Chemical Potential And Gibbs Distribution

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Chemical potential and Gibbs DistributionAnders Malthe-Sørenssen21. oktober 20131

1Chemical potentialWe started from the microcanonical ensemble, where U, V, N was constant. Then we introduced thepossibility for energy exchange, by looking at systems in contact with a large heat bath. But, still thenumber of particles were constant. But for many systems we are interested in, the number of particlesis not constant: for a crystal growing, for ice melting, for chemical reactions, the number of particlesare not constant. How can we extend the methods we have developed to handle non-constant particlenumbers?We have seen that: If two systems have the same temperature there is no net energy flow between them. If two systems have the same pressure, there is no net change of volumes If two systems have the same X, there is no net flow of particlesWhat is this X? We call it the chemical potential: If two systems are at the same temperature andonly have a single chemical species and the same value of the chemical potential, there is no net flux ofparticles from one side to another.But if the chemical potential is different, there will be a net flux. We have seen this example earlier,when we looked at two gases with different particle numbers in the same volume.How can we relate the chemical potential to other quantities we know?First, if we consider two systems A and B in contact with a heat bath at temperature T , but where thereis a diffusive equilibrium between A and B. The Helmholtz free energy for this system is thenF FA FB ,where NA NB N . Helmholtz free energy will be minium with respect to dNA dNB at equilibrium,and therefore FA FB F 0, N NA T,V NB T,Vwhich gives FB NA T,V FB NB ,T,Vat equilibrium. This severes as a good definition of chemical potential: F,µ(T, V, N ) N T,Vso that the differential for Helmholtz free energy is:dF SdT pdV µdN .The condition that µA µB characterizes the diffusive equilbrium between two systems in diffusivecontact.Notice that we cannot really divide particles into smaller pieces than one, so that the chemical potentialshould be defined as a finite difference:µ(T, V, N ) F (T, V, N ) F (T, V, N 1) ,If several chemical species are present, then each species will have its own chemical potential Fµj (T, V, N ) , Nj T,Vwhere all the other Nj are kept constant in the derivative.2

1.1Example: Chemical potential of the Einstein crystalWe found the Helmholtz free energy for the Einstein crystal to be N 1,Z 1 exp β andF kT ln Z N kT ln(1 exp( β )) ,which gives µ 1.2 F N kT ln (1 exp( β )) .Example: Chemical potential for Ideal gasFor an ideal gas, the partition function can be written as:Z 1N(Z1 Zvib Zrot ) ,N!where Z1 nQ V and nQ m2π 2 β 3/2.Helmholtz free energy is therefore:F kT ln Z kt (N ln Z1 ln N !) .We use Stirling’s approximation ln N ! ' N ln N N , getting:ddln N ! (N ln N N ) ln N 1 1 ln N ,dNdNwhich gives F kT dln Z1 ln N ! kT (ln Z1 ln N ) kT ln(N/Z1 ) .dNWe insert Z1 nQ V , getting:µ kT ln(N/V nQ ) kT ln(n/nQ ) .(We could also have found this by using µ F (N ) F (N 1), and we would then not have had to useStirling’s approximation. The result would have been the same).We see that the chemical potential increase with the density n of particles: Particles flow from systemswith high n to systems with low n.For classical concentrations – that is when n/nQ 1, the chemical potential of an ideal gas is alwaysnegative.2Potential energy and the chemical potentialWe can better understand the chemical potential by looking at a system with a difference (or a gradient)in potential energy. The simplest example is a potential step.Let us look at two systems A and B a the same temperature that may exchange particles, but the twosystems are not yet in diffusive. We assume that we start from µB µA so that particles will flow fromB to A. The difference in chemical potential is µ µB µA .3

