3) Thermodynamic equation to characterize interfaces
|
|
- Hortense Lane
- 6 years ago
- Views:
Transcription
1 3) Thermodynamc equaton to characterze nterfaces 3.1) Gbbs Model Realty: rapd contnuous change of chemcal and thermodynamc propertes Replaced by model (constant propertes up to the surface) uv bulk uv bulk thn nterface U σ Uσ = U uv u V n = cv n = cv component Amount of component n the surface n = n cv cv σ σ =Γ n A μ = μ = μ σ n : total number of moles of component Surface excess of component : Γ > 0: excess, adsorpton Γ < 0: depleton
2 3.) Gbbs adsorpton equaton Relaton between surface excess Γ, surface tenson γ and chem. Potental μ nternal energy (U(S,V,n)): bulk: surface: U = ST pv + μ n du = TdS pdv + μ dn σ σ σ = + γ + μ σ SdT+ Adγ + ndμ = 0 σ du TdS da dn n γ = μ = Γ μ σ d d d A d γ = ( Γ dμ +Γ d μ ) 1 1 T=const, dt=0 Relaton between change n surface tenson and change n chem. potental va surface excess Relaton between surface excess Γ and bulk concentraton? Smplfcaton by the rght locaton of the surface.
3 Gbbs adsorpton lqud surface, surface and subphase are n equlbrum:exchange possble Problem: Locaton of a surface at a lqud/vapor nterface? Lqud surface: nterfacal regon a few molecular damters thck (nm) Sold surface: nterfacal regon on a Å scale
4 Gbbs adsorpton equaton Δ c(z) = c(z) c Δ c(z) = c(z) c lq vap Γ= Δc(z)dz Γ= (c(z) c )dz + (c(z) c )dz vap lq Γ =Γ = + 0 (c(z) c )dz (c(z) c )dz z 0 1 H O H O,v H O,lq Γ =Γ = + 0 (c(z) c )dz (c(z) c )dz 0 SDS z SDS,v SDS,lq z z = 0 dγ dμ = Γ SDS 1 dγ Γ surfactan t = RT d ln c surfactan t
5 Γ = surfactan t 1 dγ RT d ln c surfactan t γ / mn/m saturaton below cmc Slope => adsorbed amount Value => change n free energy for brngng molecules at the nterface The longer the hydrocarbon chan, the lower the CMC e.g. SDS n water: CMC=8*10-3 mol/l, γ=40 mj/m, Γ=1Molkül / 50Å NaCl n water: 1mol/l, γ=74 mj/m, depleton
6 3.3) Monolayers of soluble amphphles: Gbbs sotherm ( ) RT ln ( X ) μ = μ + RT ln X = μ = μ + μ w w w s s s μ X RT ln w s w = X s SDS DS - + Na + dγ =Γ dμ => Electroneutralty => μ = μ + RT ln c + RT ln c DS Na dγ = RT Γ (dlnc + dlnc ) dγ dlnc DS SDS X w,x s : molar ratos DS = RTΓ + + dγ Excess of electrolyte: = RTΓ 0.1 M NaCl: a 0 (SDS)=38Å dlnc Na a 0 (SDS)=5Å Equlbrum between soluton and surface: below cmc No change of soluton wthout changng the surface
7 surafec tenson / mn/m conc (C 1 TAC) / mol/l wthout salt 0. NaCl Γ = surfac tan t Γ = surfac tan t 1 dγ RT d ln c surfactan t 1 dγ RT d ln c surfac tan t Wth salt, non-onc surfactant Wthout salt
8 3.4) Langmur nterfaces No change n surface tenson accessble Cannot be characterzed by Gbbs sotherm Langmur sotherm: D lattce model: N ndependent bndng ste, N adsorbed molecules, N-N stes occuped by solvent molecules, X =N /N (Index : solute, 1: solvent) Interacton between molecules gnored, monolayer { μ μ } { } G = G + Nμ + RT NlnX + (N N)ln(1 X) 0 s s s G X N 1 X = μ(s) = μ(s) + RT ln μ (b) = μ (b) + RTln c (b) Θ= X = adsorpton Kc (b) Kc (b) + 1 RT ln K = (b) (s) entropy bulk surface μ (b) = μ (s) Equlbrum: c (b)k>>1 => Θ 1 c (b)k<<1 => Θ c (b)
9 3.5) Monolayers of nsoluble amphphles Preparaton: dssolve nsoluble amphphles n a volatle organc solvent and depost drops of soluton onto the ar/water nterface S>0 => spreadng, evaporaton of solvent => monolayer of amphphles Pressure s needed to prevent flm from spreadng: Π = 0 s γ γ
10 3.5.1) Monolayers of nsoluble amphphles: Π(a 0 ) sotherms Collapse G: gas phase L1: lqud expanded phase (e.g. saturated unbranched carbon chans: a Å ) L: lqud condensed phase (stronger molecular nteractons, lower compressblty S: sold (e.g. alcohols, esters: a 0 19 Å ) G->L1: typcal gas lqud transton lke n 3D L1->L: transton not fnally explaned.
