BIOPLUME II Introduction to Solution Methods and Model Mechanics - PowerPoint PPT Presentation

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BIOPLUME II Introduction to Solution Methods and Model Mechanics

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First order decay. Instantaneous Biodegradation. Particle Movement. Limitations/Assumptions ... RADIOACTIVE DECAY. THALF - Half life of solute ... – PowerPoint PPT presentation

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Title: BIOPLUME II Introduction to Solution Methods and Model Mechanics


1
BIOPLUME IIIntroduction to Solution Methods and
Model Mechanics
2
What does it do?
  • Two dimensional finite difference model for
    simulating natural attenuation due to
  • advection
  • dispersion
  • sorption
  • biodegradation

3
How Does BPIII Solve Equations?
  • Contaminant transport solved using the Method of
    Characteristics
  • Particles travel along Characteristic lines
    determined by flow solution.
  • Particles carry mass
  • Advection solved via particle movement
  • Dispersion solved explicitly
  • Reaction solved explicitly
  • First order decay
  • Instantaneous Biodegradation

4
Particle Movement
5
Limitations/Assumptions
  • Darcys Law is valid
  • Porosity and hydraulic conductivity constant in
    time, porosity constant in space
  • Fluid density, viscosity and temperature have no
    effect on flow velocity
  • Reactions do not affect fluid or aquifer
    properties
  • Ionic and molecular diffusion negligible
  • Vertical variations in head/concentration
    negligible
  • Homogeneous, isotropic longitudinal and
    transverse dispersivity

6
Limitations of Biodegradation
  • No selective or competitive biodegradation of
    hydrocarbons (lumped hydrocarbons)
  • Conceptual model of biodegradation is a
    simplification of the complex biologically
    mediated redox reactions that occur in the
    subsurface

7
BIOPLUME II Flowchart
8
HOW TO SET UP A MODEL
  • 1. Data Collection Analysis
  • 2. Modeling Scale
  • 3. Discretization
  • 4. Boundary Conditions
  • 5. Parameter Estimation
  • 6. Calibration
  • 7. Sensitivity Analysis
  • 8. Error Estimation
  • 9. Prediction

9
SOURCE DATA
  • Mass of contaminant
  • Q, C0
  • Discrete vs. Continuous
  • Nature of contaminant
  • Chemical stability
  • Biological stability
  • Adsorption

10
PARAMETER ESTIMATION
  • 1. Porosity
  • 2. Dispersivity
  • 3. Storage coefficients
  • 4. Hydraulic conductivity
  • 5. Thickness of unit
  • 6. Recharge rates

11
REGIONAL SCALE - QUANTITATIVE
  • Aquifer characteristics
  • Background gradients
  • Geology
  • Recharge sources

12
LOCAL SCALE - WATER QUALITY
  • Site history
  • Site characterization
  • Source definition
  • Nature of contamination
  • Plume delineation

13
(No Transcript)
14
MOC TIMING PARAMETERS
  • Total Simulation Time
  • 1st pumping period
    2nd
  • NPMP 2
  • For Each Pumping Period
  • PINT pumping period in yrs
  • NTIM of time steps in pumping period

15
MOC BOUNDARY CONDITIONS
  • Two types
  • Constant Head
  • Water Table constant
  • Constant Flux
  • Flow rate Q
  • Concentration C0

16
MOC BOUNDARY CONDITIONSSpecifications of NCODES
  • For Each Code in NOEID map
  • LEAKANCE (s-1)
  • vertical hyd. conduct. / thickness
  • CONCENTRATION OF CONTAMINANT
  • RECHARGE RATE (ft/s)
  • NOTE
  • For constant head cells set LEAKANCE to 1.0

17
MOC SOURCE DEFINITION
  • Injection well
  • Flow rate - Q
  • Concentration - C0
  • Constant Head Cell
  • CC0
  • Recharge Cell
  • Flow rate - Q
  • Concentration - C0

18
PHYSICAL AQUIFER CHARACTERISTICS
  • 1. Transmissivity (ft2/s) VPRM
  • 2. Thickness (ft) THCK
  • 3. Dispersivity (ft)
  • Longitudinal BETA
  • Ratio DLTRAT Txx/Tyy
  • 4. Porosity POROS
  • 5. Storativity S
  • NOTE
  • For transient problems
  • TIMX increment multiplier
  • TINIT size of initial time step

19
MOC REACTION PARAMETERS
  • NREACT
  • Flag to instruct MOC to expect reaction data
  • 0 - no reactions
  • 1 - reactions taking place
  • expect card 4 free format
  • Two types of reaction
  • RETARDATION
  • KD - Distribution coefficient
  • RHOB - Bulk density
  • RADIOACTIVE DECAY
  • THALF - Half life of solute

20
INPUT PARAMETERS AFFECTING ACCURACY FOR HYDRAULIC
CALCULATIONS
  • ITMAX
  • Maximum allowable number of iterations 100-200
  • Increase ITMAX if hydraulic mass balance error is
    gt 1
  • NITP
  • Number of iteration parameters
  • USE 7
  • TOL
  • Convergence criteria lt0.01
  • Decrease TOL to get less hydraulic mass balance
    error

21
PARAMETERS AFFECTING ACCURACY OF TRANSPORT
  • NPTPND - Number of particles in a cell
  • NPMAX - Maximum number of particles
  • NX NY NPTPND

22
STABILITY CRITERIA FOR MOC
  • MOC may require dividing NTIM or PINT into
    smaller move time steps
  • ?t minimum of
  • Dispersion
  • Mixing
  • Advection

23
INPUT PARAMETERS AFFECTING STABILITY OF MOC
  • CELDIS - max distance per move
  • If CELDIS lt space between particles MOC will
    oscillate for N yrs BUT gives smallest Mass
    Balance errors for TgtN
  • If CELDIS Stability Criteria DO a sensitivity
    analysis on CELDIS
  • NPTPND - initial of particles
  • Accuracy of MOC directly proportional to NPTPND
  • Runtime inversely proportional to NPTPND
  • RULE OF THUMB
  • Initially set NPTPND4 or 5 and CELDIS0.75 or 1
  • For final runs use NPTPND9 and CELDIS0.5

24
Output control
  • NPNTMV
  • Number of particle moves after which output is
    requested. Use 0 to print at end of time steps
  • NPNTVL
  • Printing velocities
  • 0 - do not print
  • 1 - print for first time step
  • 2 - print for all time steps

25
Output control (cont.)
  • NPNTD
  • Print dispersion equation coefficients
  • NPDELC
  • Print changes in concentration
  • NPNCHV
  • Do not use this option. Always set to 0. It is
    used to request cards to be punched.
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