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Problem Set 2 is based on a problem in the MT3D manual; also discussed in Z&B, p. 228-231. 2D steady state flow in a confined aquifer We want to predict the breakthrough curve at the pumping well. The transport problem is transient.

Problem Set 2 is based on a problem in the MT3D manual; also discussed in Z&B, p. 228-231

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Problem Set 2 is based on a problem in the MT3D manual; also discussed in Z&B, p. 228-231. 2D steady state flow in a confined aquifer. We want to predict the breakthrough curve at the pumping well. The transport problem is transient. Zone of low hydraulic conductivity. - PowerPoint PPT Presentation

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Page 1: Problem Set 2  is based on a problem in the MT3D manual;  also discussed in Z&B, p. 228-231

Problem Set 2 is basedon a problem in the MT3Dmanual; also discussed inZ&B, p. 228-231.

2D steady state flow in a confined aquifer

We want to predict thebreakthrough curve at thepumping well. The transportproblem is transient.

Page 2: Problem Set 2  is based on a problem in the MT3D manual;  also discussed in Z&B, p. 228-231

Peclet numbers = 5 and 25

Zone of lowhydraulic conductivity

Page 3: Problem Set 2  is based on a problem in the MT3D manual;  also discussed in Z&B, p. 228-231

GWV screen

Note: the heterogeneityis not present in the firstcolumn

Page 4: Problem Set 2  is based on a problem in the MT3D manual;  also discussed in Z&B, p. 228-231

Units in MT3D – see p. 6-8 in the manual

Recommended: use ppm= mg/l gm/m3

That is, use meters; mass is reported in grams.

Mass = c Q t

Concentration units do not have to be consistent with the unitsused for other parameters. It is permissible, for example,to use “ft” for the system parameters and mg/l for concentration.

However, in that case the units calculated in the mass balancewill have inconsistent units and the mass balance numbers willneed to be manually corrected.

Page 5: Problem Set 2  is based on a problem in the MT3D manual;  also discussed in Z&B, p. 228-231

Cs = 57.87 ppm Cs = 0

Page 6: Problem Set 2  is based on a problem in the MT3D manual;  also discussed in Z&B, p. 228-231

0.00

0.20

0.40

0.60

0.80

1.00

1.20

0.00 0.20 0.40 0.60 0.80 1.00 1.20

Time (years)

Con

cent

ratio

n

TVD

HMOC

Upstream weighting

Central FD

Upstream FD

Central FD

TVD

NOTE. These results were produced using an old version of MT3DMS.Please run again with the latest version of the code.

Page 7: Problem Set 2  is based on a problem in the MT3D manual;  also discussed in Z&B, p. 228-231

MT3DMS Solution Options

1

2

3

4

PS#2

Page 8: Problem Set 2  is based on a problem in the MT3D manual;  also discussed in Z&B, p. 228-231

Central Difference Solution

Time step multiplier = 141 time steps

Time step multiplier = 1.213 time steps

Page 9: Problem Set 2  is based on a problem in the MT3D manual;  also discussed in Z&B, p. 228-231

See information on solution methodologies underthe MT3DMS tab on the course homepage for moreabout these parameters.

Courant number

Page 10: Problem Set 2  is based on a problem in the MT3D manual;  also discussed in Z&B, p. 228-231

Boundary Conditions

---for flow problem---for transport problem

Page 11: Problem Set 2  is based on a problem in the MT3D manual;  also discussed in Z&B, p. 228-231

Head solution--Flow problem issteady state

Page 12: Problem Set 2  is based on a problem in the MT3D manual;  also discussed in Z&B, p. 228-231

Transport Problem

Page 13: Problem Set 2  is based on a problem in the MT3D manual;  also discussed in Z&B, p. 228-231

Need to designatethese boundarycells as inactiveconcentration cells.Use zone 10 inthe diffusionsproperties menu ofGroundwater Vistas.

Page 14: Problem Set 2  is based on a problem in the MT3D manual;  also discussed in Z&B, p. 228-231

Cells in first row are in zone 10in the diffusion properties menu

This is necessary to prevent loss ofmass through the boundary by diffusion.

Page 15: Problem Set 2  is based on a problem in the MT3D manual;  also discussed in Z&B, p. 228-231

Solution at t=1 year

Page 16: Problem Set 2  is based on a problem in the MT3D manual;  also discussed in Z&B, p. 228-231

Mass Balance Considerations in MT3DMS

Sources of mass balance information:*.out file*.mas filemass balance summary in GW Vistas

See supplemental information for PS#2 postedon the course homepage for more information onmass balance options.

