1 DIFFUSIVE FLUX, HEAT & CONTAMINANT CONSERVATION Molecular diffusion is a process by which random molecular motion moves any quantity down the concentration.

Slides:



Advertisements
Similar presentations
Diffusion What is Engineering. What do these processes have in common? 1) Hydrogen embrittlement of pressure vessels in nuclear power plants 2) Flow of.
Advertisements

Mass Transport of Pollutants
Diffusion Mass Transfer
Atkins & de Paula: Atkins’ Physical Chemistry 9e
Control Volume & Fluxes. Eulerian and Lagrangian Formulations
Objectives Heat transfer Convection Radiation Fluid dynamics Review Bernoulli equation flow in pipes, ducts, pitot tube.
Continuity Equation. Continuity Equation Continuity Equation Net outflow in x direction.
Convection.
Introduction to Mass Transfer
Chapter 2: Properties of Fluids
Continuum Equation and Basic Equation of Water Flow in Soils January 28, 2002.
1 MECH 221 FLUID MECHANICS (Fall 06/07) Tutorial 6 FLUID KINETMATICS.
Transport Equations and Flux Laws Basic concepts and ideas 1.A concept model of Diffusion 2.The transient Diffusion Equation 3.Examples of Diffusion Fluxes.
Atkins’ Physical Chemistry Eighth Edition Chapter 21 – Lecture 2 Molecules in Motion Copyright © 2006 by Peter Atkins and Julio de Paula Peter Atkins Julio.
LES of Turbulent Flows: Lecture 3 (ME EN )
Chapter 4 Fluid Flow, Heat Transfer, and Mass Transfer:
Instructor: André Bakker
Introduction to Convection: Mass Transfer Chapter Six and Appendix E Sections 6.1 to 6.8 and E.4.
Diffusion Mass Transfer
© Fluent Inc. 8/10/2015G1 Fluids Review TRN Heat Transfer.
Flow and Thermal Considerations
St Venant Equations Reading: Sections 9.1 – 9.2.
Chilton and Colburn J-factor analogy
Bioseparation Dr. Kamal E. M. Elkahlout Chapter 3 Mass transfer.
Evaporation Slides prepared by Daene C. McKinney and Venkatesh Merwade
AME 513 Principles of Combustion Lecture 7 Conservation equations.
INTRODUCTION TO CONDUCTION
1 Fluid Models. 2 GasLiquid Fluids Computational Fluid Dynamics Airframe aerodynamics Propulsion systems Inlets / Nozzles Turbomachinery Combustion Ship.
Chapter 21: Molecules in motion
Conservation of mass If we imagine a volume of fluid in a basin, we can make a statement about the change in mass that might occur if we add or remove.
ME 254. Chapter I Integral Relations for a Control Volume An engineering science like fluid dynamics rests on foundations comprising both theory and experiment.
Chapter 21: Molecules in motion Diffusion: the migration of matter down a concentration gradient. Thermal conduction: the migration of energy down a temperature.
Mass Transfer Coefficient
FLUID PROPERTIES Independent variables SCALARS VECTORS TENSORS.
Equation of Continuity II. Summary of Equations of Change.
Aquatic Respiration The gas exchange mechanisms in aquatic environments.
19 Basics of Mass Transport
CONVECTIVE FLUX, FLUID MASS CONSERVATION
Analogies among Mass, Heat, and Momentum Transfer
Abj1 1.System, Surroundings, and Their Interaction 2.Classification of Systems: Identified Volume, Identified Mass, and Isolated System Questions of Interest:
Lecture 8 Control Volume & Fluxes. Eulerian and Lagrangian Formulations.
INTRODUCTION TO CONVECTION
CP502 Advanced Fluid Mechanics
Tutorial/HW Week #7 WRF Chapters 22-23; WWWR Chapters ID Chapter 14
1 CONSTITUTIVE RELATION FOR NEWTONIAN FLUID The Cauchy equation for momentum balance of a continuous, deformable medium combined with the condition of.
Flux of mass in (kg/s) = Flux of mass out (kg/s) = Net Flux of mass in ‘x’ = Net Flux of mass in ‘y’ = Net Flux of mass in ‘z’ =, u, w, v Mass per volume.
Extracellular fluid (outside) carbohydrate phospholipid cholesterol binding site phospholipid bilayer recognition protein receptor protein transport protein.
Basic concepts of heat transfer
Conservation of Tracers (Salt, Temperature) Chapter 4 – Knauss Chapter 5 – Talley et al.
Heat Transfer by Convection
Transport process In molecular transport processes in general we are concerned with the transfer or movement of a given property or entire by molecular.
Standards 3: Thermal Energy How Heat Moves  How heat energy transfers through solid.  By direct contact from HOT objects to COLD objects.
Movement in and out of cells. You need to learn this definition:  Diffusion is the net movement of molecules from a region of their higher concentration.
1 The total inflow rate of momentum into the control volume is thus MOMENTUM CONSERVATION: CAUCHY EQUATION Consider the illustrated control volume, which.
How were you able to smell the perfume?
Chapter 2: Introduction to Conduction
MODUL KE SATU TEKNIK MESIN FAKULTAS TEKNOLOGI INDUSTRI
General form of conservation equations
Diffusion Mass Transfer
Fluid Models.
Dimensional Analysis in Mass Transfer
States of Matter Standard: Students know that in solids, the atoms are closely locked in position and can only vibrate. In liquids the atoms and molecules.
Heat Transfer Coefficient
FLUID MECHANICS REVIEW
Solutions, and Movement of Molecules Therein
Chapter 21: Molecules in motion
Chapter 2 The Chemistry of Life.
Basic concepts of heat transfer: Heat Conduction
Movement in and out of cells
3rd Lecture : Integral Equations
Presentation transcript:

1 DIFFUSIVE FLUX, HEAT & CONTAMINANT CONSERVATION Molecular diffusion is a process by which random molecular motion moves any quantity down the concentration gradient, i.e. from high concentration to low concentration. Diffusion does not require flow, but it operates in the presence of flow. Consider the illustrated container of water. A dilute concentration of dye (molecules) is placed in the lower half of the container. In time, molecular action cause the dye-free fluid to mix with the dye- laden fluid, so that the concentration eventually becomes uniform.

2 Molecular diffusion is a process by which random molecular motion moves any quantity down the concentration gradient, i.e. from high concentration to low concentration. Diffusion does not require flow, but it operates in the presence of flow. Consider the illustrated container of water. A dilute concentration of dye (molecules) is placed in the lower half of the container. In time, molecular action cause the dye-free fluid to mix with the dye- laden fluid, so that the concentration eventually becomes uniform. DIFFUSIVE FLUX, HEAT & CONTAMINANT CONSERVATION

3 Molecular diffusion is a process by which random molecular motion moves any quantity down the concentration gradient, i.e. from high concentration to low concentration. Diffusion does not require flow, but it operates in the presence of flow. Consider the illustrated container of water. A dilute concentration of dye (molecules) is placed in the lower half of the container. In time, molecular action cause the dye-free fluid to mix with the dye- laden fluid, so that the concentration eventually becomes uniform. DIFFUSIVE FLUX, HEAT & CONTAMINANT CONSERVATION

4 Molecular diffusion is a process by which random molecular motion moves any quantity down the concentration gradient, i.e. from high concentration to low concentration. Diffusion does not require flow, but it operates in the presence of flow. Consider the illustrated container of water. A dilute concentration of dye (molecules) is placed in the lower half of the container. In time, molecular action cause the dye-free fluid to mix with the dye- laden fluid, so that the concentration eventually becomes uniform. DIFFUSIVE FLUX, HEAT & CONTAMINANT CONSERVATION

5 In the case below the dye is diffusing in the x 3 direction. Let c denote the concentration of dye. Note that c is a decreasing function of x 3, so that The diffusive flux of dye in the vertical direction is from high concentration to low concentration, which happens to be upward in this case. The simplest assumption we can make for diffusion is the linear Fickian form: where F D,con,3 denotes the diffusive flux of contaminant (in this case dye) in the x 3 direction, c x3x3 where D c denotes the kinematic molecular diffusivity of the contaminant. F D,con,3 DIFFUSIVE FLUX, HEAT & CONTAMINANT CONSERVATION

