Thermodynamica 1. college 5 boek hoofdstuk 3. Bendiks Jan Boersma Wiebren de Jong Thijs J.H. Vlugt Theo Woudstra. Process and Energy Department
|
|
- Julian Stewart Pearson
- 5 years ago
- Views:
Transcription
1 hermodynamia Bendiks Jan Boersma Wiebren de Jong hijs J.H. Vlugt heo Woudstra Proess and Energy Deartment February 9, 20 ollege 5 boek hoofdstuk 3
2 summary leture 4 roerties of matter -V- surfae isobar, isotherm, isohor hase transition oexisting hases working with tables, interolation S S + L S+G G February 9, 20 2 L L+G C G G aor L liquid S solid solid S S L ritial oint liquid L G aor/gas trile oint
3 equation of state of Ideal Gases he intensie roerties {,,} of matter (gas, liquid, solid) are not indeendent of one another. he relation between them is alled equation of state he simlest equation of state is the ideal gas equation of state It was found in stages, by realizing that V = C( n, ) if the Kelin-tem. sale is used, it was seen that V = C n ( ) the final equation of state is V = nr ressure [Pa] V olume [m 3 ] temerature [K ] n amount of substane [mol] uniersal gas onstant J R = mol K mol ontains N A = moleules February 9, 20 3
4 equation of state of Ideal Gases V = nr = R = V n R J = mol K ressure [Pa] V olume [m 3 ] temerature [K ] n amount of substane [mol] mol ontains N A = moleules February 9, 20 4
5 the iso -diagrams for ideal gases he relation between 2 of the 3 roerties {,,} an be isualized in state diagrams isotherm, =onst. isobar, =onst. isohor, =onst. February 9, 20 5
6 releane of the ideal gas model he ideal gas state is a limit for gases of low density Eery real omonent aroahes ideal gas behaior for ressures 0 bar and ρ 0 kg/m 3 Moleular interretation: a gas shows ideal gas behaior, when the moleular interations do not lay a role ( for low densities and/or high temerature) February 9, 20 6
7 dealing with real gases omressibility fator: Z = R ideal gas limit: lim Z = 0 redued ressure and redued temerature: R =, R = February 9, 20 7
8 February 9, 20 8
9 examles of equations of state Ideal gas equation of state Z = = R Virial equation of state (for non-ideal gasses) Z = = + B + C + D + R 2 3 ( ) ( ) ( )... Van der Waals equation of state (for non-ideal gasses) 2 na + 2 ( V nb) = nr V February 9, 20 9
10 the internal energy of an ideal gas exeriment of Joule and homson measurement: = 2 =!, V auum 2, V 2 ideal gas behaior first law: du = δq δw Δ 2U = Δ2Q Δ2W 0 0 Δ 2U = 0 U U = U(, V ) U(, V ) = u (, 2) u (, ) = 0 with 2 we onlude that u is only a funtion of temerature u() for an ideal gas February 9, 20 0
11 isothermal exansion of an ideal gas first law 2 isotherm, =onst. adiabati, ΔQ=0 du = δq δw 0 dv beause u() and =onst. V 2 2 V Δ 2Q =Δ 2W = dv = nr dv = nr ln V V V V ΔQ ΔW nr = ideal gas law V V note: an isothermal roess requires roiding energy in form of heat during exansion, otherwise the temerature would derease 2 February 9, 20
12 olytroi exansion n V = onstant (with n ) 2 V Δ W = dv = V 2 V V n 2 2 February 9, 20 2
13 Math: Differential relations of multiariable funtions onsider a differentiable funtion z(x,y) hink of z as the height oordinate in the Swiss Als, and x and y are the northerly diretion and the westerly diretion, resetiely 6 he total differential is z(x,y) dz = z x y dx + z y ( z/ x) y is the sloe with whih the height hanges with a hange dx in x-diretion. Subsrit y is for: in diretion of onstant y Note, that ( z/ x) y is a funtion of y, as seen in the illustration x dy z x 7 0 y x 3 z x 6 9 y S z y S8 y S5 x S22 February 9, 20 3
14 Seifi heat at onstant olume For an ideal gas: How does u ( ) hange with? Reall the first law: u (, ) = u ( ) du = δ q δw = δq d dq V = onstant +d At onstant olume: du = δ q Definition of heat aaity at onstant olume (here: in units of [J mol - K - ]) u : the amount of heat that needs to be added to inrease the temerature of mol material by Kelin, while keeing the olume onstant. Definition is alid also for nonideal gasses. February 9, 20 4
