U c ( ; c ( c c nr (deal gas P P const const R S P H: U + P H q for P constant U q for constant compare p const (Boyl' s law wth p const (Posson eq / γ γ ( ; P P ; γ R c C P C γ state functons (e.g. U, Cp, Cv z L db b b b; db z non state functons L dq q b s ndependent of the way from ntal ( to fnal ( state z (e.g. q, w

Entropy ds dq ds H ; ( & P const (What s dfference between ds and C p? Gbbs equaton dg dp Sd + µ α dn α k α Important defntons: Enthalpy Helmholz free energy Gbbs energy H U + P A U S G H S 3

Carnot cycle Cycles: x sothermal and x adabatc work output q η + heat nput q Pressure P olume --> sothermal --> 3 adabatc 3 --> 4 sothermal 4 --> adabatc heat work q q w -q -R ln( / q 3 w 3 -c ( - q q 34 w 34 -q -R ln( 4 / 3 q 4 w 4 -c ( - Note that the equaton w 3 -c for an adabatc step s very useful for analyzng these cycles (see above and try to remember that. (Why?: U c for an deal gas that s bascally the defnton of an deal gas-, st law U w + q, adabatc step q. 4

MAERIAL EQUILIBRIUM dsσ dssystem + dssurroundng reversble process > rreversble A:U-S (Helmholts free energy R S U W G:H-S (Gbbs free energy cf., maxmum work for const process (Arbetsfunkton thermodynamc work functon da at equlbrum for & constant cf., maxmum work for P const process dg at equlbrum for &P constant chemcal potental G ( α µ α α n const P const all mole numbers except n const α j phase equlbrum k µ α α dn α α b µ µ µ of speces s the same n every phase that contans In approachng the equlbrum: flows from phase wth larger µ to phase wth lower µ. µ µ + R ln(p /P (deal gas & P const or @ & const reacton equlbrum ν A+ ν A+... ν mam + ν m+ Am+ +... νµ 5

PHASE DIAGRAMS Phase rule: f pc+ p c( p r a Isotherms of H O f: degree of freedom; constrants: number of p: phases; c: speces; r: reactons; a: other restrctons such as stochometry, conservaton of charge Example: H O sold phase regon (f ; lqud-gas equlbrum (f. > c densty (lqud densty (gas H m vap for c Clausus-Clapeyon dln P d H ; R ln( P Hm P R ( Metastable phase G α > G β leads to a slow phase change α β example: damond graphte Phase transttons (Ehrenfest classfcaton st µ order: s dscontnuous nd µ µ order: s dscontnuous and s dscontnuous 6

SANDARD HERMODYNAMIC FUNCIONS ν A+ ν A+... ν mam + ν m A Standard enthalpy of formaton + m+ ν A H ν Hf Def.: H f s the enthalpy change for sothermally ( const converson of pure elements n ther reference forms (typcally ther most stable forms to a standard-state substance. Standard state s typcally atm & 5C. e.g. C(graphte + H (deal gas+"o(deal gas" H CO(d. gas H H ( H CO H ( graphte + H ( H deal gas + H ( oxygen d. gas f f f f Hess s law: elements + O combuston product desred molecule + O We need f H for a product that cannot be syntheszed from ts elements. H s a state functon,.e., we can add chemcal equatons and the correspondng f H together. Krchhoff s law (problem we know H ( we need H ( H H C d p z Entropy S ν S,, m ν m,, Gbbs energy G G 7

th law Defnton of the temperature. lm ( P; (P P P LAWS OF HERMODYNAMICS P trp trp (Gas thermometer st law E q+ w; system at rest: U q+ w nd law A nd order perpetuum moble does not exst. It s mpossble to buld a cyclc machne whch converts heat nto work wth an effcency of %. he total entropy s ncreasng n any rreversble process S. 3 rd law Part A: G lm ( P ; lm S K K (Leads to the defnton of a standard entropy. Part B: Unattanablty prncple: he absolute zero temperature Kelvn cannot be reached. GAS MIXURES. P Chemcal potental µ µ + R ln( Equlbrum constant G Rln( Kp wth Kp: K p ( P / P ; ν products reactants P ( P / P j ν e G / R van t Hoff equaton dln( Kp H d R Kp ( ln( K ( H R ( p 8

SOLUIONS Partal molar volume otal volume j (,, ( n j P n j const n j j (obeyed or all extensve propertes of a soluton j Important equatons mxg P mx mxg ; mx S pure Ideal soluton def. µ µ (, P + Rln( x S R n ln( x ; G R n ln( x ; mx mx H ; U mx Raoult s law he rato of the partal vapor pressure of each component of the soluton to the correspondng vapor pressure of the pure lquds s equal to the mole fracton of that component n the lqud mxture. mx vapor pressure of A n the soluton vapor pressure of pure A mole fracton of A P X P lqud pure Ideally dlute soluton X solvent µ µ (, P + Rln( x solute solute solute solvent solvent +R ln( xsolvent µ µ Henry s law P solute Constsolute X lqud solute (Raoult s law s obeyed for the solvent 9

useful but not necessarly to memorze: Gbbs equatons hermal expanson coeffcent α dh ds + dp da Sd Pd dg Sd + dp ( & P const P ( m α κ Isothermal compressblty κ ( & (for an deal gas α P n const κ P ; Joule homson experment (adabatc expanson of a gas, H µ ( p a Rb H ( C p P R S > < for < "coolng" for > "heatng" (nverson temperature, for He well below room temperature Maxwell Relatons ( ( P ( ( S P S S ( ( P S ( ( P S S P P

Mxng entropy S n Rln( x ; mx n: mole fracton he entropy of an deal gas mxture s equal to the sum of the entropes each pure gas would have f t alone occuped the volume of the mxture (at the temperature of the mxture. Follows bascally from Daltons law (P tot P + P + P 3 +... REAL GASES an der Waals equaton ( P an + ( nb nr pm m Z( P, Compresson factor deal R m

deal gas real gas p nr p ZR Z( P, : compresson factor 3 ral equaton P R( + B / + C / + D / +... Maxwell constructon Law of correspondng states: If we defne reduced parameters (e.g. P r P/P c then r equals approxmately f(p r, r for all gases.