Let us now introduce a difference in potential energy between the two systems. For example, for chargedparticles we may introduce an electric field with a voltage difference V . We apply this to all particles insystem A so that we raise their potential energy by µ. This is done by choose the potential differenceso thatq V q(VB VA ) µ .(We could also have used a difference in gravitational potential energy, mgh, or other ways to introducea potential difference).Let us now reanalyze the system thermodynamically. We have changed the potential energy of all particlesin system A, but we have not made any changes in system B. This means that we have change the energyUA of system A and Helmholtz free energy FA , but we have not changed either UB or FB . The changein free energy in system A is by the change in internal energy, UA NA q V – this means that theenergy of every state in system A has changed by mu q V . This means that the chemcial potentialin system A in the state (2) after the potential is applied, can be expressed in terms of the chemicalpotential in the states (1) before the potential was added:µA (2) µA (1) µ µA (1) (µB (1) µA (1)) µB (1) µB (2) .There is therefore no longer any difference in chemical potential – and there will not be any particle flux.This means that:The difference in chemical potential between two systems A and B corresponds to the potential energydifference needed in order to establish diffusional equilibrium.We could use this measure the chemical potential: We apply a potential difference and determine at whatpotential difference net particle flow stops.It is useful to discern between the internal and the external chemical potential. The external chemicalpotential is the potential energy per particle in an external field, and the internal chemical potentialenergy is the chemical potential that would be present without the external field.2.1Example: Barometric pressure formulaLet us assume that the atmosphere in the Earth is at the same temperature T . The potential energy ofa gas particle would be mgz, where we may place the zero in potential energy at the Earths surface. Thechemical potential of a particle in a gas in a graviational field would therefore have two contributions:µ µgas µgrav kT ln(n/nQ ) mgz .In equilbrium there should be no differences in chemical potential, hencekT ln(n(z)/nQ ) mgz kT ln(n(0)/nQ ) ,which givesn(z) n(0) exp( mgz/kT ) .What does that mean for the pressure of an ideal gas? If the temperature does not depend on height,the pressure isNpV N kT p kT nkT ,Vandp(z) p(0) exp( mgz/kT ) p(0) exp( z/zc ) ,where zc kT /mg is a characteristic height.This depends on the mass of the gas molecules! For N2 the mass of a molecule is 28 which gives zc 8.5km.Lighter molecules will extend further up – and will mostly have escaped from the atmosphere. Noticethat T is not really constant, and n(z) is generally more complicated. And also notice that various gaseshave different m, and will therefore have different values of zc – which means that the composition ofthe air will change with distance z as well.4

2.2Example: Batteries(Not written yet)2.3Potential energy adsorbed in FWe can also directly see how a potential energy enters the various expressions.Assume that we have a system with energy states i . Let us assume that we add a potential energy E0to the system, so that the new levels are i E0 .What is the consequences for Helmholtz free energy and the chemical potential?The partition function isXXZ0 exp( i /kT E0 /kT ) exp( E0 /kT )exp( /kT ) exp( E0 /kT )Z ,iiHeltholtz free energy is thereforeF 0 kT ln Z 0 E0 kT ln Z E0 F ,which corresponds to a change in Helmholtz free energy.If this is the energy for each particle, we expect that the energy for N particles (or that ZN Z 0N ), isF N kT ln Z N E0 ,and that the chemical potential therefore is 0 Fµ0 E0 µ . N V,TAdding a potential energy per particle therefore corresponds to adding a potential energy to the chemicalpotential. We call such an addition an extenal chemical potential if it is due to an external field, ascompared to the internal chemical potential which is due to the statistical physics of the system withoutthe external potential.2.43Example: Modeling potential gradientsThermodynamic relations for chemical potentialHere, we have defined the chemical potential as µ F N .V,THow does this relate the the thermodynamic identity and to the relations we introduced, but did notpursue, for the microcanonical ensemble?From the microcanonical ensemble we introduce the entropy, S(U, V, N ), and we argued that S S SdS dU dV dN U V,N V U,N N U,N 1p S dU dV dN .TT N U,N5