11 Gas phase D 3D Ideal gas equaton Devaton from deal gas: Π sa= nrt Π sa0 = kt Πsa0 Z = kt pv= nrt pv Z = nrt Compressblty factor 1 C 4 C 5 3 C 6 4 C 8 5 C 10 6 C 1 Z < 1: attracton Z > 1: repulson
12 Vsualzaton of phase transton 3.5.) Fluorescence mcroscopy Doman sze determned by balance between electrostatc repulson and lne tenson Amphphle: DMPA (dmyrstoylphosphatdc acd) Dye: DP-NBD-PE (L-α-dpalmtoyl.ntrobenzoxadazol-phosphatdylethanolamne) 1%
13 3.6) Langmur-Blodget flms Mono- or multlayers Hghly ordered flms Problem: long-term stablty
...Thermodynamics. If Clausius Clapeyron fails. l T (v 2 v 1 ) = 0/0 Second order phase transition ( S, v = 0)
If Clausus Clapeyron fals ( ) dp dt pb =...Thermodynamcs l T (v 2 v 1 ) = 0/0 Second order phase transton ( S, v = 0) ( ) dp = c P,1 c P,2 dt Tv(β 1 β 2 ) Two phases ntermngled Ferromagnet (Excess spn-up
More informationLecture. Polymer Thermodynamics 0331 L Chemical Potential
Prof. Dr. rer. nat. habl. S. Enders Faculty III for Process Scence Insttute of Chemcal Engneerng Department of Thermodynamcs Lecture Polymer Thermodynamcs 033 L 337 3. Chemcal Potental Polymer Thermodynamcs
More informationAppendix II Summary of Important Equations
W. M. Whte Geochemstry Equatons of State: Ideal GasLaw: Coeffcent of Thermal Expanson: Compressblty: Van der Waals Equaton: The Laws of Thermdynamcs: Frst Law: Appendx II Summary of Important Equatons
More informationChapter 18, Part 1. Fundamentals of Atmospheric Modeling
Overhead Sldes for Chapter 18, Part 1 of Fundamentals of Atmospherc Modelng by Mark Z. Jacobson Department of Cvl & Envronmental Engneerng Stanford Unversty Stanford, CA 94305-4020 January 30, 2002 Types
More informationUniversity of Washington Department of Chemistry Chemistry 452/456 Summer Quarter 2014
Lecture 12 7/25/14 ERD: 7.1-7.5 Devoe: 8.1.1-8.1.2, 8.2.1-8.2.3, 8.4.1-8.4.3 Unversty o Washngton Department o Chemstry Chemstry 452/456 Summer Quarter 2014 A. Free Energy and Changes n Composton: The
More informationIntroduction to Interfacial Segregation. Xiaozhe Zhang 10/02/2015
Introducton to Interfacal Segregaton Xaozhe Zhang 10/02/2015 Interfacal egregaton Segregaton n materal refer to the enrchment of a materal conttuent at a free urface or an nternal nterface of a materal.
More informationProblems from the last lecture
Problems from the last lecture Problem 2.5 Use the Kelvn equaton to calculate the radus of an openended tube wthn whch capllary condensaton of ntrogen at 77 K and a relatve pressure of 0.75 mght be expected.
More informationMass Transfer Processes
Mass Transfer Processes S. Majd Hassanzadeh Department of Earth Scences Faculty of Geoscences Utrecht Unversty Outlne: 1. Measures of Concentraton 2. Volatlzaton and Dssoluton 3. Adsorpton Processes 4.