15 Seifi heat at onstant olume u dq V = onstant +d For an ideal gas, = ( ) Usually: V = a+ b Energy hange at onstant olume uon heating: u Δ = 2 = = 2 2 u u u d d February 9, 20 5
16 Energy hange uon heating at onstant V suose: V = a+ b 2 u 2 2 Δ u = u2 u = d = d = ( a+ b) d = 2 2 b 2 2 a + b = a ( ) ( ) 2 2 February 9, 20 6
17 he Enthaly H U + V h u+ dh = du + d ( ) = du + d + d February 9, 20 7
18 adding heat while keeing the ressure onstant Reall the first law: Enthaly: First law in terms of enthaly: du = δ q δw = δq d H U + V h u+ dq d = onstant +d dh = δ q + d Adding heat at onstant ressure dh = δ q Definition of heat aaity at onstant ressure: (here: in units of [J mol - K - ]) h February 9, 20 8
19 seifi heat at onstant ressure h dq d = onstant +d For an ideal gas, = ( ) Usually: = a+ b Enthaly hange at onstant ressure uon heating: h Δ = 2 = = 2 2 h h h d d February 9, 20 9
20 heating at onstant olume or ressure At onstant olume: du = δ q At onstant ressure: dh = δ q Definition of heat aaity at onstant olume (here: in units of [J mol - K - ]) Definition of heat aaity at onstant ressure (here: in units of [J mol - K - ]) u h : the amount of heat that needs to be added to inrease the temerature of mol material by Kelin, while keeing the olume onstant : the amount of heat that needs to be added to inrease the temerature of mol material by Kelin, while keeing the ressure onstant dq V = onstant +d dq = onstant d +d February 9, 20 20
21 Instrutions Chaters,2,3 hae been treated we disussed and illustrated the ideal gas law read thoroughly in book!!! memorize the definition of enthaly memorize the first law of losed systems in terms of the enthaly understand that u() and that h() for ideal gas understand the heat aaity and what does it tell you? make exerises onerning ideal gasses and non-ideal gasses; (omressibility fator Z, use ±5% deiation as a good aroximation to the ideal gas model). February 9, 20 2
22 relation between and for an ideal gas h= u+ = u+ R ( u R) h + = = = + R P P February 9, 20 22
23 adiabati exansion of an ideal gas ( = onstant) du = δ q d = d Rd d = d d = R d 2 2 ln = R 2 2 after some math... κ d = Rln = onstant (with κ = ) February 9, 20 23
24 Adiabati Exansion V κ = onstant κ = onstant κ = February 9, 20 24
25 Clement & Desormes Exeriment () O druk gebrahte fles is toestand ; na isohore exansie is toestand 2. Na de adiabatish eronderstelde snelle exansie juist oor het sluiten an de kraan is de druk 0 (omgeingsdruk) = 0 + ρgh () 0 = - ρgh (a) a 2 = 0 + ρgh 2 (2) 2 = ( - ρgh ) + ρgh 2 = -(h -h 2 )ρg (2a) Na o druk brengen an de fles olgt adiabatishe exansie: V = V γ γ 2 2 (3) Gas na o druk brengen en na de isohore exansie bereikt uiteindelijk dezelfde V = 2 V 2 (4) V 2 (5) = V2 Met (3) en V 2 =V 0 olgt dan: γ V (6) 0 = V2 γ February 9, γ
26 Clement & Desormes Exeriment (2) 0 ln γ 2 0 Uit (5) en (6) olgt: = (7) γ = (7a) 2 ln Verdere ereenoudiging mogelijk als niet teeel an 0 afwijkt. ( ( ) ) - h-h 2 ρg ρgh = (7) en (a) (8) ( ) h-h 2 ρg ρgh = Als (h -h 2 )ρg/ << dan mag (9), aangezien geldt oor een funtie (+x) α +αx met x<< (olgt uit f(x) = f(0+x) f(0)+x f (0) ), benaderd worden met γ γ (9) ( ) h-h γ ρg ρgh 2 = γ h = h h2 (0) February 9, 20 26
Internal Energy in terms of Properties
Lecture #3 Internal Energy in terms of roerties Internal energy is a state function. A change in the state of the system causes a change in its roerties. So, we exress the change in internal energy in
More informationChapter 3. Volumetric Properties of Pure Fluids
Chapter 3. olumetri roperties of ure Fluids Introdution hermodynami properties (U, H and thus Q, W) are alulated from data data are important for sizing vessels and pipelines Subjets behavior of pure fluids
More informationThe Second Law: The Machinery
The Second Law: The Machinery Chater 5 of Atkins: The Second Law: The Concets Sections 3.7-3.9 8th Ed, 3.3 9th Ed; 3.4 10 Ed.; 3E 11th Ed. Combining First and Second Laws Proerties of the Internal Energy
More informationSOLVED QUESTIONS 1 / 2. in a closed container at equilibrium. What would be the effect of addition of CaCO 3 on the equilibrium concentration of CO 2?