We can rewrite this to get: T dS dU pdV T S N dN .U,NIn addition, we know that F U T S so that dF dU T dS SdT , which is therefore S SdF dU T dS SdT dU (dU pdV TdN ) SdT SdT pdV TdN N U,N N U,Nwhich means that µ F N TT,V S N .U,NWe have therefore related the two expressions for the chemical potential, and found that what we earliercalled the chemical potential indeed corresponds to what we now call the chemical potential – and whatwe now are starting to build an intuition for. Good! We are on the right way.We can therefore also write the thermodynamic identity asT dS dU pdV µdN .Where we now have an intuition for the chemical potential.4Gibbs factor and Gibbs sumNow – let us see how we can treat systems where the number of particles may change from a microscopicpoint of view.For a system in thermal equilbrium with a large heat bath, we found that the probability for the systemto be in state ii could be expressed asP (i) exp( i /kT ),Zwhere the partition function Z is a normalization constant.How can we generalize this to a system S in contact with a reservoir R – but where the contact allowsboth exchange of energy and exchange of particles?Let us look at a composite system which consists of the system S and a reservoir R. The system Sand reservoir R can exchange energy and particles, but the total composite system (S R) is thermallyisolated (it has constant energy) and has constant number of particles:U0 US UR , N0 NS NR ,are both constant. Let us now look at a particular case where system S is in a state 1 with energy U1and number of particles N1 . What is the probability for this state?Since S is in state 1, the multiplicity of S is 1. The multiplicity g of the whole system (R S) is thereforethe multiplicity of R, which depends on U1 and N1 , and the probability for the system S to be in state1 characterized by U1 and N1 is thereforeg(N0 N1 , U0 U1 )P (N1 , U1 ) P.g(N0 N1 , U0 U1 )Let us now look at ln P :ln P (N1 , U1 ) ln C ln g(N0 N1 , U0 U1 ) ln C S(N0 N1 , U0 U1 )/k ,6

where we can now expand S around N0 , U0 to first order, getting: S SS(N0 N1 , U0 U1 ) S(N0 , U0 ) N1 U1, N U0 U N0where we now recognize the two partial derivatives of S as 1/T and µ/T , giving:S(N0 N1 , U0 U1 ) S(N0 , U0 ) N1 µ U1 ,TTand therefore we find:P (N1 , U1 ) C 0 exp((N1 µ U1 )/kT ) ,and where normalization now gives:P (N1 , U1 ) 1,ZGandXXZG exp((N µ s(N ) )/kT ) .N s(N )This sum is called Gibbs sum or the grand sum or the grand partition function. Notice that the sum isover all the states of the system for each particle number N , starting from N 0.Again, we find averages by sums of the probabilities:XXhXi X(N, s)P (N, s) ,N s(N )Notice that both the energy and the number of particles now are fluctuating quantities!4.1Average number of particlesThe average number of particles is given ashN i 1 XXN exp((N µ s )/kT .ZGN s(N )we can again use the “derivative trick” we used earlier, but now take the derivative with respect to µ:N exp((N µ s )/kT ) kTand thereforehN i kT4.2dexp((N µ s )/kT ) ,dµ1 d ln ZGZG kT.ZG dµ µExample: CO poisoningEach hemoglobin molecule has four, independent adsorption sites, each consiting of a Fe2 ion, and eachsite can couple to one O2 molecule. The system therefore has two possible states, occupied by oxygenand not occupied by oxygen, with energies 0 (unoccupied) and (occupied), where 0.7eV .In this case, we analyze the system using the grand partition function.ZG 1 exp( ( µ)/kT ) ,7