More informationUniversity of Washington Department of Chemistry Chemistry 452/456 Summer Quarter 2013
Lecture 8/8/3 Unversty o Washngton Departent o Chestry Chestry 45/456 Suer Quarter 3 A. The Gbbs-Duhe Equaton Fro Lecture 7 and ro the dscusson n sectons A and B o ths lecture, t s clear that the actvty
More informationMonolayers. Factors affecting the adsorption from solution. Adsorption of amphiphilic molecules on solid support
Monolayers Adsorption as process Adsorption of gases on solids Adsorption of solutions on solids Factors affecting the adsorption from solution Adsorption of amphiphilic molecules on solid support Adsorption
More informationNAME and Section No. it is found that 0.6 mol of O
NAME and Secton No. Chemstry 391 Fall 7 Exam III KEY 1. (3 Ponts) ***Do 5 out of 6***(If 6 are done only the frst 5 wll be graded)*** a). In the reacton 3O O3 t s found that.6 mol of O are consumed. Fnd
More informationAssignment 4. Adsorption Isotherms
Insttute of Process Engneerng Assgnment 4. Adsorpton Isotherms Part A: Compettve adsorpton of methane and ethane In large scale adsorpton processes, more than one compound from a mxture of gases get adsorbed,
More informationV T for n & P = constant
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
More informationOpen Systems: Chemical Potential and Partial Molar Quantities Chemical Potential
Open Systems: Chemcal Potental and Partal Molar Quanttes Chemcal Potental For closed systems, we have derved the followng relatonshps: du = TdS pdv dh = TdS + Vdp da = SdT pdv dg = VdP SdT For open systems,
More informationEnergy, Entropy, and Availability Balances Phase Equilibria. Nonideal Thermodynamic Property Models. Selecting an Appropriate Model
Lecture 4. Thermodynamcs [Ch. 2] Energy, Entropy, and Avalablty Balances Phase Equlbra - Fugactes and actvty coeffcents -K-values Nondeal Thermodynamc Property Models - P-v-T equaton-of-state models -
More informationCHEMICAL ENGINEERING
Postal Correspondence GATE & PSUs -MT To Buy Postal Correspondence Packages call at 0-9990657855 1 TABLE OF CONTENT S. No. Ttle Page no. 1. Introducton 3 2. Dffuson 10 3. Dryng and Humdfcaton 24 4. Absorpton
More informationThermodynamics II. Department of Chemical Engineering. Prof. Kim, Jong Hak
Thermodynamcs II Department of Chemcal Engneerng Prof. Km, Jong Hak Soluton Thermodynamcs : theory Obectve : lay the theoretcal foundaton for applcatons of thermodynamcs to gas mxture and lqud soluton
More informationCHEMICAL REACTIONS AND DIFFUSION
CHEMICAL REACTIONS AND DIFFUSION A.K.A. NETWORK THERMODYNAMICS BACKGROUND Classcal thermodynamcs descrbes equlbrum states. Non-equlbrum thermodynamcs descrbes steady states. Network thermodynamcs descrbes
More informationChapter 2. Electrode/electrolyte interface: ----Structure and properties
Chapter 2 Electrode/electrolyte nterface: ----Structure and propertes Electrochemcal reactons are nterfacal reactons, the structure and propertes of electrode / electrolytc soluton nterface greatly nfluences
More informationand Statistical Mechanics Material Properties
Statstcal Mechancs and Materal Propertes By Kuno TAKAHASHI Tokyo Insttute of Technology, Tokyo 15-855, JAPA Phone/Fax +81-3-5734-3915 takahak@de.ttech.ac.jp http://www.de.ttech.ac.jp/~kt-lab/ Only for
More informationIf two volatile and miscible liquids are combined to form a solution, Raoult s law is not obeyed. Use the experimental data in Table 9.
9.9 Real Solutons Exhbt Devatons from Raoult s Law If two volatle and mscble lquds are combned to form a soluton, Raoult s law s not obeyed. Use the expermental data n Table 9.3: Physcal Chemstry 00 Pearson
More informationName: SID: Discussion Session:
Name: SID: Dscusson Sesson: Chemcal Engneerng Thermodynamcs 141 -- Fall 007 Thursday, November 15, 007 Mdterm II SOLUTIONS - 70 mnutes 110 Ponts Total Closed Book and Notes (0 ponts) 1. Evaluate whether
More informationChapter 5. Simple Mixtures Fall Semester Physical Chemistry 1 (CHM2201)
Chapter 5. Simple Mixtures 2011 Fall Semester Physical Chemistry 1 (CHM2201) Contents The thermodynamic description of mixtures 5.1 Partial molar quantities 5.2 The thermodynamic of Mixing 5.3 The chemical
More informationIntroduction to Statistical Methods
Introducton to Statstcal Methods Physcs 4362, Lecture #3 hermodynamcs Classcal Statstcal Knetc heory Classcal hermodynamcs Macroscopc approach General propertes of the system Macroscopc varables 1 hermodynamc
More informationa for save as PDF Chemistry 163B Introduction to Multicomponent Systems and Partial Molar Quantities
a for save as PDF Chemstry 163B Introducton to Multcomponent Systems and Partal Molar Quanttes 1 the problem of partal mmolar quanttes mx: 10 moles ethanol C 2 H 5 OH (580 ml) wth 1 mole water H 2 O (18
More informationReview of Classical Thermodynamics
Revew of Classcal hermodynamcs Physcs 4362, Lecture #1, 2 Syllabus What s hermodynamcs? 1 [A law] s more mpressve the greater the smplcty of ts premses, the more dfferent are the knds of thngs t relates,
More informationGouy-Chapman model (1910) The double layer is not as compact as in Helmholtz rigid layer.