SOLVED QUESTIONS Multile Choie Questions. and are the veloity onstants of forward and bakward reations. The equilibrium onstant k of the reation is (A) (B) (C) (D). Whih of the following reations will
More informationSubject: Modeling of Thermal Rocket Engines; Nozzle flow; Control of mass flow. p c. Thrust Chamber mixing and combustion
16.50 Leture 6 Subjet: Modeling of Thermal Roket Engines; Nozzle flow; Control of mass flow Though onetually simle, a roket engine is in fat hysially a very omlex devie and diffiult to reresent quantitatively
More informationCOMPENDIUM OF EQUATIONS Unified Engineering Thermodynamics
COMPENDIUM OF EQUAIONS Unified Engineering hermodynamics Note: It is with some reseration that I suly this comendium of equations. One of the common itfalls for engineering students is that they sole roblems
More informationPure Component Phase Diagram. Definitions. Definitions (cont.) Class 17 Non-Ideal Gases
Class 17 Non-Ideal Gases Definitions Critial emperature, ressure Vapor Gas Van der Waals EOS Other Equations of State Compressibility Fator riniple of Corresponding States Kay s Rule Water hase Change
More informationTest bank chapter (14)
Test bank hater (14) Choose the most orret answer 1. Whih is the orret equilibrium onstant exression for the following reation? Fe 2 O 3 (s) + 3H 2 (g) 2Fe(s) + 3H 2 O(g) a) K = [Fe 2 O 3 ] [H 2 ] 3 /[Fe]
More informationδq T = nr ln(v B/V A )
hysical Chemistry 007 Homework assignment, solutions roblem 1: An ideal gas undergoes the following reversible, cyclic rocess It first exands isothermally from state A to state B It is then comressed adiabatically
More information( ) ( ) Volumetric Properties of Pure Fluids, part 4. The generic cubic equation of state:
CE304, Spring 2004 Leture 6 Volumetri roperties of ure Fluids, part 4 The generi ubi equation of state: There are many possible equations of state (and many have been proposed) that have the same general
More informationREVERSIBLE NON-FLOW PROCESS CONSTANT VOLUME PROCESS (ISOCHORIC PROCESS) In a constant volume process, he working substance is contained in a rigid
REVERSIBLE NON-FLOW PROCESS CONSTANT VOLUME PROCESS (ISOCHORIC PROCESS) I a ostat olume roess, he workig substae is otaied i a rigid essel, hee the boudaries of the system are immoable, so work aot be
More informationIf y = Bx n (where B = constant)
Pages 87-90 of ext Book 361-18 Lec 14 Mon 24se18 First: One variable: Calculus Review: If y Bx n (where B constant) dy n? Bnx 1 dx How do you KNOW (not memorize) that it is x n-1? What are the units of
More informationTHERMODYNAMICS. Prepared by Sibaprasad Maity Asst. Prof. in Chemistry For any queries contact at
HERMODYNAMIS reared by Sibarasad Maity Asst. rof. in hemistry For any queries contact at 943445393 he word thermo-dynamic, used first by illiam homson (later Lord Kelvin), has Greek origin, and is translated
More informationRelative Maxima and Minima sections 4.3
Relative Maxima and Minima setions 4.3 Definition. By a ritial point of a funtion f we mean a point x 0 in the domain at whih either the derivative is zero or it does not exists. So, geometrially, one
More informationATMOS Lecture 7. The First Law and Its Consequences Pressure-Volume Work Internal Energy Heat Capacity Special Cases of the First Law
TMOS 5130 Lecture 7 The First Law and Its Consequences Pressure-Volume Work Internal Energy Heat Caacity Secial Cases of the First Law Pressure-Volume Work Exanding Volume Pressure δw = f & dx δw = F ds
More informationPHYS1001 PHYSICS 1 REGULAR Module 2 Thermal Physics Chapter 17 First Law of Thermodynamics
PHYS1001 PHYSICS 1 REGULAR Module Thermal Physics Chater 17 First Law of Thermodynamics References: 17.1 to 17.9 Examles: 17.1 to 17.7 Checklist Thermodynamic system collection of objects and fields. If
More informationF = U TS G = H TS. Availability, Irreversibility S K Mondal s Chapter 5. max. actual. univ. Ns =
Availability, Irreversibility S K Mondal s Chater 5 I = W W 0 max ( S) = Δ univ actual 7. Irreversibility rate = I = rate of energy degradation = rate of energy loss (Wlost) = 0 S gen for all rocesses
More informationAt 1atm = 101,325Pa, one mole of gas at 20 0 C = 293K has volume V = 2.40 x10-2 m 3 = 24 litres
Ideal Gases and eat Enges he oeration, and theoretial effiieny, of ombustion driven iston enges (e.g. diesel or etrol fuelled) an be analysed by onsiderg harges to ressure, temerature and volume of the
More information3. High Temperature Gases FPK1 2009/MZ 1/23
3. High Temerature Gases FP 9/MZ /3 Terms and Concets Dissociation Diatomic element gases Bond energy, dissociation energy (enthali) Flood s dissociation diagram Vaorization, eaoration, boiling, sublimation
More informationC a h p a t p er 3 The Importance of State Functions: Internal Energy and Enthalpy
Chapter 3 he Importance of State Functions: Internal Energy and Enthalpy Engel & Reid 1 Outline 3.1 he Mathematical roperties of State Functions 3.2 he Dependence of U on and 3.3 Does he Internal Energy
More informationReview of classical thermodynamics
Review of lassial thermodynamis Fundamental Laws, roperties and roesses () First Law - Energy Balane hermodynami funtions of state Internal energy, heat and work ypes of paths (isobari, isohori, isothermal,
More informationChapter 8 Thermodynamic Relations
Chapter 8 Thermodynami Relations 8.1 Types of Thermodynami roperties The thermodynami state of a system an be haraterized by its properties that an be lassified as measured, fundamental, or deried properties.