What is µ in this case? Near the lungs, we assume the blood is in diffusive equilbrium with the air inthe lungs, and we can therefore use the chemical potential for an ideal gas:µ kT ln(nQ /n) ' 0.6eV ,when T 310K, which is the temperature in your body. This givesexp( ( µ)/kT ) ' exp(0.1eV/kT ) ' 40 ,which means that the probabilty to be occupied isP 40' 0.98 .1 40Now, what happens if CO is also present, which also can be adsorbed. Now, there are three possiblestates: unoccupied, occupied by O2 or occupied by CO. The grand partition function is nowZG 1 exp( ( O µO )/kT ) exp( ( CO µCO )/kT )) .Now we need numbers. CO is more strongly bound, so CO 0.85eV . But what is the chemicalpotential? We could still use the expression for the ideal gas, but with the concentration n of CO in air.If CO is x times less abundant that oxygen, we would find thatµCO kT ln(nQ /nCO ) kT ln(nQ /xnO ) kT ln(nQ /nO ) kT ln x ,where kT ln 100 0.12eV, so that µCO 0.72eV. This gives for the new Gibbs factor:exp( ( CO µCO )/kT ) 120 ,and thereforeP (O) 40 0.25 .1 40 120So just a small amount of CO is devastating!4.35Numerical example: VacanciesGibbs Free Energy and Chemical ReactionsWe introduced Helmholtz free energy, F , to describe systems with constant T , V , and N . However, inmany experimental and practical situations it is not the volume that is constant, but we perform anexperiment at constant pressure – this is what happens if we perform an experiment here in the lecturehall.In this case it is useful to introduce another free energy to address the equilibrium at constant T , p, andN , Gibbs free energy, G:G F pV U T S pV .We can show that Gibbs free energy is minimal in equilibrium. We consider a case where the system Sis in thermal equilbrium with a heat reservoir R1 and mechanical equilbrium with a pressure reservoirR2 . The differential for G isdG dU T dS SdT pdV V dp .We insert the thermodynamic identity, T dS dU pdV µdN , getting:dG SdT V dp µdN ,and when pressure and temperature (and N ) is constant, dp 0 and dT 0, dN 0, we getdGS 0 .8

This shows that GS is either a maximum or a minimum. What is it? Any irreversible change in thesystem S will result in an increase in the entropy, dS 0, and therefore dG 0, which means that G isa minimum for a system in equilbrium.From the differential in equation 5 we see that G G GdG dT dp dN SdT V dp µdN , T p,N p T,N N T,pwhich gives the following expressions: G G G S , V , µ. T p,N p T,N N T,pWe can now find three Maxwell relations – you may do this for yourself.6Intensive, Extensive Variables, and GWe take two identical systems – for example two system of ideal gas or two systems of the einstein crystal– and put them together, forming a system with double the number of particles.Some variable will change and some will not in this process.We call the variable that dot not change intensive variables. They are p, T , µ.Other variables are linear in N : They double when the system doubles. We call these variables extensivevariables. Examples are U , S, V , N , F , G.If G is directly proportional to N , we can write G N g(p, T ), where g G/N . What is g? It is simply G g,µ N T,pandG(T, p, N ) N µ(T, p) .7Multi-component systemsHow can we generalize all our results to multi-component systems?Originally, we introduced the thermodynamic identity from the microcanonical ensemble, and we foundthat we could write the entropy, S as a function of U and V , which gave us the differentialedS p1dU dV ,TTthen we extended to a system with N particles, gettingdS 1pµdU dV dN .TTTThis can now directly be extended to a system with j 1, . . . , k different species by introducing a termrelated to the diffusive equilbrium for each of the species, resulting in (review the original introductionif you are in doubt):X µj1pdS dU dV dNj .TTTj9

Similarly, we can generalize the chemical potential we found from Helmholtz free energy (which is thesame as the one we found from the entropy): F.µj Nj T,V,{Nj }And similarly for Gibbs free energy:G(T, p, {Nj }) XNj µj .jThe thermodynamic identity then becomesT dS dU pdV Xµj dNj ,jand the differential for G becomesdG SdT V dp Xµj dNj .jWe will use this to address reactions between different chemical components – by introducing the fundamental laws of chemistry.8Dilute solutions(Ikke pensum i 2013)9Chemical reactionsWe now have what we need to address chemical reactions – how some species are transformed into otherspecies without changing the total number of atoms. (The total number of particles may change).We describe a chemical reaction by it stochiometric coefficients, νj :ν1 A1 ν2 A2 . . . νk Ak 0 ,where Aj describes a chemical species such as O or O2 or H2 O. For example, the reactionH OH H2 O ,is described as 1 H 1 OH 1 H2 O 0 ,that isν1 1 , A1 H , ν2 1 , A2 OH , ν3 1 , A3 H2 O .Usually, we consider equilibrium in a chemical reaction at constant pressure and temperature – this ishow most experiments are done, and how I would do it here in the lecture hall.In equilibrium, Gibbs free energy must therefore be minimal, and the differential must be zero:XdG µj dNj 0 .j10

