Scaling Analysis in Modeling Transport and Reaction Processes || Appendix E: Equations of Motion for...

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APPENDIX E Equations of Motion for Porous Media E.1 RECTANGULAR COORDINATES The following forms of the x -, y -, and z-components of the equations of motion in rectangular coordinates for flow through porous media are based on Brinkman’s empirical modification of Darcy’s law and assume a body force due to a grav- itational field, and an incompressible fluid having constant viscosity µ and per- meability k p ; the u i denote the components of the superficial velocity based on considering a porous medium to be homogeneous 1 : 0 =− ∂P ∂x µ k p u x + µ 2 u x ∂x 2 + µ 2 u x ∂y 2 + µ 2 u x ∂z 2 + ρg x (E.1-1) 0 =− ∂P ∂y µ k p u y + µ 2 u y ∂x 2 + µ 2 u y ∂y 2 + µ 2 u y ∂z 2 + ρg y (E.1-2) 0 =− ∂P ∂z µ k p u z + µ 2 u z ∂x 2 + µ 2 u z ∂y 2 + µ 2 u z ∂z 2 + ρg z (E.1-3) E.2 CYLINDRICAL COORDINATES The following forms of the r -, θ -, and z-components of the equations of motion in cylindrical coordinates for flow through porous media are based on Brinkman’s empirical modification of Darcy’s law and assume a body force due to a grav- itational field, and an incompressible fluid having constant viscosity µ and per- meability k p ; the u i denote the components of the superficial velocity based on considering a porous medium to be homogeneous 2 : 0 =− ∂P ∂r µ k p u r + µ ∂r 1 r ∂r (r u r ) + µ 1 r 2 2 u r ∂θ 2 µ 2 r 2 u θ ∂θ + µ 2 u r ∂z 2 + ρg r (E.2-1) 1 H. C. Brinkman, Appl. Sci. Res., A1, 27–34, 81–86 (1947). 2 Ibid. Scaling Analysis in Modeling Transport and Reaction Processes: A Systematic Approach to Model Building and the Art of Approximation, By William B. Krantz Copyright 2007 John Wiley & Sons, Inc. 494

Transcript of Scaling Analysis in Modeling Transport and Reaction Processes || Appendix E: Equations of Motion for...

Page 1: Scaling Analysis in Modeling Transport and Reaction Processes || Appendix E: Equations of Motion for Porous Media

APPENDIX EEquations of Motion for Porous Media

E.1 RECTANGULAR COORDINATES

The following forms of the x-, y-, and z-components of the equations of motionin rectangular coordinates for flow through porous media are based on Brinkman’sempirical modification of Darcy’s law and assume a body force due to a grav-itational field, and an incompressible fluid having constant viscosity µ and per-meability kp; the �ui denote the components of the superficial velocity based onconsidering a porous medium to be homogeneous1:

0 = −∂P

∂x− µ

kp

�ux + µ∂2�ux

∂x2+ µ

∂2�ux

∂y2+ µ

∂2�ux

∂z2+ ρgx (E.1-1)

0 = −∂P

∂y− µ

kp

�uy + µ∂2�uy

∂x2+ µ

∂2�uy

∂y2+ µ

∂2�uy

∂z2+ ρgy (E.1-2)

0 = −∂P

∂z− µ

kp

�uz + µ∂2�uz

∂x2+ µ

∂2�uz

∂y2+ µ

∂2�uz

∂z2+ ρgz (E.1-3)

E.2 CYLINDRICAL COORDINATES

The following forms of the r-, θ -, and z-components of the equations of motionin cylindrical coordinates for flow through porous media are based on Brinkman’sempirical modification of Darcy’s law and assume a body force due to a grav-itational field, and an incompressible fluid having constant viscosity µ and per-meability kp; the �ui denote the components of the superficial velocity based onconsidering a porous medium to be homogeneous2:

0 = −∂P

∂r− µ

kp

�ur + µ∂

∂r

[1

r

∂r(r�ur)

]+ µ

1

r2

∂2�ur

∂θ2− µ

2

r2

∂�uθ

∂θ+ µ

∂2�ur

∂z2+ ρgr

(E.2-1)

1H. C. Brinkman, Appl. Sci. Res., A1, 27–34, 81–86 (1947).2Ibid.

Scaling Analysis in Modeling Transport and Reaction Processes: A Systematic Approachto Model Building and the Art of Approximation, By William B. KrantzCopyright 2007 John Wiley & Sons, Inc.

494

Page 2: Scaling Analysis in Modeling Transport and Reaction Processes || Appendix E: Equations of Motion for Porous Media

SPHERICAL COORDINATES 495

0 = −1

r

∂P

∂θ− µ

kp

�uθ + µ∂

∂r

[1

r

∂r(r�uθ)

]+ µ

1

r2

∂2�uθ

∂θ2

+ µ2

r2

∂�ur

∂θ+ µ

∂2�uθ

∂z2+ ρgθ (E.2-2)

0 = −∂P

∂z− µ

kp

�uz + µ1

r

∂r

(r∂�uz

∂r

)+ µ

1

r2

∂2�uz

∂θ2+ µ

∂2�uz

∂z2+ ρgz (E.2-3)

E.3 SPHERICAL COORDINATES

The following forms of the r-, θ -, and φ-components of the equations of motionin spherical coordinates for flow through porous media are based on Brinkman’sempirical modification of Darcy’s law and assume a body force due to a grav-itational field, and an incompressible fluid having constant viscosity µ and per-meability kp; the �ui denote the components of the superficial velocity based onconsidering a porous medium to be homogeneous3:

0 = −∂P

∂r− µ

kp

�ur + µ1

r2

∂2

∂r2(r2�ur) + µ

1

r2 sin θ

∂θ

(sin θ

∂�ur

∂θ

)

+ µ1

r2 sin2 θ

∂2�ur

∂φ2+ ρgr (E.3-1)

0 = −1

r

∂P

∂θ− µ

kp

�uθ + µ1

r2

∂r

(r2 ∂�uθ

∂r

)+ µ

1

r2

∂θ

[1

sin θ

∂θ(�uθ sin θ)

]

+ µ1

r2 sin2 θ

∂2�uθ

∂φ2+ µ

2

r2

∂�ur

∂θ− µ

2 cos θ

r2 sin2 θ

∂�uφ

∂φ+ ρgθ (E.3-2)

0 = − 1

r sin θ

∂P

∂φ− µ

kp

�uφ + µ1

r2

∂r

(r2 ∂�uφ

∂r

)+ µ

1

r2

∂θ

[1

sin θ

∂θ(�uφ sin θ)

]

+ µ1

r2 sin2 θ

∂2�uφ

∂φ2+ µ

2

r2 sin θ

∂�ur

∂φ+ µ

2 cos θ

r2 sin2 θ

∂�uθ

∂φ+ ρgφ (E.3-3)

3Ibid.