CHE465/865, 6-3, Lecture 1, 7 nd Sep., 6 Gouy-Chapman model (191) The double layer s not as compact as n Helmholtz rgd layer. Consder thermal motons of ons: Tendency to ncrease the entropy and make the
More informationEnvr 210, Chapter 3, Intermolecular forces and partitioning Free energies and equilibrium partitioning chemical potential fugacity activity coef.
Envr 20, Chapter 3, Intermolecular forces and parttonng Free energes and equlbrum parttonng chemcal potental fugacty actvty coef. phase transfer- actvty coef and fugactes more on free energes and equlbrum
More informationNAME and Section No.
Chemstry 391 Fall 2007 Exam I KEY (Monday September 17) 1. (25 Ponts) ***Do 5 out of 6***(If 6 are done only the frst 5 wll be graded)*** a). Defne the terms: open system, closed system and solated system
More informationLecture 3 Electrostatic effects November 6, 2009
The stablty of thn (soft) flms Lecture 3 Electrostatc effects November 6, 009 Ian Morrson 009 Revew of Lecture The dsjonng pressure s a jump n pressure at the boundary. It does not vary between the plates.
More informationElectrical double layer: revisit based on boundary conditions
Electrcal double layer: revst based on boundary condtons Jong U. Km Department of Electrcal and Computer Engneerng, Texas A&M Unversty College Staton, TX 77843-318, USA Abstract The electrcal double layer
More informationElectrochemical Equilibrium Electromotive Force
CHM465/865, 24-3, Lecture 5-7, 2 th Sep., 24 lectrochemcal qulbrum lectromotve Force Relaton between chemcal and electrc drvng forces lectrochemcal system at constant T and p: consder Gbbs free energy
More informationOsmotic pressure and protein binding
Osmotc pressure and proten bndng Igor R. Kuznetsov, KochLab Symposum talk 5/15/09 Today we take a closer look at one of the soluton thermodynamcs key ponts from Steve s presentaton. Here t s: d[ln(k off
More informationMS212 Thermodynamics of Materials ( 소재열역학의이해 ) Lecture Note: Chapter 7
2017 Spring Semester MS212 Thermodynamics of Materials ( 소재열역학의이해 ) Lecture Note: Chapter 7 Byungha Shin ( 신병하 ) Dept. of MSE, KAIST Largely based on lecture notes of Prof. Hyuck-Mo Lee and Prof. WooChul
More informationLecture 8. Chapter 7. - Thermodynamic Web - Departure Functions - Review Equations of state (chapter 4, briefly)
Lecture 8 Chapter 5 - Thermodynamc Web - Departure Functons - Revew Equatons of state (chapter 4, brefly) Chapter 6 - Equlbrum (chemcal potental) * Pure Component * Mxtures Chapter 7 - Fugacty (chemcal
More informationEquation of State Modeling of Phase Equilibrium in the Low-Density Polyethylene Process
Equaton of State Modelng of Phase Equlbrum n the Low-Densty Polyethylene Process H. Orbey, C. P. Boks, and C. C. Chen Ind. Eng. Chem. Res. 1998, 37, 4481-4491 Yong Soo Km Thermodynamcs & Propertes Lab.
More informationA Modulated Hydrothermal (MHT) Approach for the Facile. Synthesis of UiO-66-Type MOFs
Supplementary Informaton A Modulated Hydrothermal (MHT) Approach for the Facle Synthess of UO-66-Type MOFs Zhgang Hu, Yongwu Peng, Zx Kang, Yuhong Qan, and Dan Zhao * Department of Chemcal and Bomolecular
More information1. Mean-Field Theory. 2. Bjerrum length
1. Mean-Feld Theory Contnuum models lke the Posson-Nernst-Planck equatons are mean-feld approxmatons whch descrbe how dscrete ons are affected by the mean concentratons c and potental φ. Each on mgrates
More informationChemistry 163B Free Energy and Equilibrium E&R ( ch 6)
Chemstry 163B Free Energy and Equlbrum E&R ( ch 6) 1 ΔG reacton and equlbrum (frst pass) 1. ΔG < spontaneous ( natural, rreversble) ΔG = equlbrum (reversble) ΔG > spontaneous n reverse drecton. ΔG = ΔHΔS
More information5.60 Thermodynamics & Kinetics Spring 2008
MIT OpenCourseWare http://ocw.mt.edu 5.60 Thermodynamcs & Knetcs Sprng 2008 For nformaton about ctng these materals or our Terms of Use, vst: http://ocw.mt.edu/terms. 5.60 Sprng 2008 Lecture #29 page 1
More informationUniversity of Washington Department of Chemistry Chemistry 452/456 Summer Quarter 2014
Lecture 16 8/4/14 Unversty o Washngton Department o Chemstry Chemstry 452/456 Summer Quarter 214. Real Vapors and Fugacty Henry s Law accounts or the propertes o extremely dlute soluton. s shown n Fgure
More information4.2 Chemical Driving Force
4.2. CHEMICL DRIVING FORCE 103 4.2 Chemcal Drvng Force second effect of a chemcal concentraton gradent on dffuson s to change the nature of the drvng force. Ths s because dffuson changes the bondng n a
More informationNon-Ideality Through Fugacity and Activity
Non-Idealty Through Fugacty and Actvty S. Patel Deartment of Chemstry and Bochemstry, Unversty of Delaware, Newark, Delaware 19716, USA Corresondng author. E-mal: saatel@udel.edu 1 I. FUGACITY In ths dscusson,
More informationDiffusion Mass Transfer
Dffuson Mass Transfer General onsderatons Mass transfer refers to mass n transt due to a speces concentraton gradent n a mture. Must have a mture of two or more speces for mass transfer to occur. The speces
More information3. Be able to derive the chemical equilibrium constants from statistical mechanics.