Now, what are the changes in Nj in such a chemical potential? Notice, that the Nj values may not bethe same – they may all be different. But for each chemical reaction that happens, the relationXνj Aj 0 ,jmust hold. What does that means – it means that the changes must be similarly related. If the chemicalreaction happens m times, then the change in species j from before and after the reaction is νj m. (Thesign depends on what way the reaction goes the m times). This means the dNj νj m, and thereforethat XXXdG µj dNj µj νj m νj µj m ,jjjand in equilibrium we know that dG 0. We therefore get a relation that is independent of m: XXdG νj µj m 0 νj µj 0 .jjThis is the condition for chemical equilibrium. We can calculate it for any reaction if we only know thechemical potential µj for each of the species. (Notice that this relation is derived for constant p and T ,but it also applied to the equilibrium of reactions at constant T and V ).Notice: The chemical potential µj is an intensive quantity, but it does in principle depend on the otherNi values, because G,µj Nj T,p,{Ni }where the derivative is over all i 6 j. But since we expect µj to be intensive, we may instead assumethat it only depends on the fractions, Xi Ni /N of particles of species j, which does not change whenwe change N .Notice also that it is usual to call the relationdG SdT V dp Xµj dNj 0 ,j(which it is in equilibrium) the Gibbs-Duhem relation when rewritten asXµj dNj SdT V dp .j10Chemical equilibrium for Ideal Gas systemsIf each of the constituent can be described as ideal gases – which are non-interacting by design andtherefore have no cross-dependencies in their chemical potentials, we get nice and simple results.(How reasonable is this for example for a material in a dilute solution - you should discuss this here!)For an ideal gas we know thatµ kT ln(nQ /n) ,which we can write asµj kT ln(nj /nQ,j Zj,int ) kT (ln nj ln cj ) ,where cj nQ,j Zj,int depends on the temperature, but it does not depend on the concentration nj (orany of the other concentrations ni ). Here, Zj,int is the partition function for the other, internal degreesof freedom.11

We can rewrite the equilibrium condition to beXXνj ln nj νj ln cj (T ) ,jjwhich we can write asXνln nj j Xjjand we can writeXνln nj j lnYjandXνln cj j ,νnj j ,jνln cj j lnYνcj j K(T ) .jjwhich is a function of temperature, T , but not the densities nj . We call this the equilibrium constant.Notice that we can actually calculate this for ideal gases!We therefore getYνnj j K(T ) ,jwhich is called the law of mass action (massevirkningsloven).Notice that when we calculate K(T ) we must be very careful to choose a consistent value for all theenergies – we need to select the zero level in the same way for all the particles.(We will see this clearly in an example later.)One way to define energies that are internally consistent can be explained through a disassociationreaction, where a molecule A2 disassociates into 2A. In this case, we should choose the zero level of eachcomposite particle (A2 ) to be the energy of the disassociated particles (A) at rest. That is, if the bindingenergy for A2 is (this is the energy needed to place the two consituents of A2 infinitely far away fromeach other), we place the ground state of the composite particle (A2 ) at .10.1Example: Disassociation of hydrogenWe start with the reactionH2 2Hwhich also can be written asH2 - 2H 0The law of mass action gives:Yνnj j K(T ) ,jwhere j 1 corresponds to H2 , so that ν1 1, and j 2 corresponds to H, so that ν2 2.It is usual to writenH2 as [H2 ]The law of mass action is therefore12

