Project 1. Proposal. Describe the problem you propose to analyze. Include Background: describe the problem you intend to analyze, give motivation for.

Slides:



Advertisements
Similar presentations
Mineral Surfaces Minerals which are precipitated can also interact with other molecules and ions at the surface Attraction between a particular mineral.
Advertisements

Subsurface Fate and Transport of Contaminants
Lecture 15: Capillary motion
Adsorptive Desulfurization of Liquid Hydrocarbons: Langmuir Adsorption modeling using COMSOL Ram EGEE 520 Spring 2007.
Carbon Deposition in Heterogeneous Catalysis
Dongxiao Zhang Mewbourne School of Petroleum and Geological Engineering The University of Oklahoma “Probability and Materials: from Nano- to Macro-Scale”
A modified Lagrangian-volumes method to simulate nonlinearly and kinetically adsorbing solute transport in heterogeneous media J.-R. de Dreuzy, Ph. Davy,
Gas/Particle Partitioning. Why is gas/particle partitioning important? Dispersion of Pollutants Introduced into the Atmosphere as Determined by Residence.
ERT 313/4 BIOSEPARATION ENGINEERING MASS TRANSFER & ITS APPLICATIONS
Ground-Water Flow and Solute Transport for the PHAST Simulator Ken Kipp and David Parkhurst.
INTRODUCTION TO CATALYSIS –KINETICS OF CATALYTIC REACTIONS CH
1 Soil Vapor Extraction Limitations and Enhancements LeeAnn Racz AgE 558 Semester Project April 2001.
Numerical Porous Media KAUST SRI Center Modeling and simulation of multiscale problems N Ahmed, VM Calo, Y Efendiev, H Fayed, O Iliev, Z.Lakdawala, K.Leonard,
Conservative and Reactive Solutes Conservative do not react with soil / groundwater Chloride is a good example Sorbed onto mineral grains as well as organic.
REVIEW. What processes are represented in the governing equation that we use to represent solute transport through porous media? Advection, dispersion,
Reactors . ä Reactor: a “container” where a reaction occurs ä Examples: ä Clear well at water treatment plant (chlorine contact) ä Activated sludge tank.
Monroe L. Weber-Shirk S chool of Civil and Environmental Engineering Partitioning of Volatile Organic Carbon Compoundss.
Interdisciplinary Modeling of Aquatic Ecosystems Curriculum Development Workshop July 18, 2005 Groundwater Flow and Transport Modeling Greg Pohll Division.
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.
Solutions to the Advection-Dispersion Equation
Partitioning of VOCs: Why do we care? ä Determines how best to treat a site ä vapor extraction ä pump and treat ä remove contaminated soil ä Determines.
Diffusion Mass Transfer
BIOPLUME II Introduction to Solution Methods and Model Mechanics.
Solute (and Suspension) Transport in Porous Media
Slides courtesy of Prof M L Kraft, Chemical & Biomolecular Engr Dept, University of Illinois at Urbana-Champaign. L21-1 Review: Heterogeneous Catalyst.
Clean water Start and end times of two reaction intervals Specify domain’s starting fluid composition on the Initial pane.
Diffusional Limitation in Immobilized Enzyme System Immobilized enzyme system normally includes - insoluble immobilized enzyme - soluble substrate, or.
Contaminant Transport CIVE 7332 Lecture 3. Transport Processes Advection The process by which solutes are transported by the bulk of motion of the flowing.
Mass Transfer Coefficient
Variably Saturated Flow and Transport: Sorbing Solute.
Review: Steps in a Heterogeneous Catalytic Reaction
Upscaling of Transport Processes in Porous Media with Biofilms in Non-Equilibrium Conditions L. Orgogozo 1, F. Golfier 1, M.A. Buès 1, B. Wood 2, M. Quintard.
Sept 2007Wetland Pollutant Dynamics and Control 1 ARTIFICIAL WETLAND MODELLING FOR PESTICIDES FATE AND TRANSPORT USING A 2D MIXED HYBRID FINITE.
Advection-Dispersion Equation (ADE)
Cement waste matrix evaluation and modelling of the long-term stability of cementitious waste matrices.
19 Basics of Mass Transport
Working With Simple Models to Predict Contaminant Migration Matt Small U.S. EPA, Region 9, Underground Storage Tanks Program Office.
Urban Water Global water aspects
CE 3354 Engineering Hydrology Lecture 21: Groundwater Hydrology Concepts – Part 1 1.
(Z&B) Steps in Transport Modeling Calibration step (calibrate flow & transport model) Adjust parameter values Design conceptual model Assess uncertainty.
Heat Transfer Su Yongkang School of Mechanical Engineering # 1 HEAT TRANSFER CHAPTER 6 Introduction to convection.
CONVECTION : An Activity at Solid Boundary P M V Subbarao Associate Professor Mechanical Engineering Department IIT Delhi Identify and Compute Gradients.
Solute transport in sediments Physical properties Transport: Diffusion “Irrigation” Advection.
Environmental Engineering Lecture Note Week 10 (Transport Processes) Joonhong Park Yonsei CEE Department CEE3330 Y2013 WEEK3.
Clemson Hydro Heat Transport Temperature of a wolf pup.
Heat Transport Temperature of a wolf pup.
Hemant Kumar EGEE /28/2009 DEPARTMENT OF ENERGY AND MINERAL ENGINEERING COLLEGE OF EARTH AND MINERAL SCIENCES.
CONTAMINANT TRANSPORT MECHANISMS
Clemson Hydro Project Describing Methods. Clemson Hydro Reactive Transport Silver dichromate forming Leisegang rings in a test tube experiment
Reactor analysis (Mass balances, Flow models, Reactors)
Clemson Hydro Diffusion Mass transfer in the absence of.
Diffusion Mass transfer in the absence of fluid motion
Heat Transport Temperature of a wolf pup.
Project Describing Methods.
Specify kinetic rate laws for mineral precipitation and dissolution (and other reaction types) on the Reactants pane. Use Arrhenius equation to calculate.
Project 1. Proposal. Describe the problem you propose to analyze. Include Background: describe the problem you intend to analyze, give motivation for.
Advanced Contaminant-Transport Techniques
Diffusion Mass Transfer
A First Course on Kinetics and Reaction Engineering
A First Course on Kinetics and Reaction Engineering
Impact of Flowing Formation Water on Residual CO2 Saturations
Advection-Dispersion Equation (ADE)
Modeling and experimental study of coupled porous/channel flow
Contaminant Transport Equations
Steps in a Heterogeneous Catalytic Reaction
Specify domain’s starting fluid composition on the Initial pane
in Fixed-bed Tubular Reactor
React traces reaction paths involving fluids, minerals, gases, and microbes.
Heat Transfer Coefficient
Review: Steps in a Heterogeneous Catalytic Reaction
Presentation transcript:

Project 1. Proposal. Describe the problem you propose to analyze. Include Background: describe the problem you intend to analyze, give motivation for doing the analysis, cite literature. Objective: Describe what you intend to achieve as a result of doing the simulation Method: Describe the analysis you will conduct. This should include a description of the mathematical problem, including governing equation, boundary and initial conditions, parameters, and geometry. Verification: Describe existing analyses you would use to verify your results. This could be an analytical solution or existing numerical solution. Validation or calibration: Describe data that you would use to calibrate your simulation. Identify the approach you would use for calibration. Approach: Outline 3-5 analyses of increasing complexity that ends with the final goal. Results: Describe the results you expect to get from the analyses. References: Identify and cite at least 3 papers

Transport with Fluid-Solid Reactions Ion exchange resin Gas chromatograph Mineralized vein http://www.insilico.hu/liesegang/index.html

Reaction Locations Bulk Material (homogeneous rxn) Fluid—Multi-scale mixing Solid– Diffusion dominant Interfaces (heterogeneous rxn) Fluid-Solid—No flow at interfacediffusion Liquid-Gas

Conceptual Model Cf fluid solid Cs

Concentrations In water: In soil: On surfaces:

Processes Sorption: bonding, but similar species as aqueous Precipitation: change species Clogging: significant thickness Dissolution: remove solid Biofilm: growth of filmreactions, clogging Matrix diffusion: species into matrix, store/react

Reaction Rates Fast relative to transport Equilibrium Partitioning between fluid/solid Cs = f(Cf) Similar or slower than transport Disequilibrium, kinetics important Reaction time scale: 1/k1 Diffusion time scale: L2/D Advection time scale: L/v

Sorption Isotherms https://www.soils.org/publications/sssaj/articles/67/4/1140

Equilibrium Sorption Slope = Distribution Coefficient, Kd Concentration sorbed (mass/mass) Concentration in water Slope = Distribution Coefficient, Kd Good for low concentrations Linear Isotherm Sorption sites fill at high concentrations Examples Concentration sorbed (mass/mass) Non- linear Isotherm High concentrations Concentration in water

Equilibrium Partitioning Important Concept, FluidSolid Surface Porous media, Two overlapping domains Equilibrium Partitioning Fluid concentration, Cf[Ms/Lf3] Solid surface concentration, Cs[Ms/Mso] Fluid conc Solid conc

Effects of Equilibrium Sorption on Transport of a Plume Breakthrough curves Source as mass flux over a circular area Chromatographic eff

