Chapter 12 Lyes KADEM [Thermodynamics II] 2007

Similar documents
Chapter 13. Gas Mixtures. Study Guide in PowerPoint. Thermodynamics: An Engineering Approach, 5th edition by Yunus A. Çengel and Michael A.

Chapter One Mixture of Ideal Gases

Fermi-Dirac statistics

THERMODYNAMICS of COMBUSTION

XII.3 The EM (Expectation-Maximization) Algorithm

Study of the possibility of eliminating the Gibbs paradox within the framework of classical thermodynamics *

PHYS 1443 Section 002 Lecture #20

Our focus will be on linear systems. A system is linear if it obeys the principle of superposition and homogenity, i.e.

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

Chemical Engineering 160/260 Polymer Science and Engineering. Lecture 10 - Phase Equilibria and Polymer Blends February 7, 2001

Applied Mathematics Letters

COS 511: Theoretical Machine Learning

System in Weibull Distribution

University of Washington Department of Chemistry Chemistry 452/456 Summer Quarter 2013

Excess Error, Approximation Error, and Estimation Error

Physics 3A: Linear Momentum. Physics 3A: Linear Momentum. Physics 3A: Linear Momentum. Physics 3A: Linear Momentum

Solutions for Homework #9

Solution Thermodynamics

Open Systems: Chemical Potential and Partial Molar Quantities Chemical Potential

,..., k N. , k 2. ,..., k i. The derivative with respect to temperature T is calculated by using the chain rule: & ( (5) dj j dt = "J j. k i.

Multipoint Analysis for Sibling Pairs. Biostatistics 666 Lecture 18

On Pfaff s solution of the Pfaff problem

Final Exam Solutions, 1998

Designing Fuzzy Time Series Model Using Generalized Wang s Method and Its application to Forecasting Interest Rate of Bank Indonesia Certificate

AN ANALYSIS OF A FRACTAL KINETICS CURVE OF SAVAGEAU

1 Review From Last Time

Computational and Statistical Learning theory Assignment 4

Obtaining U and G based on A above arrow line: )

1.3 Hence, calculate a formula for the force required to break the bond (i.e. the maximum value of F)

Description of the Force Method Procedure. Indeterminate Analysis Force Method 1. Force Method con t. Force Method con t

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

Scattering by a perfectly conducting infinite cylinder

Department of Mechanical Engineering ME 322 Mechanical Engineering Thermodynamics. Ideal Gas Mixtures II. Lecture 32

Revision: December 13, E Main Suite D Pullman, WA (509) Voice and Fax

Linear Multiple Regression Model of High Performance Liquid Chromatography

Preference and Demand Examples

CHAPTER 10 ROTATIONAL MOTION

Physics 123. Exam #1. October 11, 2006

Solubilities and Thermodynamic Properties of SO 2 in Ionic

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

VERIFICATION OF FE MODELS FOR MODEL UPDATING

Lecture. Polymer Thermodynamics 0331 L Chemical Potential

Page 1. SPH4U: Lecture 7. New Topic: Friction. Today s Agenda. Surface Friction... Surface Friction...

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

ITERATIVE ESTIMATION PROCEDURE FOR GEOSTATISTICAL REGRESSION AND GEOSTATISTICAL KRIGING

What is LP? LP is an optimization technique that allocates limited resources among competing activities in the best possible manner.

Least Squares Fitting of Data

GAUTENG DEPARTMENT OF EDUCATION SENIOR SECONDARY INTERVENTION PROGRAMME. PHYSICAL SCIENCE Grade 11 SESSION 11 (LEARNER NOTES)

Denote the function derivatives f(x) in given points. x a b. Using relationships (1.2), polynomials (1.1) are written in the form

Gadjah Mada University, Indonesia. Yogyakarta State University, Indonesia Karangmalang Yogyakarta 55281

total If no external forces act, the total linear momentum of the system is conserved. This occurs in collisions and explosions.

Quantum Particle Motion in Physical Space

Elastic Collisions. Definition: two point masses on which no external forces act collide without losing any energy.

Lecture-24. Enzyme kinetics and Enzyme inhibition-ii

Finite Vector Space Representations Ross Bannister Data Assimilation Research Centre, Reading, UK Last updated: 2nd August 2003

Special Relativity and Riemannian Geometry. Department of Mathematical Sciences

Slobodan Lakić. Communicated by R. Van Keer

The Parity of the Number of Irreducible Factors for Some Pentanomials

Department of Mechanical Engineering ME 322 Mechanical Engineering Thermodynamics. Ideal Gas Mixtures. Lecture 31

Important Instructions to the Examiners:

ELASTIC WAVE PROPAGATION IN A CONTINUOUS MEDIUM

Thermodynamics General

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

FUZZY MODEL FOR FORECASTING INTEREST RATE OF BANK INDONESIA CERTIFICATE

All Excuses must be taken to 233 Loomis before 4:15, Monday, April 30.