2[H2 ] [H] [H2 ]2[H] K(T ) ,This means that1[H2 ] ,1/2[H][H2 ] K 1/2so that the relative concentration of hydrogen is inversely proportional to the concentration of H2 .What is K(T )? We find thatln K ln nQ (H2 ) 2 ln nQ (H) F (H2 )/kT ,where spin factors are put into F . Zero of energy is for an H atom at rest.If H2 is more tightly bound, then the more negative if F and the higher is K. As a result there is ahigher proportion of H2 in the mixture – which is not surprising.10.2Example: pH and the Ionization of waterWater goes through the processH2 O H OH ,when in liquid form. This process is called the disassociation of water.The law of mass action gives: OH [H2 O] K(T ) .H(We should now really have introduced dilute solutions already – but this is not currently part of thecurriculum – we need to change this).In pure water each of the concentrations are H OH 10 7 mol l 1 .We can change this concentration by introducing a proton donor. This increases the number of H ionsand decreases the number of OH ions to ensure the product of the concentrations is constant.It is usualy to introduce the pH through pH log10 H .The pH of pure water is therefore 7.Strong acids have low pH values. An apple has pH around 3.10.3Example: Kinetics, reaction rates, and catalytic processesWhat if we study the processA B AB ,Then the rate at which the concentrations changes are related bydnAB CnA nB DnAB ,dt13

where C describes how AB is formed in collisions and D is the reverse process.In equilibrium the concentrations does not change, andCnA nB DnAB ,which also are related by the law of mass action:nA nBD K(T ) .nABCNow, what if AB is not formed by collisions between A and B, but in a two step process involving acatalyst E:A E AE , AE B AB E ,where E is returned to its original state after the reaction.What is the point of E? It may increase the rates significantly?How? The rates are not only determined by the energy of the final configuration, but also by an energybarrier. The rate is determined by the height of the energy barrier and the temperature (Arrheniusprocesses). However, by introducing E we may lower the energy barrier in each step, increasing the rateof the reaction.Now, if the process is rapid so that E is short lived, then AE does not form a significant quantity of A.Then the ratio nA nB /nAB is the same as we found above – it is given by the law of mass action. Theroute taken by the reaction is not important - the end result is the same.In equilibrium, the direct and the inverse reaction rates must be the same – what we assumed above –is called the principle of detailed balance.10.4Example: Dissolved OxygenHenry’s law. Needs dilute solutions. Not part of the curriculum. May do later.10.5Example: Charge distribution of the Hemoglobin Moleculelonger analytical and numerical example.11Phase transformationsWe call the curve P (V ) for constant T an isotherm.Let us sketch an isotherm for a real gas (not ideal) - such as the Lennard-Jones system we introduced.We can have solid, liquid, and gas phases.14

pIsotherm, T constDUILIQLIQUID GASGASVLIQUIDLIQUID GASGASA phase is a portion of a system that is uniform in composition. (Whatever that means).Two phases can exist at the same time. For example, an isotherm may go from a liquid to a gas, througha region where the liquid and gas coexists.As we continue to increase the volume (pull the piston), we change the composition of gas and liquid inthe same, until all is gas.Liquid and gas (vapor) may coexist only when the isotherm is below the critical temperature. Abovethis, we cannot discern a liquid from its vapor, and we talk about a fluid instead.pLIQUIDCritical pointMeltingMp constBEvaporationSOLIDTriple pointGASSublimationT15