More informationPressure Volume Work 2
ressure olume Work Multi-stage Expansion 1 3 w= 4 5 ( ) + 3( 3 ) + 4( 4 3) + ( ) 1 5 5 4 Reversible Expansion Make steps so small that hen d 0, d 0 δ w= d ( ) = + d d int d int w= dw= d path 1 int For
More informationREAL GASES. (B) pv. (D) pv. 3. The compressibility factor of a gas is less than unity at STP. Therefore, molar volume (V m.
SINGLE ORRET ANSWER REAL GASES 1. A real gas is suosed to obey the gas equation ( b) = at STP. If one mole of a gas occuies 5dm 3 volume at STP, then its comressibility factor is (b=.586 L mol 1F) (A)
More informationDefinitions. Pure Component Phase Diagram. Definitions (cont.) Class 16 Non-Ideal Gases
Sore 100% 90% 80% 70% 60% 50% 40% 30% 20% 10% 0% Average = 85% Exam 1 0 5 10 15 20 25 30 35 40 45 Rank Class 16 Non-Ideal Gases Definitions Critial emperature, ressure Vapor Gas Van der Waals EOS Other
More informationThermodynamics part III.
Thermodynamics part III. a.) Fenomenological thermodynamics macroscopic description b.) Molecular thermodynamics microscopic description b1.) kinetical gas theory b2.) statistical thermodynamics Laws of
More informationFirst Law CML 100, IIT Delhi SS. The total energy of the system. Contribution from translation + rotation + vibrations.
Internal Energy he total energy of the system. Contribution from translation + rotation + vibrations. Equipartition theorem for the translation and rotational degrees of freedom. 1/ k B Work Path function,
More informationGeneral Equilibrium. What happens to cause a reaction to come to equilibrium?
General Equilibrium Chemial Equilibrium Most hemial reations that are enountered are reversible. In other words, they go fairly easily in either the forward or reverse diretions. The thing to remember
More informationCHAPTER 16. Basic Concepts. Basic Concepts. The Equilibrium Constant. Reaction Quotient & Equilibrium Constant. Chemical Equilibrium
Proerties of an Equilibrium System CHAPTER 6 Chemial Equilibrium Equilibrium systems are DYNAMIC (in onstant motion) REVERSIBLE an be aroahed from either diretion Pink to blue Co(H O) 6 Cl ---> > Co(H
More informationHEAT, WORK, AND THE FIRST LAW OF THERMODYNAMICS
HET, ORK, ND THE FIRST L OF THERMODYNMIS 8 EXERISES Section 8. The First Law of Thermodynamics 5. INTERPRET e identify the system as the water in the insulated container. The roblem involves calculating
More informationPhase transition. Asaf Pe er Background
Phase transition Asaf Pe er 1 November 18, 2013 1. Background A hase is a region of sace, throughout which all hysical roerties (density, magnetization, etc.) of a material (or thermodynamic system) are
More informationWhat is Physical Chemistry?