Page 17: Problem Set 2  is based on a problem in the MT3D manual;  also discussed in Z&B, p. 228-231

Mass Balance states that:Mass IN = Mass OUTwhere changes in mass storageare considered either as contributionsto mass IN or to mass OUT.

Water Flow:IN= through upper boundary; injection wellOUT= pumping well; lower boundary

Mass Flux:IN= through injection well; changes in storageOUT= pumping well; lower boundary; changes in storage

wells

IN - OUT = S where S = 0 at steady state conditions

Page 18: Problem Set 2  is based on a problem in the MT3D manual;  also discussed in Z&B, p. 228-231

From the *.out file (TVD solution)

Page 19: Problem Set 2  is based on a problem in the MT3D manual;  also discussed in Z&B, p. 228-231
Page 20: Problem Set 2  is based on a problem in the MT3D manual;  also discussed in Z&B, p. 228-231

Mass Storage: Water

Consider a cell in the model

IN - OUT = S where change in storage isS = S(t2) – S(t1)

If IN > OUT, the water level rises andthere is an increase in mass of water in the cell.IN = OUT + S, where S is positive.Note that S is on the OUT side of the equation.

If OUT > ININ – S = OUT, where S is negativeS is on the IN side of the equation.

Page 21: Problem Set 2  is based on a problem in the MT3D manual;  also discussed in Z&B, p. 228-231

From the *.out file (TVD solution)

S

S = c (x y z )

Page 22: Problem Set 2  is based on a problem in the MT3D manual;  also discussed in Z&B, p. 228-231

Mass Storage: Solute

IN - OUT = S where change in storage isS = S(t2) – S(t1)

If IN > OUT, concentration in cell increases andthere is an increase in solute mass in the cell.IN = OUT + S, where S is positive.Note that S is on the OUT side of the equation.There is an apparent “sink” inside the cell.

If OUT > IN, the concentration in cell decreases andthere is a decrease in solute mass in the cell.IN – S = OUT, where S is negative and S is on the IN side of the equation. There is anapparent “source” inside the cell.

Page 23: Problem Set 2  is based on a problem in the MT3D manual;  also discussed in Z&B, p. 228-231

From the *.out file (TVD solution)

S

IN – OUT = 0(INsource+SIN) - (OUTsource + SOUT)= 0

SIN - SOUT = Storage

Page 24: Problem Set 2  is based on a problem in the MT3D manual;  also discussed in Z&B, p. 228-231

HMOC *.mas file

q’s =

Page 25: Problem Set 2  is based on a problem in the MT3D manual;  also discussed in Z&B, p. 228-231

General form of the ADE:

Expands to 9 terms

Expands to 3 terms

(See eqn. 3.48 in Z&B)

Where does the extra termcome from?

q’s =

Page 26: Problem Set 2  is based on a problem in the MT3D manual;  also discussed in Z&B, p. 228-231
Page 27: Problem Set 2  is based on a problem in the MT3D manual;  also discussed in Z&B, p. 228-231

Assume local chemical equilibrium (LEA):

Isotherms

Page 28: Problem Set 2  is based on a problem in the MT3D manual;  also discussed in Z&B, p. 228-231
Page 29: Problem Set 2  is based on a problem in the MT3D manual;  also discussed in Z&B, p. 228-231

HMOC *.mas file

Page 30: Problem Set 2  is based on a problem in the MT3D manual;  also discussed in Z&B, p. 228-231

Mass Balance error for FD solutions should be lessthan 1%.

Page 31: Problem Set 2  is based on a problem in the MT3D manual;  also discussed in Z&B, p. 228-231

MOC methods typically report high mass balance errors,especially at early times.

Page 32: Problem Set 2  is based on a problem in the MT3D manual;  also discussed in Z&B, p. 228-231

TVD Solution

Page 33: Problem Set 2  is based on a problem in the MT3D manual;  also discussed in Z&B, p. 228-231

From the *.out file (TVD solution)

S

IN – OUT = 0(INsource+SIN) - (OUTsource + SOUT)= 0

SIN - SOUT = Storage

Page 34: Problem Set 2  is based on a problem in the MT3D manual;  also discussed in Z&B, p. 228-231

From the *.out file (TVD solution)

Page 35: Problem Set 2  is based on a problem in the MT3D manual;  also discussed in Z&B, p. 228-231

Last t = 0.0089422 yr

Mass Flux = (mass at t2 - mass at t1) / t