The calculation of ternary vapor-liquid system equilibrium by using P-R equation of state

ON THE NUMBER OF PRIMITIVE PYTHAGOREAN QUINTUPLES

Topic 4. Orthogonal contrasts [ST&D p. 183]

Handling Overload (G. Buttazzo, Hard Real-Time Systems, Ch. 9) Causes for Overload

Chapter 25: Machining Centers, Machine Tool Structures and Machining Economics

CHEMICAL REACTIONS AND DIFFUSION

Irreversible Work of Separation and Heat-Driven Separation

G4023 Mid-Term Exam #1 Solutions

An Improved Group Contribution Volume Translated Peng-Robinson Equation of State

Multiplicative Functions and Möbius Inversion Formula

Economics 101. Lecture 4 - Equilibrium and Efficiency

5/24/2007 Collisions ( F.Robilliard) 1

Neryškioji dichotominių testo klausimų ir socialinių rodiklių diferencijavimo savybių klasifikacija

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

Chemical Engineering Department University of Washington

ACTM State Calculus Competition Saturday April 30, 2011

Chapter 10 Sinusoidal Steady-State Power Calculations

Introducing Entropy Distributions

Linear Momentum. Center of Mass.

Be true to your work, your word, and your friend.

Least Squares Fitting of Data

Supplementary Notes for Chapter 9 Mixture Thermodynamics

Finite Fields and Their Applications

University of Washington Department of Chemistry Chemistry 453 Winter Quarter 2015

Module 3: The Whole-Process Perspective for Thermochemical Hydrogen

Chapter 1. Theory of Gravitation

Structure and Drive Paul A. Jensen Copyright July 20, 2003

AP Physics Thermodynamics Wrap-up

Finite Element Modelling of truss/cable structures

EXAMPLES of THEORETICAL PROBLEMS in the COURSE MMV031 HEAT TRANSFER, version 2017

1 The properties of gases The perfect gas

Xiangwen Li. March 8th and March 13th, 2001

APPLICATION OF SPACE TETHERED SYSTEMS FOR SPACE DEBRIS REMOVAL

04 - Treaps. Dr. Alexander Souza

A novel mathematical model of formulation design of emulsion explosive

Transcription:

Chapter 2 Lyes KDEM [Therodynacs II] 2007 Gas Mxtures In ths chapter we wll develop ethods for deternng therodynac propertes of a xture n order to apply the frst law to systes nvolvng xtures. Ths wll be an essental step to understand checal reactons and cobuston. The objectve of ths part s, therefore, to answer to ths sple queston: If I gve you the propertes of a coponent and the propertes of a coponent, what wll be the propertes of the xture +. The frst soluton to answer to ths queston wll be to defne a table of therodynac propertes for each xture. ut obvously, ths s not achevable snce the nuber of cobnatons s endless. It wll be uch easer to deterne the propertes of the xture usng the propertes of each coponent. For that, we need to now the coposton of the xture, as well as, the propertes of the ndvdual coponents. Let us start by soe defntons: The total ass of the xture:... + + + C The ole nuber of a xture: + + C +... The ole fracton ole nuber of a coponent ole nuber of the xture Mole fracton y ote that, therefore: y y The ass fracton The ass of a coponent The ass of the xture ote that, Mass fracton f f therefore The olecular weght of the xture can be obtaned as: f M M ym Gas Mxtures 53

Chapter 2 Lyes KDEM [Therodynacs II] 2007 nd the xture gas constant wll be: R R U where R U s the unversal gas constant (8.34 J/ol K). M When perforng an analyss on a xture t s portant to state f the analyss s based on the ass [gravetrc analyss] or on the ole nubers or volue [voluetrc analyss] Exaple Molar analyss of ar ndcates that t s coposed prarly of ntrogen (78%) and oxygen (22%). Deterne: - The ole fractons. - The gravetrc analyss. - Its olecular weght. - Its gas constant. -v-t behavor of gas xtures or deal gas-low for xtures: Two odels are used to obtan the -v-t relaton for a xture of deal gases: The agat s odel: In ths odel each coponent s consdered, as t exsts separately at the sae pressure and teperature of the xture. The total volue s the su of the volue of each coponent. agat s odel sae T and For the xture (+) V V For coponent V For coponent ut + V / V / Therefore for the agat s odel: V The general for s: V V V and V are the partal volues. ( ) T, V / + V +V The Dalton s odel: n ths odel each coponent occupes the sae volue and has the sae teperature of the xture. The total pressure s the su of the coponent pressures (partal pressures). Dalton s odel sae T and V V For the xture (+) V For coponent V For coponent Gas Mxtures 54