Lecture #17 1 Lecture 17 Objectves: 1. Notaton of chemcal reactons 2. General equlbrum 3. Be able to derve the chemcal equlbrum constants from statstcal mechancs. 4. Identfy how nondeal behavor can be
More informationName ID # For relatively dilute aqueous solutions the molality and molarity are approximately equal.
Name ID # 1 CHEMISTRY 212, Lect. Sect. 002 Dr. G. L. Roberts Exam #1/Sprng 2000 Thursday, February 24, 2000 CLOSED BOOK EXM No notes or books allowed. Calculators may be used. tomc masses of nterest are
More informationThermodynamics and statistical mechanics in materials modelling II
Course MP3 Lecture 8/11/006 (JAE) Course MP3 Lecture 8/11/006 Thermodynamcs and statstcal mechancs n materals modellng II A bref résumé of the physcal concepts used n materals modellng Dr James Ellott.1
More informationThe Second Law of Thermodynamics (Chapter 4)
The Second Law of Thermodynamics (Chapter 4) First Law: Energy of universe is constant: ΔE system = - ΔE surroundings Second Law: New variable, S, entropy. Changes in S, ΔS, tell us which processes made
More informationChemical Equilibrium. Chapter 6 Spontaneity of Reactive Mixtures (gases) Taking into account there are many types of work that a sysem can perform
Ths chapter deals wth chemcal reactons (system) wth lttle or no consderaton on the surroundngs. Chemcal Equlbrum Chapter 6 Spontanety of eactve Mxtures (gases) eactants generatng products would proceed
More informationSOLUTION/EXAMPLES. Contact during the exam: phone: , EXAM TBT4135 BIOPOLYMERS. 14 December Time:
1 NRWEGIN UNIVERSITY F SCIENCE ND TECHNLGY DEPRTMENT F BITECHNLGY Professor Bjørn E. Chrstensen, Department of Botechnology Contact durng the exam: phone: 73593327, 92634016 EXM TBT4135 BIPLYMERS 14 December
More informationHomework Chapter 21 Solutions!!
Homework Chapter 1 Solutons 1.7 1.13 1.17 1.19 1.6 1.33 1.45 1.51 1.71 page 1 Problem 1.7 A mole sample of oxygen gas s confned to a 5 lter vessel at a pressure of 8 atm. Fnd the average translatonal knetc
More informationPhysical Chemistry I for Biochemists. Chem340. Lecture 16 (2/18/11)
hyscal Chemstry I or Bochemsts Chem34 Lecture 16 (/18/11) Yoshtaka Ish Ch4.6, Ch5.1-5.5 & HW5 4.6 Derental Scannng Calormetry (Derental hermal Analyss) sample = C p, s d s + dh uson = ( s )Kdt, [1] where
More informationIntroduction to geochemical modeling
Introducton to geochemcal modelng Prof. Dr. Broder J. Merkel Char of Hydrogeology Technsche Unverstät Bergakademe Freberg Germany What determnes the dstrbuton of aquatc speces? Interactons of aquatc speces
More informationCritical Micellization Concentration Determination using Surface Tension Phenomenon
Critical Micellization Concentration Determination using Phenomenon 1. Introduction Surface-active agents (surfactants) were already known in ancient times, when their properties were used in everyday
More informationEffect of adding an ideal inert gas, M
Effect of adding an ideal inert gas, M Add gas M If there is no change in volume, then the partial pressures of each of the ideal gas components remains unchanged by the addition of M. If the reaction
More informationAdsorption: A gas or gases from a mixture of gases or a liquid (or liquids) from a mixture of liquids is bound physically to the surface of a solid.