Application of pulse test to determine ne and R Average linear flow velocity v=L/tm,w tm=9215 s (from first moment, conservative tracer) L=300m (from set up) v=300m/9215 s =0.032 m/s Effective porosity Flux = q =0.01 m/s (specified in model) Effective porosity =q/v = 0.01/0.032 = 0.31 Compare to porosity specified in model=0.3 Retardation factor vc=L/tm,c tm=20700 s (from first moment sorbing compound) v=300m/20700 s =0.014 m/s L R=vw/vc= 0.032/0.014=2.3 Chromatographic effect

Rate of change due to sorption

Advection-Dispersion w/ surface reaction Governing Equation Advection-Dispersion w/ surface reaction c = Cn Storage Advective Flux Diffusive Flux (Fick’s Law) Dispersive Flux Source Governing

Governing Eq. AD w/Equilibrium Sorption, Linear Isotherm Retardation factor

Governing Eq. AD w/Equilibrium Sorption, Langmuir Isotherm Retardation factor

Governing Eq. AD w/Equilibrium Sorption, Linear Isotherm Comsol format For Reference Retardation factor

Nonequilibrium (Kinetic) Sorption Macroscopic, Two adjacent domains Cf Fluid concentration, Cf ,[mol/m3] Solid surface concentration, Cs , [mol/m2] kads: sorption rate constant [1/(m s)] kdes: desorption rate constant [1/s] Transport bulk fluid solid = Solid rxn rate Fluid solid Cs Cf 1st order sorption kinetics reversible Mass flux boundary condition on fluid Jboundary Cs

Nonequilibrium Sorption Kinetics http://www.sciencedirect.com/science/article/pii/S0883292706002629#

Non-equilibrium Sorption Pore-scale Cf Specify rate of change of Cs Fluid solid First-order irreversible kinetics First-order reversible Cs Solid Fluid

Important Concept, FluidSolid Surface Porous media, Two overlapping domains Dual Porosity, Dual Permeability Two domains (fractures, matrix) (fluid, solid) (liquid, gas) Usually contrasting k Mass transfer between domains

Example First-order non-equilib sorption Reversible and irreversible Breakthrough curves water Cwater solid Non-reversible water reversible Left behind on solid

Advection-Dispersion w/ surface reaction Governing Equation Advection-Dispersion w/ surface reaction Dual Porosity Approach, with concentrations in both domains Advection Diffusion only

Clogging of a flow channel from precipitation on wall Non-equilibrium sorption Pipes clogged with precipitate Cementation of pore space biofilm Plaque clogging artery Biofilm

Biofilm Conceptual Model Growth/decay of biomass uptake of nutrients, increase in thickness decay, decrease in thickness 3D geometry on surface interaction with flow fluid sheardetachment Mass transfer to biofilm transport through fluid mass transfer through stagnant water layer mass transfer within biofilm Reactions within biofilm first-order, monod, growth/death other vary within biofilm http://www.bti.umn.edu/bond/bond_lab___university_of_minnesota.html http://wyss.harvard.edu/viewmedia/133/bacterial-biofilm-1;jsessionid=6F46332D65A9586919824B047248B4E0.wyss2

Clogging and Channeling Fluid concentration, Cf ,[mol/m3] Solid surface concentration, Cs , [mol/m2] Solid concentration, Cs , [Ms/Mos] Macroscopic model REV Model Cf Fluid solid Cs [ 𝐿 𝑐 𝑇 ]velocity of interface (moving mesh). Use to calc rate of change in porosity Use porosity change to get k change

Clogging of flow channel from precipitation Non-equilibrium sorption Cf: fluid concentration [mol/m3] Cs: concentration on solid [mol/m2] kads: sorption rate constant [m/s] kerode: erosion rate constant[mol/m2] tw: wall shear rate[1/s] tw: critical wall shear stress for erosion[1/s] w: thickness of layer along wall [m] Mvol: Molar volume [m3/mol] Cf Fluid solid w Cs Reaction Flux out of fluid Movement of wall Cf Jboundary w Cs

Example Physics Geometry (mm) No flow 0.001m/s P=0 Fluid No flow Transport In water Surface reaction No flow No flux Cf=1 Outflow No diffusive flux Flux out = -rxn Physics Laminar flow Viscosity = f(C_m) Transport, rxn C_substrate C_microbe population non-reactive | reactive

Biofilm growth and clogging https://vimeo.com/65554224 Baseline, fluid shear has no effect Less sensitive to shear More sensitive to shear https://vimeo.com/65554293 https://vimeo.com/65554294

Strategy Geometry, definitions, physics Flow Flow+transport Flow+transport+surface rxn Flow+transport+surface rxn+deformed mesh

concentration non-reactive | reactive

http://ac. els-cdn. com/S0008622304002155/1-s2 http://ac.els-cdn.com/S0008622304002155/1-s2.0-S0008622304002155-main.pdf?_tid=2c787188-8be7-11e2-b17d-00000aab0f02&acdnat=1363183759_8cfe4ddd81d00a9db89666573888753f