Chemistry 313 Dr. Caleb Arrington 10:30 am - 11:20 am M,W,&F Lab: Wednesday 2:00-5:00 Office RMSC 306-A What do we do the first day of every class? syllabus What is Physical Chemistry? Mathematically redictive
More informationdf da df = force on one side of da due to pressure
I. Review of Fundamental Fluid Mechanics and Thermodynamics 1. 1 Some fundamental aerodynamic variables htt://en.wikiedia.org/wiki/hurricane_ivan_(2004) 1) Pressure: the normal force er unit area exerted
More informationdn i where we have used the Gibbs equation for the Gibbs energy and the definition of chemical potential
Chem 467 Sulement to Lectures 33 Phase Equilibrium Chemical Potential Revisited We introduced the chemical otential as the conjugate variable to amount. Briefly reviewing, the total Gibbs energy of a system
More informationProportional-Integral-Derivative PID Controls
Proortional-Integral-Derivative PID Controls Dr M.J. Willis Det. of Chemial and Proess Engineering University of Newastle e-mail: mark.willis@nl.a.uk Written: 7 th November, 998 Udated: 6 th Otober, 999
More informationFlow Characteristics of High-Pressure Hydrogen Gas in the Critical Nozzle
Flow Charateristis of High-Pressure Hydrogen Gas in the Critial Nozzle Shigeru MATSUO *1, Soihiro KOYAMA *2, Junji NAGAO *3 and Toshiaki SETOGUCHI *4 *1 Saga University, Det. of Mehanial Engineering, 1
More informationJournal of Theoretics Vol.5-2 Guest Commentary Relativistic Thermodynamics for the Introductory Physics Course
Journal of heoretis Vol.5- Guest Commentary Relatiisti hermodynamis for the Introdutory Physis Course B.Rothenstein bernhard_rothenstein@yahoo.om I.Zaharie Physis Department, "Politehnia" Uniersity imisoara,
More informationChapter 15: Chemical Equilibrium
Chapter 5: Chemial Equilibrium ahoot!. At eq, the rate of the forward reation is the rate of the reverse reation. equal to, slower than, faster than, the reverse of. Selet the statement that BEST desribes
More informationUniversity of Washington Department of Chemistry Chemistry 452/456 Summer Quarter 2011
Homework Assignment #4: Due at 500 pm Monday 8 July,. University of Washington Department of Chemistry Chemistry 45/456 Summer Quarter 0 ) o a very good approximation, ammonia obeys the Bertholet equation
More informationdv = adx, where a is the active area of the piston. In equilibrium, the external force F is related to pressure P as
Chapter 3 Work, heat and the first law of thermodynamics 3.1 Mechanical work Mechanical work is defined as an energy transfer to the system through the change of an external parameter. Work is the only
More informationSimple Cyclic loading model based on Modified Cam Clay
Simle li loading model based on Modified am la Imlemented in RISP main rogram version 00. and higher B Amir Rahim, The RISP onsortium Ltd Introdution This reort resents a simle soil model whih rovides
More informationLecture 13 Heat Engines
Lecture 3 Heat Engines hermodynamic rocesses and entroy hermodynamic cycles Extracting work from heat - How do we define engine efficiency? - Carnot cycle: the best ossible efficiency Reading for this
More informationSimple Considerations on the Cosmological Redshift
Apeiron, Vol. 5, No. 3, July 8 35 Simple Considerations on the Cosmologial Redshift José Franiso Garía Juliá C/ Dr. Maro Mereniano, 65, 5. 465 Valenia (Spain) E-mail: jose.garia@dival.es Generally, the
More informationWhat is thermodynamics? and what can it do for us?
What is thermodynamics? and what can it do for us? The overall goal of thermodynamics is to describe what happens to a system (anything of interest) when we change the variables that characterized the
More informationSummary of EUV Optics Contamination Modeling Meeting
Summary of EUV Otis Contamination Modeling Meeting IEUVI Otis Contamination/Lifetime TWG San Jose, CA, USA February 28, 2008 Andrea Wüest, SEMATECH Shannon Hill, NIST Lennie Klebanoff, Sandia Nat. Lab.
More informationChemistry 420/523 Chemical Thermodynamics (Spring ) Examination 1
Chemistry 420/523 Chemical hermodynamics (Sring 2001-02) Examination 1 1 Boyle temerature is defined as the temerature at which the comression factor Z m /(R ) of a gas is exactly equal to 1 For a gas
More informationGEF2200 vår 2017 Løsningsforslag sett 1
GEF2200 vår 2017 Løsningsforslag sett 1 A.1.T R is the universal gas constant, with value 8.3143JK 1 mol 1. R is the gas constant for a secic gas, given by R R M (1) where M is the molecular weight of
More informationResearch Article Substance Independence of Efficiency of a Class of Heat Engines Undergoing Two Isothermal Processes
hermodynamis olume 0, Artile ID 6797, 5 pages doi:0.55/0/6797 Researh Artile Substane Independene of Effiieny of a Class of Heat Engines Undergoing wo Isothermal roesses Y. Haseli Department of Mehanial
More informationThermodynamics I Chapter 6 Entropy
hermodynamics I hater 6 Entroy Mohsin Mohd ies Fakulti Keuruteraan Mekanikal, Uniersiti eknologi Malaysia Entroy (Motiation) he referred direction imlied by the nd Law can be better understood and quantified
More informationGeneral Physical Chemistry I
General Physical Cheistry I Lecture 12 Aleksey Kocherzhenko Aril 2, 2015" Last tie " Gibbs free energy" In order to analyze the sontaneity of cheical reactions, we need to calculate the entroy changes
More informationCY1001 BASIC CONCEPTS
CY1001 BASIC CONCES Lecture 1. radeep 22574208 pradeep@iitm.ac.in Atomists and ionists 9/6/2010 1 1. Chemical thermodynamics 2. Statistical thermodynamics 3. Kinetics 4. Surface science Books: 1. G. W.
More informationI affirm that I have never given nor received aid on this examination. I understand that cheating in the exam will result in a grade F for the class.