Searatons n Chemcal Engneerng Searatons (gas from a mxture of gases, lquds from a mxture of lquds, solds from a soluton of solds n lquds, dssolved gases from lquds, solvents from gases artally/comletely
More informationChapter 3. Property Relations The essence of macroscopic thermodynamics Dependence of U, H, S, G, and F on T, P, V, etc.
Chapter 3 Property Relations The essence of macroscopic thermodynamics Dependence of U, H, S, G, and F on T, P, V, etc. Concepts Energy functions F and G Chemical potential, µ Partial Molar properties
More informationChapters 18 & 19: Themodynamics review. All macroscopic (i.e., human scale) quantities must ultimately be explained on the microscopic scale.
Chapters 18 & 19: Themodynamcs revew ll macroscopc (.e., human scale) quanttes must ultmately be explaned on the mcroscopc scale. Chapter 18: Thermodynamcs Thermodynamcs s the study o the thermal energy
More informationSupplementary Notes for Chapter 9 Mixture Thermodynamics
Supplementary Notes for Chapter 9 Mxture Thermodynamcs Key ponts Nne major topcs of Chapter 9 are revewed below: 1. Notaton and operatonal equatons for mxtures 2. PVTN EOSs for mxtures 3. General effects
More information2.If the concentration is of bulk phenomenon, it is absorption. (e.g) Absorption of Ink on the surface of a chalk.
183101 EGIEERIG CHEMISTRY UIT 3 SURFACE CHEMISTRY TERMS AD DEFIITIOS: 1. Adsorpton: Concentraton of lqud or gaseous molecules over the surface of a sold materal s known as adsorpton. It s a surface phenomenon.
More informationThe Euler Equation. Using the additive property of the internal energy U, we can derive a useful thermodynamic relation the Euler equation.
The Euler Equation Using the additive property of the internal energy U, we can derive a useful thermodynamic relation the Euler equation. Let us differentiate this extensivity condition with respect to
More informationChapter 02: Numerical methods for microfluidics. Xiangyu Hu Technical University of Munich
Chapter 02: Numercal methods for mcrofludcs Xangyu Hu Techncal Unversty of Munch Possble numercal approaches Macroscopc approaches Fnte volume/element method Thn flm method Mcroscopc approaches Molecular
More informationChemical Potential. Combining the First and Second Laws for a closed system, Considering (extensive properties)
Chemical Potential Combining the First and Second Laws for a closed system, Considering (extensive properties) du = TdS pdv Hence For an open system, that is, one that can gain or lose mass, U will also
More informationSolution Thermodynamics
CH2351 Chemcal Engneerng Thermodynamcs II Unt I, II www.msubbu.n Soluton Thermodynamcs www.msubbu.n Dr. M. Subramanan Assocate Professor Department of Chemcal Engneerng Sr Svasubramanya Nadar College of
More informationVapor-Liquid Equilibria for Water+Hydrochloric Acid+Magnesium Chloride and Water+Hydrochloric Acid+Calcium Chloride Systems at Atmospheric Pressure
Chnese J. Chem. Eng., 4() 76 80 (006) RESEARCH OES Vapor-Lqud Equlbra for Water+Hydrochlorc Acd+Magnesum Chlorde and Water+Hydrochlorc Acd+Calcum Chlorde Systems at Atmospherc Pressure ZHAG Yng( 张颖 ) and
More informationMultivariable Calculus
Multivariable Calculus In thermodynamics, we will frequently deal with functions of more than one variable e.g., P PT, V, n, U UT, V, n, U UT, P, n U = energy n = # moles etensive variable: depends on
More informationLecture 2 Grand Canonical Ensemble GCE
Lecture 2 Grand Canoncal Ensemble GCE 2.1 hermodynamc Functons Contnung on from last day we also note that thus, dω = df dµ µd = Sd P dv dµ (2.1) P = V = S = From the expresson for the entropy, we therefore
More informationWilbur and Ague 4 WILBUR AND AGUE; APPENDIX DR1. Two-dimensional chemical maps as well as chemical profiles were done at 15 kv using
DR2006139 Wlbur and Ague 4 WILBUR AND AGUE; APPENDIX DR1 MINERAL ANALYSES Two-dmensonal chemcal maps as well as chemcal profles were done at 15 kv usng the JEOL JXA-8600 electron mcroprobe at Yale Unversty
More information1. Mathematical models of the chromatographic process
1. athematcal models of the chromatographc process - What determnes retenton tme n L? - What causes pea broadenng n L? - Why are the L peas often asymmetrc? - Why s partton chromatography much more popular
More informationSome properties of the Helmholtz free energy
Some properties of the Helmholtz free energy Energy slope is T U(S, ) From the properties of U vs S, it is clear that the Helmholtz free energy is always algebraically less than the internal energy U.