6 The units of c are quantity/volume. For example, in the case of dissolved salt this would be kg/m 3, and in the case of heat it would be joules/m 3. The units of D c are thus These units happen to be the same as those of the kinematic viscosity of the fluid, i.e.. c x3x3 In the case of heat, D c is denoted as D h and F D,con,3 is denoted as F D,heat, 3. F D,con,3 The units of F D,con,3 should be quantity (crossing)/face area/time. In the case of dissolved salt, this would be kg/m 2 /s, and in the case of heat it would be joules/m 2 /s. DIFFUSIVE FLUX, HEAT & CONTAMINANT CONSERVATION

7 The 3D generalization of the Fickian forms for diffusivity are where c is the concentration of the contaminant (quantity/volume). The concentration of heat per unit volume (Joules/m 3 ) is given as  c p . Thus where k =  c p D h denotes the thermal conductivity. The dimensionless Prandtl number Pr and Schmidt number Sc are defined as This comparison is particularly useful because we will later identify the kinematic viscosity with the kinematic diffusivity of momentum. DIFFUSIVE FLUX, HEAT & CONTAMINANT CONSERVATION

8 Some numbers for heat Heat in air kg/m 3 J/kg/  K N s/m 2 m 2 /s J/s/m/  K m 2 /s CC KK  cpcp  kDhDh Pr E E E E E E E E E E E E E E E E E E E E E E E E-01 Heat in water kg/m 3 J/kg/  K N s/m 2 m 2 /s J/s/m/  K m 2 /s CC KK  cpcp  kDhDh Pr E E E E E E E E E E E E E E E E E E E E E E E E E E E E+00 In the above relations  denotes the dynamic viscosity of water. DIFFUSIVE FLUX, HEAT & CONTAMINANT CONSERVATION

9 Some values of D c and D h are given as follows. gases and vapors in air at 25  C = 1.54e-5 m 2 /s m 2 /s substanceDcDc Sc H2H2 7.12E CO E Ethyl alcohol1.19E Benzene8.80E dissolved solutes in water at 20  C = 1.004e-6 m 2 /s m 2 /s substanceDcDc Sc H2H2 5.13E E+02 O2O2 1.80E E+02 CO E E+02 N2N2 1.64E E+02 NaCl1.35E E+02 Glycerol7.20E E+03 Sucrose4.50E E+03 DIFFUSIVE FLUX, HEAT & CONTAMINANT CONSERVATION

10 Consider a control volume that is fixed in space, through which fluid can freely flow in and out. In words, the equation of conservation of contaminant is:  /  t(quantity of contaminant in control volume) = net inflow rate of contaminant in control volume + Net rate of production of contaminant in control volume Contaminant concentration is denoted as c (quantity/volume). Contaminant can be produced internally by e.g. a chemical reaction (that produces heat or some some species of molecule). Let S denote the rate of production of contaminant per unit volume per unit time (quantity/m 3 /s). Where S is negative it represents a sink (loss rate) rather then source (gain rate) of contaminant. The net inflow rate includes both convective and diffusive flux terms. Translating words into an equation, dA nini DIFFUSIVE FLUX, HEAT & CONTAMINANT CONSERVATION

11 But by the divergence theorem Thus the conservation equation becomes or since the volume is arbitrary, DIFFUSIVE FLUX, HEAT & CONTAMINANT CONSERVATION

12 Now So the conservation equation reduces to a convection-diffusion equation with a source term: If the fluid is incompressible, i.e.  u i /  x i = 0, the relation reduces to DIFFUSIVE FLUX, HEAT & CONTAMINANT CONSERVATION

13 Special case of heat, for which c   c p  and D c  D h, S  S h or thus DIFFUSIVE FLUX, HEAT & CONTAMINANT CONSERVATION