Multiphase Transport Phenomena - Purdue · PDF file¾Macroscale multiphase flow...
Transcript of Multiphase Transport Phenomena - Purdue · PDF file¾Macroscale multiphase flow...
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Multiphase Transport Phenomena
C.T. MillerUniversity of North Carolina
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Approach
Interdisciplinary research and education challengesLearning theory and Zen on learning and confusionEngagementBuild on background
Connect to other lectures Some things classical and some things notFacilitate abstractionProvide for the needy
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Some Terminology
Scales: molecular, micro, macro, meso, and megaPhases: single-fluid phase, multiple fluid phase systemsFlow versus species transportContinuum scale modelingClosure, or constitutive, relationsForward versus inverse problems
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Overview
Modeling processConventional macroscale, or porous medium continuum scale, modeling approachMacroscale multiphase flowMacroscale multiphase flow and transport Multiscale modelingMicroscale modeling approachesExample applications
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Modeling Porous Medium Systems
Conceptual Model
Observations
Mathematical Formulation *{see types
Simulation Model
Parameter Estimation
Objective -model error -cost
Simulation
-may be stochastic
* Model Types: (1) Statistical (2) Empirical (3) Mechanistic
- PDE’s - ODE’s - DAE’s - AC’s
Stochastic Nature Uncertainty In: -model -parameters -auxiliary Conditions Leads to uncertainty in predictions
Parameter Estimation for: (1) Fitting model (2) Minimizing objective function
Model Use -prediction -design -policy
model parameters
y
CDF 1
P
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Mechanistic Modeling Framework
Closure Relations
Experimental Theoretical Computational
Conceptual Model
Conservation Equations
Mathematical Model
κ= f (pore geometry)P-S relationS-κr relation
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Conservation Equations
• Averaging procedures were alluded to as a means to develop and close the single-phase flow equation•Averaging procedures were also discussed as a means to develop a species transport equation
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Ponderables
What set of constraints can be developed with respect to the quantities that appear in the species conservation equation?Using these constraints, show how the flow equation can be derived from the species mass conservation equation
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Conservation Equations and Constraints
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Ponderables
For single-phase flow, what is the closure problem?Consider Darcy’s experiments and law and use as an alternative to computational or theoretical approaches to solve the closure problem and note all other assumptions usedDerive the single-phase flow model for the case in which porosity is constant and the fluid is incompressible, note the consequences, and assess if these are reasonable
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Conservation Equations and Constraints
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Darcy’s Law
Henry Darcy (1803-1858)
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Traditional Single-Phase Flow Model
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Microscale Multiphase Physics
Equilibrium state
θγ cos2R
pp wn =−
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Physics of Multiphase Porous Medium Systems
In a multiphase porous medium system, fluids move in response to viscous, capillary, and gravity forcesThis balance of forces is influenced by properties of the medium and the fluids: morphology of the pore space, contact angle, interfacial tensions, densities, and viscositiesThese forces result in very complex patterns of flow and entrapment of residual non-wetting phases can result
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Multiphase Flow and Species Transport
Multiphase flow---more than one fluid occupying the pore space
Water infiltrationShort time scale NAPL infiltrationPetroleum exploration
Multiphase flow and species transport---more than one fluid and species mass fractions or concentrations are important
Pesticide transportBTEX problems from petroleum spills
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DNAPL Behavior in Heterogeneous Porous Media
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Multiphase Flow Example
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Multiphase Conservation Equations
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Ponderables
Define the closure problem for two-phase flow in a macroscale porous medium systemHow might one investigate approaches to produce a closed model?What sorts of assumptions are implicit in traditional closure approaches?
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Closure Problem for Two-Phase FlowAssuming an immobile solid phase
For a two-fluid system, this results in five unknowns for each phase or a total of ten unknowns in two equations
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Capillary Pressure Saturation Relations
•C-109 sand experiment•Key features to note:
•Primary drainage•Entry pressure•Uniformity effects•Main imbibition•Non-wetting phase trapped•Wetting scanning curves•Hysteresis•Quasi-static experiments
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Examples of Common Closure Assumptions
Saturation is solely determined based upon capillary pressure and its history in a quasi-static senseDarcy’s law can be extended with modification to multiphase systemsRelative permeability is solely dependent upon the saturation of the respective phase and its historyRigorous connection with microscale quantities can be ignored
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Ponderables
Write a general form for a closed multiphase flow modelConsider an air-water system and write a closed model for this special case noting the reasoning steps used in the simplification
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Closed Multiphase Flow Model
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Example Closure Relations
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Air-Water System
Air is much more mobile than water, therefore pressure gradients must be small for the air phase--assume zeroPorosity is assumed constant, thus changes in water and air volume fractions are inversely relatedCommon multiphase extension of Darcy’s law appliesQuasi-static pressure-saturation-relative permeability relations applySpatial gradients of aqueous-phase density can be ignored
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Richards’ Equation
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Multiphase Flow and Transport
Often the problem of concernCommonality with single-phase systems that transport model requires solution of the flow model for closureCommonality with single-phase flow model as well for implications of reaction form on size and formal type of resultant system of conservation equations
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Ponderables
Formulate a model to describe the transport and fate of contaminants resulting from the spill of a refined petroleum product in the unsaturated zoneDescribe the flow modelWhat transport processes are of concern?Without simplifying assumptions, what is the size of the system of conservation equations?