More informationSolution Thermodynamics
Soluton hermodynamcs usng Wagner Notaton by Stanley. Howard Department of aterals and etallurgcal Engneerng South Dakota School of nes and echnology Rapd Cty, SD 57701 January 7, 001 Soluton hermodynamcs
More informationMODULE 6 HUMIDIFICATION AND AIR CONDITIONING
MODULE 6 UMIDIFICATION AND AIR CONDITIONING LECTURE NO. 7 6.7 Evaporaton loss of water n coolng tower: Blowdown: Durng the coolng process of hot water n coolng tower, around % water evaporates [-3]. In
More informationGasometric Determination of NaHCO 3 in a Mixture
60 50 40 0 0 5 15 25 35 40 Temperature ( o C) 9/28/16 Gasometrc Determnaton of NaHCO 3 n a Mxture apor Pressure (mm Hg) apor Pressure of Water 1 NaHCO 3 (s) + H + (aq) Na + (aq) + H 2 O (l) + CO 2 (g)
More informationChapter 3 Thermochemistry of Fuel Air Mixtures
Chapter 3 Thermochemstry of Fuel Ar Mxtures 3-1 Thermochemstry 3- Ideal Gas Model 3-3 Composton of Ar and Fuels 3-4 Combuston Stochometry t 3-5 The1 st Law of Thermodynamcs and Combuston 3-6 Thermal converson
More informationPhysics 607 Exam 1. ( ) = 1, Γ( z +1) = zγ( z) x n e x2 dx = 1. e x2
Physcs 607 Exam 1 Please be well-organzed, and show all sgnfcant steps clearly n all problems. You are graded on your wor, so please do not just wrte down answers wth no explanaton! Do all your wor on
More informationPETE 310 Lectures # 24 & 25 Chapter 12 Gas Liquid Equilibrium
ETE 30 Lectures # 24 & 25 Chapter 2 Gas Lqud Equlbrum Thermal Equlbrum Object A hgh T, Object B low T Intal contact tme Intermedate tme. Later tme Mechancal Equlbrum ressure essels Vale Closed Vale Open
More information1) Silicon oxide has a typical surface potential in an aqueous medium of ϕ,0
1) Slcon oxde has a typcal surface potental n an aqueous medum of ϕ, = 7 mv n 5 mm l at ph 9. Whch concentraton of catons do you roughly expect close to the surface? What s the average dstance between
More informationMonte Carlo method II
Course MP3 Lecture 5 14/11/2006 Monte Carlo method II How to put some real physcs nto the Monte Carlo method Dr James Ellott 5.1 Monte Carlo method revsted In lecture 4, we ntroduced the Monte Carlo (MC)
More informationChapter 3 - First Law of Thermodynamics
Chapter 3 - dynamics The ideal gas law is a combination of three intuitive relationships between pressure, volume, temp and moles. David J. Starling Penn State Hazleton Fall 2013 When a gas expands, it
More informationPhase equilibria Introduction General equilibrium conditions
.5 hase equlbra.5. Introducton A gven amount of matter (usually called a system) can be characterzed by unform ntensve propertes n ts whole volume or only n some of ts parts; a porton of matter wth unform
More informationChemical Engineering 160/260 Polymer Science and Engineering. Lecture 10 - Phase Equilibria and Polymer Blends February 7, 2001
Checal Engneerng 60/60 Polyer Scence and Engneerng Lecture 0 - Phase Equlbra and Polyer Blends February 7, 00 Therodynacs of Polyer Blends: Part Objectves! To develop the classcal Flory-Huggns theory for
More informationTurbulent Nonpremixed Flames
School of Aerospace Engneerng Turbulent Nonpremxed Flames Jerry Setzman. 5 Mole Fracton.15.1.5 CH4 HO HCO x 1 Temperature Methane Flame.1..3 Dstance (cm) 15 1 5 Temperature (K) TurbulentNonpremxed -1 School
More informationGeneral Thermodynamics for Process Simulation. Dr. Jungho Cho, Professor Department of Chemical Engineering Dong Yang University
General Thermodynamcs for Process Smulaton Dr. Jungho Cho, Professor Department of Chemcal Engneerng Dong Yang Unversty Four Crtera for Equlbra μ = μ v Stuaton α T = T β α β P = P l μ = μ l1 l 2 Thermal
More informationSupporting Materials
Chrstopher Lockhart and Dmtr K. Klmov Molecular nteractons of Alzhemer's bomarker FDDNP wth A peptde Supportng Materals Parameterzaton of FDDNP molecule: CHARMM General Force Feld (CGenFF verson 2b6) was
More information3.5. Kinetic Approach for Isotherms
We have arrived isotherm equations which describe adsorption from the two dimensional equation of state via the Gibbs equation (with a saturation limit usually associated with monolayer coverage). The