Chem340 Physical Chemistry for Biochemists Exam Mar 16, 011 Your Name _ I affirm that I have never given nor received aid on this examination. I understand that cheating in the exam will result in a grade
More informationLecture 13. Heat Engines. Thermodynamic processes and entropy Thermodynamic cycles Extracting work from heat
Lecture 3 Heat Engines hermodynamic rocesses and entroy hermodynamic cycles Extracting work from heat - How do we define engine efficiency? - Carnot cycle: the best ossible efficiency Reading for this
More informationarxiv: v1 [math-ph] 21 Dec 2007
Dynamic Phase ransitions in PV Systems ian Ma Deartment of Mathematics, Sichuan Uniersity, Chengdu, P. R. China Shouhong Wang Deartment of Mathematics, Indiana Uniersity, Bloomington, IN 4745 (Dated: February
More informationInfluence of Real-Fluid Properties in Modeling Decompression Wave Interacting with Ductile Fracture Propagation
Oil & Gas Siene and ehnology Rev. IFP, Vol. 6 (5), No. 4,. 7-79 Coyright 5, Institut français du étrole Influene of Real-Fluid Proerties in Modeling Deomression Wave Interating with Dutile Frature Proagation
More informationThermodynamic Properties are Measurements p,t,v, u,h,s - measure directly -measure by change
Thermodynamic Proerties are Measurements,T,, u,h,s - measure directly -measure by change s Tables T T Proerty Data Cure its Tables Correlation's, Boyles Law Tables c@tc limited hand calculations Equations
More informationMass Transfer (Stoffaustausch) Fall 2012
Mass Transfer (Stoffaustaush) Fall Examination 9. Januar Name: Legi-Nr.: Edition Diffusion by E. L. Cussler: none nd rd Test Duration: minutes The following materials are not permitted at your table and
More informationwhether a process will be spontaneous, it is necessary to know the entropy change in both the
93 Lecture 16 he entroy is a lovely function because it is all we need to know in order to redict whether a rocess will be sontaneous. However, it is often inconvenient to use, because to redict whether
More informationFoundations of thermodynamics Fundamental thermodynamical concepts
Foundations of thermodynamics Fundamental thermodynamical concets System is the macrohysical entity under consideration Surrounding is the wld outside of the system Oen system can exchange matter heat
More informationThe Hanging Chain. John McCuan. January 19, 2006
The Hanging Chain John MCuan January 19, 2006 1 Introdution We onsider a hain of length L attahed to two points (a, u a and (b, u b in the plane. It is assumed that the hain hangs in the plane under a
More informationFundamental Theorem of Calculus
Chater 6 Fundamental Theorem of Calulus 6. Definition (Nie funtions.) I will say that a real valued funtion f defined on an interval [a, b] is a nie funtion on [a, b], if f is ontinuous on [a, b] and integrable
More informationThe Effect of Gauge Measurement Capability and Dependency Measure of Process Variables on the MC p
Journal of Industrial and Systems Engineering Vol. 4, No., 59-76 Sring The Effet of Gauge easurement Caability and Deendeny easure of Proess Variables on the C Daood Shishebori, Ali Zeinal Hamadani Deartment
More informationLecture Thermodynamics 9. Entropy form of the 1 st law. Let us start with the differential form of the 1 st law: du = d Q + d W
Lecture hermodnamics 9 Entro form of the st law Let us start with the differential form of the st law: du = d Q + d W Consider a hdrostatic sstem. o know the required d Q and d W between two nearb states,
More informationPhysics 41 Chapter 22 HW
Pysis 41 apter 22 H 1. eat ine performs 200 J of work in ea yle and as an effiieny of 30.0%. For ea yle, ow mu energy is (a) taken in and (b) expelled as eat? = = 200 J (1) e = 1 0.300 = = (2) From (2),
More informationAE301 Aerodynamics I UNIT A: Fundamental Concepts
AE301 Aerodynamics I UNIT A: Fundamental Concets ROAD MAP... A-1: Engineering Fundamentals Reiew A-: Standard Atmoshere A-3: Goerning Equations of Aerodynamics A-4: Airseed Measurements A-5: Aerodynamic
More informationCHAPTER 3 LECTURE NOTES 3.1. The Carnot Cycle Consider the following reversible cyclic process involving one mole of an ideal gas:
CHATER 3 LECTURE NOTES 3.1. The Carnot Cycle Consider the following reversible cyclic process involving one mole of an ideal gas: Fig. 3. (a) Isothermal expansion from ( 1, 1,T h ) to (,,T h ), (b) Adiabatic
More informationCY1001 BASIC CONCEPTS
CY1001 BASIC CONCES Lecture 1. radeep 22574208 pradeep@iitm.ac.in Atomists and ionists 9/19/2013 1 1. Chemical thermodynamics 2. Statistical thermodynamics 3. Kinetics 4. Surface science Books: 1. Kuhn
More informationF = F x x + F y. y + F z
ECTION 6: etor Calulus MATH20411 You met vetors in the first year. etor alulus is essentially alulus on vetors. We will need to differentiate vetors and perform integrals involving vetors. In partiular,
More informationMathematics II. Tutorial 5 Basic mathematical modelling. Groups: B03 & B08. Ngo Quoc Anh Department of Mathematics National University of Singapore
Mathematis II Tutorial 5 Basi mathematial modelling Groups: B03 & B08 February 29, 2012 Mathematis II Ngo Quo Anh Ngo Quo Anh Department of Mathematis National University of Singapore 1/13 : The ost of
More informationPY2005: Thermodynamics
ome Multivariate Calculus Y2005: hermodynamics Notes by Chris Blair hese notes cover the enior Freshman course given by Dr. Graham Cross in Michaelmas erm 2007, except for lecture 12 on phase changes.