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Ponderables
How can separation of time scales be used to simplify the system of equations?How can the number of species be reduced?What assumptions are used to support the notion of natural attenuation for this class of problem?
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Examples of Current Multiphase Research
Multiscale inspiredSingle-phase flowPressure-saturation relationsNAPL dissolution fingeringViscous coupling of fluidsMultiscale NAPL dissolutionThermodynamically constrained averaging theoryDNAPL remediation revisited
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Multiscale Porous Medium Systems
Pore scale
Lab scale Field scale
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Motivation for Pore-Scale Modeling
A predictive tool to determine constitutive relations for standard continuum-scale models
A significant means to close new continuum-scale theories for multiphase flow
An important way of understanding the fundamental pore-scale processes
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Single-Phase Flow
LB models
Pore-networkmodels
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Lattice-Boltzmann Method (LBM)
Simulate fluids as microscopic particles that move along a lattice and collide with each other
Fully recover Navier-Stokes equation
Relatively easy implementation of boundary condition on complex geometries
Suitable for massively parallel computers
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Lattice-Boltzmann Method
: density∑=i
if'ρ
ii
i efu rr ∑='ρ : momentum
[ ]),(),(1),()1,( )( txftxftxftexf ieq
iii i
rrrrr−=−++
τ
e1e2
e3
e4
e5
e6e8 e13
e9
e7
e14
e10 e11
e12
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Simulated Porous Media
1438010328Ns
0.3340.442φ
6.1924.250L(mm)
66%0.5%σ/
0.190.20<D> (mm)
RSP23RSP1
<D>
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Random-Size Sphere Packing
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Random-Size Sphere Pack
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LBM-Simulated Microscale Flow
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Simulation Results for κ
2)1(
3
180
22
φ
φκ
−=
DCK
5.56.5
22 φκ
DRG =
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Simulation Results for κ
⎥⎥⎥
⎦
⎤
⎢⎢⎢
⎣
⎡+= 4)(312
12βσβ
βφβκ
DD
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Non-Darcy Flow from LB Simulation
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Non-Darcy Flow
Onset of Non-Darcy flow
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Non-Darcy Flow
Forchheimer equation:
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Two-Phase Pressure Saturation Relations
•C-109 sand experiment•Key features to note:
•Primary drainage•Entry pressure•Uniformity effects•Main imbibition•Non-wetting phase trapped•Wetting scanning curves•Hysteresis•Quasi-static experiments
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Pore-Scale Modeling
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Experimental and Simulated Properties
9532------Number of Spheres
------Dyed PCE- waterNWP-WP
2.352.35Domain Length L (mm)
0.3560.356 ± 0.002Porosity φ0.01160.0121σD (mm)0.11490.1156<D> (mm)
Simulated GB1bGB1b
<D>: Arithmetic mean diameter
σD : Arithmetic standard deviation of grain diameter
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Calibration of LB Multiphase Model
Density ratio between fluidsViscosity ratioInterfacial tension (fluid - fluid interaction)Wettability (fluid - solid interaction)Boundary conditions
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Bubble Test
Initial state Equilibrium state
No solid phase
No body force
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Bubble at the Equilibrium State
Pressure profileInterfacial tension force profile
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θγ cos2R
pp wn =−
Test of Laplace's Law
Laplace's Law:
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Displacement Simulation
Non-wetting phase reservoir
Medium domain
Wetting phase reservoir
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Displacement Simulation
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Drainage and Imbibition Simulation
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Pore-Scale DNAPL Entrapment
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Micromodel TCE Residual
•Two-dimensional glass bead micromodel
•TCE dyed with Oil Red O
•Water saturated followed by DNAPL displacement and then water flushing
•TCE residual saturation results
•Large range of sizes of trapped TCE
•Largest features contain the majority of the TCE mass and are the most difficult to remove
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Pore-Scale Network Model of NAPL Entrapment
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Percolation Simulation: K Field
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Percolation Simulation of DNAPL
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Percolation Simulation of DNAPL
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Percolation Simulation of DNAPL
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Percolation Simulation of DNAPL
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Percolation Simulation of DNAPL
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Percolation Simulation of DNAPL
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Percolation Simulation of DNAPL
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Percolation Simulation of DNAPL
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Percolation Simulation of DNAPL
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Percolation Simulation of DNAPL
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NAPL Dissolution Tailing for TCE
•Column brought to residual saturation with TCE
•Water flusing in an attempt to obtain drinking water standard concentrations of TCE
•Large TCE residual feature determines clean-up time
•Eventually complex TCE region breaks up and drinking water standards reached
•Reference: Imhoff et al. [ES&T, 32(16), 1998]
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Mass Transfer Fundamentals
Linear model
Important dimensionless groupings
MassFlux ka C Cl na s= −( )
K kal l na=
ShK dD
v dD
l p
m
a a p
a
a
a m
= = =2
, Re , Sc , n
ρ
μμ
ρθ
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Experiment in 3-D Cell
Column: 9-cm dia. and 1.2-m long
= 2.2 m/day initial
= 0.14
NAPL - Dyed TCE
= 0.035 cmEffluent End
Influent End
Glass Tube
112 cmMedia
Va
Sn
d50
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1-D Experiments: Fingering
As the dissolution front moved downward through the medium, preferential flow paths developed.