More informationln( P vap(s) / torr) = T / K ln( P vap(l) / torr) = T / K
Chem 4501 Introduction to Thermodynamics, 3 Credits Kinetics, and Statistical Mechanics Fall Semester 2017 Homework Problem Set Number 9 Solutions 1. McQuarrie and Simon, 9-4. Paraphrase: Given expressions
More informationQ e E i /k B. i i i i
Water and Aqueous Solutons 3. Lattce Model of a Flud Lattce Models Lattce models provde a mnmalst, or coarse-graned, framework for descrbng the translatonal, rotatonal, and conformatonal degrees of freedom
More informationSTATISTICAL MECHANICS
STATISTICAL MECHANICS Thermal Energy Recall that KE can always be separated nto 2 terms: KE system = 1 2 M 2 total v CM KE nternal Rgd-body rotaton and elastc / sound waves Use smplfyng assumptons KE of
More informationThermodynamics General
Thermodynamcs General Lecture 1 Lecture 1 s devoted to establshng buldng blocks for dscussng thermodynamcs. In addton, the equaton of state wll be establshed. I. Buldng blocks for thermodynamcs A. Dmensons,
More informationChemical Engineering Department University of Washington
Chemcal Engneerng Department Unversty of Washngton ChemE 60 - Exam I July 4, 003 - Mass Flow Rate of Steam Through a Turbne (5 onts) Steam enters a turbne at 70 o C and.8 Ma and leaves at 00 ka wth a qualty
More informationYou MUST sign the honor pledge:
CHEM 3411 MWF 9:00AM Fall 2010 Physical Chemistry I Exam #2, Version B (Dated: October 15, 2010) Name: GT-ID: NOTE: Partial Credit will be awarded! However, full credit will be awarded only if the correct
More informationI wish to publish my paper on The International Journal of Thermophysics. A Practical Method to Calculate Partial Properties from Equation of State
I wsh to publsh my paper on The Internatonal Journal of Thermophyscs. Ttle: A Practcal Method to Calculate Partal Propertes from Equaton of State Authors: Ryo Akasaka (correspondng author) 1 and Takehro
More informationPhysics Nov The Direction of a Reaction A + B C,
Physcs 301 12-Nov-2003 21-1 Suppose we have a reacton such as The Drecton of a Reacton A + B C whch has come to equlbrum at some temperature τ. Now we rase the temperature. Does the equlbrum shft to the
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 informationComputation of Phase Equilibrium and Phase Envelopes
Downloaded from orbt.dtu.dk on: Sep 24, 2018 Computaton of Phase Equlbrum and Phase Envelopes Rtschel, Tobas Kasper Skovborg; Jørgensen, John Bagterp Publcaton date: 2017 Document Verson Publsher's PDF,
More informationTP A SOLUTION. For an ideal monatomic gas U=3/2nRT, Since the process is at constant pressure Q = C. giving ) =1000/(5/2*8.31*10)
T A SOLUTION For an deal monatomc gas U/nRT, Snce the process s at constant pressure Q C pn T gvng a: n Q /( 5 / R T ) /(5/*8.*) C V / R and C / R + R 5 / R. U U / nr T (/ ) R T ( Q / 5 / R T ) Q / 5 Q
More informationEinstein Classes, Unit No. 102, 103, Vardhman Ring Road Plaza, Vikas Puri Extn., Outer Ring Road New Delhi , Ph. : ,
CT 1 THERMODYNAMICS 6.1 Thermodynamcs Terms : Q. Defne system and surroundngs. Soluton : A system n thermodynamcs refers to that part of unverse n whch observatons are made and remanng unverse consttutes
More informationAn Improved Model for the Droplet Size Distribution in Sprays Developed From the Principle of Entropy Generation maximization
ILASS Amercas, 9 th Annual Conference on Lqud Atomzaton and Spray Systems, oronto, Canada, May 6 An Improved Model for the Droplet Sze Dstrbuton n Sprays Developed From the Prncple of Entropy Generaton
More informationThe Chemical Potential
CHEM 331 Physical Chemistry Fall 2017 The Chemical Potential Here we complete our pivot towards chemical thermodynamics with the introduction of the Chemical Potential ( ). This concept was first introduced
More informationPrediction of Ultrasonic Velocity in Binary Mixtures of a Nuclear Extractant and Monocarboxylic Acids using Several Theoretical Models
Predcton of ltrasonc Velocty n Bnary Mxtures of a Nuclear Extractant and Monocarboxylc Acds usng Several Theoretcal Models R. K. Mshra 1, B. Dala 1*, N. Swan 2 and S.K. Dash 3 1 BSH, Gandh Insttute of
More information