More information1.72, Groundwater Hydrology Prof. Charles Harvey Lecture Packet #11: Solute Transport in Groundwater
1.72, Groundwater Hydrology Prof. harles Harvey Leture Paket #11: Solute Transport in Groundwater Importane of Solute Transport in Groundwater Geologi questions: ion migration, ore deposition. Environmental
More informationExam 2, Chemistry 481, 4 November 2016
1 Exam, Chemistry 481, 4 November 016 Show all work for full credit Useful constants: h = 6.66 10 34 J s; c (speed of light) =.998 10 8 m s 1 k B = 1.3807 10 3 J K 1 ; R (molar gas constant) = 8.314 J
More informationTHE ZEROTH AND FISRT LAW OF THERMODYNAMICS. Saeda Al-Mhyawi secend Tearm 1435H
H ZROH AND FISR LAW OF HRMODYNAMIS Saeda Al-Mhyawi secend earm 435H HAR II H ZROH AND FISR LAW OF HRMODYNAMIS Lecture () Outline Introduction he Zeroth Law of hermodynamics he First Law of hermodynamics
More informationChemistry 163B Absolute Entropies and Entropy of Mixing
Chemistry 163B Absolute Entropies and Entropy of Mixing 1 APPENDIX A: H f, G f, BUT S (no Δ, no sub f ) Hº f Gº f Sº 2 Third Law of Thermodynamics The entropy of any perfect crystalline substance approaches
More informationChapter 20: Exercises: 3, 7, 11, 22, 28, 34 EOC: 40, 43, 46, 58
Chater 0: Exercises:, 7,,, 8, 4 EOC: 40, 4, 46, 8 E: A gasoline engine takes in.80 0 4 and delivers 800 of work er cycle. The heat is obtained by burning gasoline with a heat of combustion of 4.60 0 4.
More informationWhere as discussed previously we interpret solutions to this partial differential equation in the weak sense: b
Consider the pure initial value problem for a homogeneous system of onservation laws with no soure terms in one spae dimension: Where as disussed previously we interpret solutions to this partial differential
More informationMEASURE AND INTEGRATION: LECTURE 15. f p X. < }. Observe that f p
L saes. Let 0 < < and let f : funtion. We define the L norm to be ( ) / f = f dµ, and the sae L to be C be a measurable L (µ) = {f : C f is measurable and f < }. Observe that f = 0 if and only if f = 0
More information2.2 BUDGET-CONSTRAINED CHOICE WITH TWO COMMODITIES
Essential Miroeonomis -- 22 BUDGET-CONSTRAINED CHOICE WITH TWO COMMODITIES Continuity of demand 2 Inome effets 6 Quasi-linear, Cobb-Douglas and CES referenes 9 Eenditure funtion 4 Substitution effets and
More informationThe Procedure of Finding the Stress-Energy. Tensor and Equations of Vector Field of Any Form
Advaned Studies in Theoretial Phsis Vol. 8, 14, no. 18, 771-779 HIKARI Ltd, www.m-hikari.om htt://d.doi.org/1.1988/ast.14.4711 The Proedure of Finding the Stress-Energ Tensor and Equations of Vetor Field
More informationLecture 27: Entropy and Information Prof. WAN, Xin
General Pysis I Leture 27: Entropy and Information Prof. WAN, Xin xinwan@zju.edu.n ttp://zimp.zju.edu.n/~xinwan/ 1st & 2nd Laws of ermodynamis e 1st law speifies tat we annot get more energy out of a yli
More informationATM The thermal wind Fall, 2016 Fovell
ATM 316 - The thermal wind Fall, 2016 Fovell Reca and isobaric coordinates We have seen that for the synotic time and sace scales, the three leading terms in the horizontal equations of motion are du dt
More informationSUBSONIC GAS-PARTICLE TWO-PHASE FLOW IN PIPES
Proeedings of the 006 WSEAS/IASME International Conferene on Fluid Mehanis, Miami, Florida, USA, January 8-0, 006 (95-00) SUBSONIC GAS-PARTICLE TWO-PHASE FLOW IN PIPES Mofreh H. Hamed Mehanial Power Engineering
More information/ p) TA,. Returning to the
Toic2610 Proerties; Equilibrium and Frozen A given closed system having Gibbs energy G at temerature T, ressure, molecular comosition (organisation ) and affinity for sontaneous change A is described by
More informationTheory. Coupled Rooms
Theory of Coupled Rooms For: nternal only Report No.: R/50/TCR Prepared by:. N. taey B.., MO Otober 00 .00 Objet.. The objet of this doument is present the theory alulations to estimate the reverberant
More informationAnelastic MHD Equations : Theory
Anelasti MHD Equations : Theory Abhishek Kr. Srivastava Armagh Observatory Northern Ireland Different zones of the Sun Comlex magneti field is the key behind all tyes of solar ativity and formation of
More informationChapter 14. The Concept of Equilibrium and the Equilibrium Constant. We have for the most part depicted reactions as going one way.
