Chemical Potential
8. Chemical Potential
The chemical potential drives mass (or species) transfer in
a manner similar to the thermal potential that drives heat transfer from higher to lower temperatures.
a. Multicomponent into Mul- ticomponent
Consider a vessel divided Figure 26. Heat transfer mechanism. into two sections C and D (as shown in Figure 27 ) that initially contains oxygen throughout, and in which charcoal is spread over the floor of section D. As- sume that as the charcoal is burned, sections C and D consist of two components: oxygen and
CO 2 . Further, consider a specific time at which the mole fraction of O 2 in section C (say, x O 2 = 80%) is larger compared to that in section D (say, X O2 = 30%).
Since molecules move randomly, for every 1000 molecules that migrate from C into
D through the section Y–Y, 1000 molecules will move from D into C. Consequently, 800 molecules of O 2 will move into D while only 300 molecules of this species will migrate to C from D, so that there is net transfer of 500 molecules of O 2 from section C into D. Simultane- ously, there is a net transfer of 500 molecules of CO 2 across the Y–Y plane from section D into
C. The oxygen transfer enables continued combustion of the charcoal. This mass transfer (or species transfer) due to random molecular motion is called diffusion. The chemical potential µ for ideal gases is related to the species concentrations
(hence, their mole fractions). A higher species mole fraction implies a higher chemical poten- tial for that species. For instance, the chemical potential of O 2 , µ O 2 is higher in section C com-
pared to D, thereby inducing oxygen transfer from C to D. If the charcoal is extinguished, CO 2 production (therefore, O 2 consumption) ceases, and eventually a state of species equilibrium is reached. At this state the chemical potential of each species or its concentration is uniform in the system.
b. Single Component into Multicomponent Consider the following scenario. A vessel is divided into two sections E and F by a porous membrane, as shown in Figure 28a . Section E initially contains a single component (denoted by o) at a lower pressure, and Section F contains a multicomponent gas mixture at the same temperature, but at double the pressure. Assume that the mole fraction of o molecules in section F is initially x o,F = 0.2, and that there are 50 molecules per unit volume contained in section E and 100 molecules per unit volume in section F. Further, assume the porosity of the membrane to be selective such that it allows only o molecules to be transferred through its pores (i.e., it is a semipermeable membrane). Assuming 200 molecules s –1 of o to migrate from
E into F, 400 molecules of all species will attempt to transfer into E from F due to the higher pressure in that section. However, the semipermeable membrane allows only o molecules to
CO 2 D
Figure 27: Illustration of species transfer. Oxygen mole-
cules are denoted by o and CO 2 molecules by x.
transfer from F, so that of these 400 only the 80 molecules of o move from F into E. Therefore, there is net flow equal to (200–80)=120 molecules s –1 from E into F. If the pressure in section
F is increased eightfold, molecules of species o can no longer be transferred into it, since of the 1600 molecules that now attempt to migrate every second, the membrane allows only the 320 which are of o to move into section E (cf. Figure 28b ). The net motion is 320 – 200 = 120 molecules s –1 into section E from F.
Therefore, by adjusting the pressure in section F, we can control the direction of spe- cies transfer, or prevent it altogether by maintaining chemical equilibrium. For example, if under these conditions, the pressure in section F is five times that in E, 1000 molecules s –1 at- tempt to migrate from F to E, but only 200 molecules s –1 of o actually do, balancing the trans- fer of the same amount from E to F. The chemical potential of species o becomes uniform across the membrane at this state. Altering the pressure from this condition will change the chemical potential. In general, the larger the pressure, the higher the chemical potential.
Parts
» COMPUTATIONAL MECHANICS and APPLIED ANALYSIS
» Explicit and Implicit Functions and Total Differentiation
» Exact (Perfect) and Inexact (Imperfect) Differentials
» Intermolecular Forces and Potential Energy
» Internal Energy, Temperature, Collision Number and Mean Free Path
» Vector or Cross Product r The area A due to a vector product
» First Law for a Closed System
» First Law For an Open System
» STATEMENTS OF THE SECOND LAW
» Cyclical Integral for a Reversible Heat Engine
» Irreversibility and Entropy of an Isolated System
» Degradation and Quality of Energy
» SINGLE–COMPONENT INCOMPRESSIBLE FLUIDS
» Evaluation of Entropy for a Control Volume
» Internally Reversible Work for an Open System
» MAXIMUM ENTROPY AND MINIMUM ENERGY
» Generalized Derivation for a Single Phase
» LaGrange Multiplier Method for Equilibrium
» Absolute and Relative Availability Under Interactions with Ambient
» Irreversibility or Lost Work
» Applications of the Availability Balance Equation
» Closed System (Non–Flow Systems)
» Heat Pumps and Refrigerators
» Work Producing and Consumption Devices
» Graphical Illustration of Lost, Isentropic, and Optimum Work
» Flow Processes or Heat Exchangers
» CLASSICAL RATIONALE FOR POSTULATORY APPROACH
» Generalized Legendre Transform
» Van der Waals (VW) Equation of State
» Other Two–Parameter Equations of State
» Compressibility Charts (Principle of Corresponding States)
» Boyle Temperature and Boyle Curves
» Three Parameter Equations of State
» Empirical Equations Of State
» State Equations for Liquids/Solids
» Internal Energy (du) Relation
» EXPERIMENTS TO MEASURE (u O – u)
» Vapor Pressure and the Clapeyron Equation
» Saturation Relations with Surface Tension Effects
» Temperature Change During Throttling
» Throttling in Closed Systems
» Procedure for Determining Thermodynamic Properties
» Euler and Gibbs–Duhem Equations
» Relationship Between Molal and Pure Properties
» Relations between Partial Molal and Pure Properties
» Mixing Rules for Equations of State
» Partial Molal Properties Using Mixture State Equations
» Ideal Solution and Raoult’s Law
» Completely Miscible Mixtures
» DEVIATIONS FROM RAOULT’S LAW
» Mathematical Criterion for Stability
» APPLICATION TO BOILING AND CONDENSATION
» Physical Processes and Stability
» Constant Temperature and Volume
» Equivalence Ratio, Stoichiometric Ratio
» Entropy, Gibbs Function, and Gibbs Function of Formation
» Entropy Generated During an Adiabatic Chemical Reaction
» MASS CONSERVATION AND MOLE BALANCE EQUATIONS
» Evaluation of Properties During an Irreversible Chemical Reaction
» Criteria in Terms of Chemical Force Potential
» Generalized Relation for the Chemical Potential
» Nonideal Mixtures and Solutions
» Gas, Liquid and Solid Mixtures
» Availability Balance Equation
Show more