Chapter 2 Lyes KDEM [Therodynacs II] 2007 ut V + V V Therefore for the Dalton s odel: + The general for s: ( T, V ) and are the partal pressures. We can show that, y and y Exaple rgd tan contans 2 g of 2 and 4 g of CO 2 at a teperature of 25 C and 2 Ma. Deterne: - The partal pressures of the two gases. - The gas constant of the xture. ropertes of xtures of deal gases The extensve propertes of a xture, such as H, U and S can be found by sply addng the contrbuton of each coponent, for exaple for enthalpy: H H H... H + + In ter of specfc enthalpy h: H h h Therefore, h h f Ths can be also expressed on a olar bass So n general for: H h h h y h Gas Mxtures 55

Chapter 2 Lyes KDEM [Therodynacs II] 2007 u h f f ( Cp) ( C ) s v u h s f f f C C p v Exaple xture s coposed of 2 ol CO 2 and 4 ol 2. It s copressed sentropcally n a cylnder fro 00 a and 20 C to 2 Ma. ssung constant specfc heats. Calculate: - The fnal teperature. - The wor requred. - The change n entropy. John Dalton Englsh eteorologst who swtched to chestry when he saw the applcatons for chestry of hs deas about the atosphere. He proposed the toc Theory n 803 whch stated that () all atter was coposed of sall ndvsble partcles tered atos, (2) atos of a gven eleent possess unque characterstcs and weght, and (3) three types of atos exst: sple (eleents), copound (sple olecules), and coplex (coplex olecules). Dalton's theory was presented n ew Syste of Checal hlosophy (808-827). Ths wor dentfed checal eleents as a specfc type of ato, therefore rejectng ewton's theory of checal affntes. Instead, Dalton nferred proportons of eleents n copounds by tang ratos of the weghts of reactants, settng the atoc weght of hydrogen to be dentcally one. Followng Rchter, he proposed that checal eleents cobne n ntegral ratos. Despte the portance of the wor as the frst vew of atos as physcally real enttes and ntroducton of a syste of checal sybols, ew Syste of Checal hlosophy devoted alost as uch space to the calorc theory as to atos. Fgure.0.. John Dalton. Gas Mxtures 56

Chapter 2 Lyes KDEM [Therodynacs II] 2007 Mxture of real Gases Dalton s law and agat s law can also be appled to real gases (non-deal gases) wth a reasonable accuracy. However, the devaton fro the deal gas law ust be taen nto account by: - Usng ore approprate (and coplex ) relatons for a real gas. 2- Usng the copressblty factor (Z) V ZR T For a xture, Z can be coputed as: Reeber that: U Z yz ole nuber of a coponent y ole nuber of the xture The proble wth usng the copressblty factor s that ths approach consders only the nfluence of le olecules on each other, neglectng the effect of the olecules of the coponent on the olecules of the coponent. In practce, the predcted values usng the approach of the copressblty factor, aybe far fro the experentally deterned values. The soluton? Kay s rule nother ore accurate approach to predct the behavor of a real gas s to use the Kay s rule (For W.. Kay 963). For that, pseudo crtcal pressure and pseudo crtcal teperature have to be coputed. Then, the copressblty factor wll be deterned usng the elson-obert generalzed copressblty chart (chart page 868 [Cengel s boo]). seudo pressure: ' cr, ycr, ' seudo teperature: T y T cr,i s the crtcal pressure for each coponent of the xture. cr, cr, cr,i s the crtcal teperature for each coponent of the xture. Fro (table., page 824 [Cengel s boo]) The results obtaned by usng Kay s rule s accurate to wthn 0% over a wde range of teperatures and pressures. Ths accuracy s acceptable for ost engneerng purposes. Exaple n nsulated rgd tan of volue 0.2 3 contans 0.25 ol of O 2 and 0.4 ol of CO 2 at 300 K. Deterne the pressure of the xture usng: a/ the deal-gas equaton of state. b/ copressblty factors based on Dalton s odel. c/ copressblty factors based on agat s odel d/ Kay s rule. Gas Mxtures 57

Chapter 2 Lyes KDEM [Therodynacs II] 2007 ropertes of real gas xtures The study of the propertes of real gas xtures aybe very coplex and counterntutve. To llustrate ths, let us see the followng exaple (Cengel boo page 645). Real gas 25 C 0.4 3 00 a Real gas 25 C 0.6 3 00 a Real gas + 25 C 3 02 a Fgure.0.2. Mxture of real gases. Whle the pressure of both coponents s 00 a, the pressure of the xture s 02 a. Ths ay be explaned by the nfluence of the olecules of dfferent gases on each other. Even though, several approaches exst to deterne the propertes of real gas xtures, the easest way s to use the Kay s rule ( once agan). Exaple r s a xture of 2, O 2 and a sall aounts of other gases, and t can be approxated as 79 percent 2 and 2 O 2 on a ole bass. Durng a steady flow process, ar s cooled fro 220 to 60 K at a constant pressure of 0 Ma. Deterne the heat transfer durng ths process per ol of ar, usng the Kay s rule. Gas Mxtures 58