Initial interface
6 cm 16 cm 19 cm
2.5 cm4.8 cm
t = 8 hours t = 22 hours t = 26 hours
PV = 6.2 PV =16.8 PV = 20
5.3 cm
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Dissolution Experiment Results
X-ray measurementsat t = 0 h
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X-ray measurementsat later times
Dissolution Experiment Results
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Dissolution Experiment: Simulated ResultsInitial Saturation t = 22 h
t = 44 h t = 66.5 h
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Dissolution Fingering Simulation
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DNAPLs in Homogeneous Systems
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DNAPLs in Heterogeneous Systems
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Residual NAPL distribution
2
Pore morphology and topology1
LB two-fuid phase simulation
Morphological analysis of pore space
Nonaqueous Phase Dissolution
e1
e2e3
e4
e5
e6e8 e13
e9
e7
e14
e10 e11
e12
3 NAPL dissolution
Pore-scale ADE solver with adaptive-stencil finite-volume scheme
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Nonaqueous Phase Dissolution
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Viscous Coupling
Relative permeability-saturation (ks) relation:
Viscous coupling effect
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Deficiencies in Traditional Models
Models are often based upon ill-defined variables and empirically derived closure approximations lacking in theoretical support and precise knowledge of limitationsEmpirical closure relations are routinely extended beyond their level of experimental support
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Deficiencies in Traditional Models
Rigorous linkages among scales is usually absentImportant phenomena are often not includednaturally in multiphase models (e.g., wettability) Standard porous medium models are not typically constrained to obey the second law of thermodynamics
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Deficiencies in Traditional Models
Quantities of interest, such as interfacial areas, do not explicitly arise in standard modelsStandard models are often built upon assumptions well-known to be violated(e.g. quasi-equilibrium states)
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Deficiencies in Traditional Models
Standard approaches lack a rigorous structure in which to examine simplifying assumptions
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TCAT Approach
Form general conservation equationsUse general conservation equations to formulate specific conservation equationsfor mass, momentum, angular momentum, energy, and entropySpecify thermodynamic dependence of internal energy and independent system variables
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TCAT Approach
Derive a total system entropy inequalityConstrain the entropy inequality with the product of Lagrange multipliers and specific conservation equations, thermodynamic relations, and other constraintsSolve for Lagrange multipliers to simplify entropy inequality
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TCAT Approach
Exploit entropy inequality to guide development of closure relationsUse sub-scale theory, computation, or experiment to guide final form of closure relationsCompare model systems to experimental observations and use to guide experimental design
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TCAT Approach for Single-Phase Flow
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TCAT---Entropy Balance
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TCAT---Conservation Equations
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TCAT---Averaged Thermodynamics
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TCAT---Entropy Inequality Forms
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TCAT---Simplified Entropy Inequality
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TCAT---Simplified Entropy Inequality
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TCAT---Model Closure
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Characteristics of Behavior
NAPLs leave a state of residual saturation in media through which they passNAPLs follow a complex pattern of flow, which is importantly influenced by media heterogeneityLNAPLs accumulate on the top of the water tableDNAPLs can sink below the waterNAPLs often reach stable configurations of locally high saturations known as poolsNAPLs are usually sparingly soluble and DNAPL contaminants usually degrade slowly---thus are long lived in the environment
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Two-Dimensional Unsaturated Downward Vertical Displacement of TCE
•21-cm x 21-cm two-dimensional cell
•Pooled TCE established
•TCE dyed with Oil Red O for visualization
•Established bottom brine layer
•Drained to unsaturated conditions
•0.3 pore-volume downward flush with mixture of sulfosuccinate surfantants
•Measured 80.0% TCE removal, no visible pools
•Reference: Hill et. al. [ES&T, 35(14), 2001]