Critical T forO2 is 154.3 K H2O is 647.1 K CO2 is 304.2 K N2 is 126.0 K H2 is 33.2 KWhat is the condition for the isotherm?The system is in thermal equilbrium at the isotherm. Since the system is at constant p, and T , thismeans that Gibbs free energy for the system is minimal.Gibbs free energy will have contributions from both the gas, liquid and solid phases, and we can writeng Ng /N0 , nl Nl /N0 and ns Ns /N0 . The total Gibbs free energy isG(ns , nl , ng , p, T ) ns gs (p, T ) nl gl (p, T ) ng gg (p, T ) ,andn ns nl ng const. .Notice that in general the three (molar) energies may have different behaviors with p, T . We have sketchedtheir behavior for a constant p line as shown in the figure above:ggsglggSolid is stableLiquid is stableTM(p)Melting pointGas is stableTB(p)Boiling pointTThe phase equilibria are characterized bygl (T, pv (T )) gg (T, pv (T )) ,This also corresponds to µg (p, T ) µl (p, T ), but let us stay with Gibbs free energy for now.11.1Coexistence curve, p(T )Let us find p(T ) for coexistence.The condition that gl gg along the curve means that if we start at T0 and then move a small distancedT along the curve, we will getgl (p0 , T0 ) gg (p0 , T0 ) ,andgl (p0 dp, T0 dT ) gg (p0 dp, T0 dT ) ,We subtract the two, gettingdgl gl (p0 dP, T0 dT ) gl (p0 , T0 ) dgg gg (p0 dP, T0 dT ) gg (p0 , T0 ) .16

We can now write dgl and dgs by the corresponding differentialsdgl sl dT vl dp ,dgg sg dT vg dp ,We subtract the two equations, and use that dgl dgg , getting:(sg sl )dT (vg vl )dp 0and dpdT along curvesg sl,vg vlWhat is sg sl ?The increase in entropy when we transfer one molecule (or one mole, depending on the definition of n)from the liquid to the gas phase.And vg vl is the change in volume in the system when we transfer one molecule from the liquid to thegas.Notice that this is only true for the coexistence curve p(T ).We can relate sg sl to the heat that must be added to the system in order to keep the temperatureconstant.The heat added isQ T (sg sl ) ,We introduceL T (sg sl ) ,as the latent heat of vaporization.We also introduce v vg vl .Then we havedpL .dTT vThis is called Clausius-Clapeyrons equation.We can make two approximations to make it simpler.(i) If vg vl then v ' vg .(ii) We assume that the ideal gas law, pV N kT , applies to the gas phase, so that v kT /p. Thenthe equation becomesLdp p,dTkT 2anddLln p .dTkT 2Given L(T ), we can integrate the equation to find the curve.If the latent heat is not dependent on T over a region, then we can find the solution:ZZdpdT L0,pkT 217

andln p L0 /kT const ,andp(T ) p0 exp( L0 /kT ) .Triple point: All phases coexist in equilibrium.Used to define Kelvin scale. at 0.01K above melt temp at atmospheric pressure. (0.01 deg celcius).11.2Latent heat and entalpyThe latent heat correspond to the difference of H U pV between two phases when the process occursat constant pressure p. The quantity H is called the entalpy.Let us show this:Along the coexistence curve we have µl µg . The theromdynamic identity is thereforeT dS dU pdV (µg µl ) dN ,but since µg µl the last term is zero.At constant pressure, the latent heat is the heat T dS transferred, which isL T dS dU pdV dH dU pdV V dp Hg Hl . {z} 0We find the values of H by integrating the heat capacity at constant pressure: dS U V HCP T p .dT p T p T p T pandZH 11.3Cp dT .Model system for solid-gas equilibriumEquilibrium between ideal gas and Einstein crystal.Energy in crystal is n 0 , where 0 is the binding energy,The partition function for a single oscillator isZs Xexp( (i 0 )/kT ) iexp( 0 /kT ).1 exp( /kT )and Fs is Fs kT ln Zs and Gs Fs pvs µs , where we assume that pvs is small and we ignore it.The activity isλs exp(µs /kT ) ' exp(Fs /kT ) exp( ln Zg ) 1exp( 0 /kT ) .ZG1 exp( /kT )For a zero spin ideal gas, the chemical potential isµg kT ln Z kT ln(nQ /n) ,18

