Lecture 19 and 20 Flow through porous media

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Lecture 19 and 20 Flow through porous media

Lecture 19 and 20 Flow through porous media

History A lovely picture of Henry Darcy (1856)

History A lovely picture of Henry Darcy (1856)

Darcy’s Experiment water q 1 h 1 L h 2 2 atm

Darcy’s Experiment water q 1 h 1 L h 2 2 atm

Hydraulic Head (h) Energy of a stationary liquid b y 1 Head = potential

Hydraulic Head (h) Energy of a stationary liquid b y 1 Head = potential energy + pressure For this case: h 1 = h 2 Why? y 2

Head Loss Energy loss of liquid For steady moving viscous flow: Friction loss h

Head Loss Energy loss of liquid For steady moving viscous flow: Friction loss h 1 -h 2 = head loss = friction loss

Darcy’s Experiment 1 q L 2 A K is the hydraulic conductivity K [=]

Darcy’s Experiment 1 q L 2 A K is the hydraulic conductivity K [=] L/t Darcy’s law can be interpreted as a momentum, or as an energy equation

Generalization to nonvertical flow q Elevation datum L b A 2 1 z 2

Generalization to nonvertical flow q Elevation datum L b A 2 1 z 2

Generalization to nonvertical flow

Generalization to nonvertical flow

Definition of permeability, k Nutting (1930) found K ~ 1/ k is the intrinsic

Definition of permeability, k Nutting (1930) found K ~ 1/ k is the intrinsic permeability k [=] L 2

Darcy’s Law q is the volumetric flow rate q [=] cm 3/s q/A =

Darcy’s Law q is the volumetric flow rate q [=] cm 3/s q/A = u is the flux velocity also called the linear velocity q/A [=] cm/s

Flux velocity and interstitial velocity Flux velocity Velocity of liquid averaged over total volume

Flux velocity and interstitial velocity Flux velocity Velocity of liquid averaged over total volume Interstitial velocity Velocity of liquid averaged over void volume (measures velocities in the pores)

How good is Darcy’s law? q potential kinetic Pay attention when you deviate from:

How good is Darcy’s law? q potential kinetic Pay attention when you deviate from: • steady state • homogeneous material • incompressible fluid • average flow velocity Darcy flow Non-Darcy flow dp/ds

Units for k 1 cm 3 cube/s 1 darcy = 10 -12 m 2

Units for k 1 cm 3 cube/s 1 darcy = 10 -12 m 2 1 atm =1 cp k=1 darcy 1 md = 10 -15 m 2

Oilfield units k in md is specific gravity in cp is dip angle q

Oilfield units k in md is specific gravity in cp is dip angle q in STB/day dp/ds is psi/ft B in res bbl/STB

Horizontal Flow q x For horizontal flow s=x:

Horizontal Flow q x For horizontal flow s=x:

Vertical Flow through Core air 1 q 2 air p 1 = p 2

Vertical Flow through Core air 1 q 2 air p 1 = p 2 = patm= 0 psig

Vertical Flow with Driving Head b 1 L q 2

Vertical Flow with Driving Head b 1 L q 2

Upward Vertical Flow q L b

Upward Vertical Flow q L b

Radial Flow of a Production Well q rw re • s is the direction

Radial Flow of a Production Well q rw re • s is the direction of flow • r is from well to the boundary

Radial Flow of a Production Well q rw re Can we now integrate?

Radial Flow of a Production Well q rw re Can we now integrate?

Radial Flow of a Production Well A is a function of r r bb

Radial Flow of a Production Well A is a function of r r bb q re q constant for steady state

Radial Flow of a Production Well

Radial Flow of a Production Well

Extension to heterogeneous systems Parallel beds q 1 k 1 b 1 q 2

Extension to heterogeneous systems Parallel beds q 1 k 1 b 1 q 2 k 2 b 2 q 3 k 3 b 3 L How to compute total q ? b w

Set up Darcy’s law for each layer q 1 k 1 b 1 q

Set up Darcy’s law for each layer q 1 k 1 b 1 q 2 k 2 b 2 q 3 k 3 b 3 L b w

Extension to heterogeneous systems Series of beds Δp 1 Δp 2 Δp 3 L

Extension to heterogeneous systems Series of beds Δp 1 Δp 2 Δp 3 L 1 L 2 L 3 q Show that

Extension to heterogeneous systems Why are they so different? Δp 1 q 1 k

Extension to heterogeneous systems Why are they so different? Δp 1 q 1 k 1=500 b 1=10 q 2 k 2=0. 01 b 2=1 q 3 k 3=10 b 3=5 Δp 2 Δp 3 b q k 1=500 L 1=10 k 3=10 k 2=0. 01 L 2=1 L 3=5 w L Does this seem realistic to you?