Chapter 14 The Conept of Equilibrium and the Equilibrium Constant In hapter 1 we dealt with Physial Equilibrium Physial Changes HO 2 (l) HO 2 (g) In hapter 14 we will learn about Chemial Equilibrium. We
More informationI have not proofread these notes; so please watch out for typos, anything misleading or just plain wrong.
hermodynamics I have not roofread these notes; so lease watch out for tyos, anything misleading or just lain wrong. Please read ages 227 246 in Chater 8 of Kittel and Kroemer and ay attention to the first
More informationNon-Equilibrium Thermodynamics for Engineers
Non-Equilibrium Thermodynamics for Engineers How do we find the otimal rocess unit? Signe Kjelstru, Chair of Engineering Thermodynamics Deartment of Process and Energy TU Delft ecture no. 7 Why is the
More informationChapter-6: Entropy. 1 Clausius Inequality. 2 Entropy - A Property
hater-6: Entroy When the first law of thermodynamics was stated, the existence of roerty, the internal energy, was found. imilarly, econd law also leads to definition of another roerty, known as entroy.
More informationTHERMODYNAMICS CONTENTS
1. Introduction HERMODYNAMICS CONENS. Maxwell s thermodynamic equations.1 Derivation of Maxwell s equations 3. Function and derivative 3.1 Differentiation 4. Cyclic Rule artial Differentiation 5. State
More informationIII. SURFACE PROPERTIES III.A. SURFACE TENSION SURFACE PROPERTIES
III. SURFACE PROPERTIES III.A. SURFACE TENSION GOAL: To investigate the influene of the solution onentration and/or the kind of the solute on the surfae tension INTRODUCTION Liquids tend to adopt shapes
More informationChemistry. Lecture 10 Maxwell Relations. NC State University
Chemistry Lecture 10 Maxwell Relations NC State University Thermodynamic state functions expressed in differential form We have seen that the internal energy is conserved and depends on mechanical (dw)
More informationU = 4.18 J if we heat 1.0 g of water through 1 C. U = 4.18 J if we cool 1.0 g of water through 1 C.
CHAPER LECURE NOES he First Law of hermodynamics: he simplest statement of the First Law is as follows: U = q + w. Here U is the internal energy of the system, q is the heat and w is the work. CONVENIONS
More informationSERBIATRIB th International Conference on Tribology. Kragujevac, Serbia, May 2011
erbian ribology oiety ERBIARIB 11 12 th International Conferene on ribology ragujea, erbia, 11 13 May 2011 Faulty of Mehanial Engineering in ragujea ANALYI OF CHANGE OF BUL MODULU OF MINERAL OIL EFFEC
More informationTHE FIRST LAW OF THERMODYNAMICS
THE FIRST LA OF THERMODYNAMIS 9 9 (a) IDENTIFY and SET UP: The ressure is constant and the volume increases (b) = d Figure 9 Since is constant, = d = ( ) The -diagram is sketched in Figure 9 The roblem
More informationdr v dt ) ( k R d 2 rv dt 2 f el rv ) + ( 1 ex e z S μ ( K) + C L ( K S( K)) K μ + (C 66 M v K 2 + C 44 K z 2 ) S μ ( K) + f μ ( K) ( K) ( K f R S Rμ
he Oen Suerondutors Journal 00-8 Oen Aess heory of hermally Atiated ortex undles Flow Oer the Diretional- Deendent Potential arriers in ye-ii Suerondutors Wei Yeu hen * Deartment of Physis amkang Uniersity
More informationHOMOGENEOUS CLOSED SYSTEM
CHAE II A closed system is one that does not exchange matter with its surroundings, although it may exchange energy. W n in = 0 HOMOGENEOUS CLOSED SYSEM System n out = 0 Q dn i = 0 (2.1) i = 1, 2, 3,...
More informationChemical Engineering Thermodynamics II ( ) 02 - The Molar Gibbs Free Energy & Fugacity of a Pure Component
Chemial Engineering Thermodynamis II (090533) 0 - The Molar Gibbs Free Energy & Fugaity of a ure Component Dr. Ali Khalaf Al-matar Chemial Engineering Department University of Jordan banihaniali@yahoo.om
More informationIntroduction. Statistical physics: microscopic foundation of thermodynamics degrees of freedom 2 3 state variables!
Introduction Thermodynamics: phenomenological description of equilibrium bulk properties of matter in terms of only a few state variables and thermodynamical laws. Statistical physics: microscopic foundation
More information