and the activity isλg npp nQkT nQkT 2π 2M kT 3/2.For equilibrium the two activities are equal:p kT nQexp( 0 /kT )1 exp( /kT )and we insert nQ , gettingp(T ) 1212.1 m 3/2exp( 0 /kT )kT 5 /22π 21 exp( /kT )Modeling real gases using Lennard-Jones systemsMatlab MD script% LJ MD calculationclear all ; clf ;L 10; % Number of atoms L 2N L*L;rho 0.8; % reduced densityTemp 0.1; % reduced temperaturensteps 10000;dt 0.02;printfreq 1;% Initial coordinates on cubic gridr zeros (N ,2) ;v zeros (N ,2) ;[ x y ] meshgrid ((0: L -1) ,(0: L -1) ) ;r (: ,1) x (:) ; r (: ,2) y (:) ;% Rescale to wanted rhoL L *(1.0/ rho 2) ; r r *(1.0/ rho 2) ;% Initialize with wanted Tv sqrt ( Temp ) * randn (N ,2

For classical concentrations { that is when n n Q 1, the chemical potential of an ideal gas is always negative. 2 Potential energy and the chemical potential We can better understand the chemical potential by looking at a system with a di erence (or a gradient) in

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VARIABLES & MAXWELL RELATIONS. Some More Thermodynamic Potentials. The Gibbs Function, sometimes known as the Gibbs Free Energy or Gibbs Potential has already been introduced in its magnetic form when dealing with the thermodynamics of paramagnetism. There we defined the magnetic Gibbs function G U TS B 0 M Mag

8.2 THE PARTIAL MOLAR GIBBS ENERGY AND THE GENERALIZED GIBBS-DUHEM EQUATION Since the Gibbs energy of a multicomponent mixture is a function of temperature, pres-sure, and each species mole number, the total differential of the Gibbs energy function can be written as G dG T

SdT Vdp Nd 0 or d sdT vdp the Gibbs-Duhem relation (1.3.15) One cannot vary T, pand independently. The Gibbs-Duhem relation gives the variation of one in terms of the variation of the other two. If Tis varied by dT, and pis varied by dp, then we cannot vary independent but d is determined by the Gibbs-Duhem relation.

entropy is additive :- variational problem for A(q) . Matrix of Inference Methods EP, variational EM, VB, NBP, Gibbs EP, EM, VB, NBP, Gibbs EKF, UKF, moment matching (ADF) Particle filter Other Loopy BP Gibbs Jtree sparse linear algebra Gaussian BP Kalman filter Loopy BP, mean field, structured variational, EP, graph-cuts Gibbs

Chemical Formulas and Equations continued How Are Chemical Formulas Used to Write Chemical Equations? Scientists use chemical equations to describe reac-tions. A chemical equation uses chemical symbols and formulas as a short way to show what happens in a chemical reaction. A chemical equation shows that atoms are only rearranged in a chemical .

Levenspiel (2004, p. iii) has given a concise and apt description of chemical reaction engineering (CRE): Chemical reaction engineering is that engineering activity concerned with the ex-ploitation of chemical reactions on a commercial scale. Its goal is the successful design and operation of chemical reactors, and probably more than any other ac-File Size: 344KBPage Count: 56Explore further(PDF) Chemical Reaction Engineering, 3rd Edition by Octave .www.academia.edu(PDF) Elements of Chemical Reaction Engineering Fifth .www.academia.eduIntroduction to Chemical Engineering: Chemical Reaction .ethz.chFundamentals of Chemical Reactor Theory1www.seas.ucla.eduRecommended to you b

(Right) Scatterplot of samples from 104 Gibbs sampling iterations. 2.1 Toy example Suppose we need to sample from the bivariate distribution with p.d.f. p(x;y) /e xy1(x;y2(0;c)) where c 0, and (0;c) denotes the (open) interval between 0 and c. (This example is due to Casella & George, 1992.) The Gibbs sampling approach is to alternately sample .

Andreas Wagner1, Wolfgang Wiedemann1, Thomas Wunderlich1 1 Chair of Geodesy, Faculty of Civil, Geo and Environmental Engineering, Technical University of Munich, Munich, Germany, a.wagner@tum.de .