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Motivation


Analytical model of temperature step-response in a Homogenous Stationary Pipe Flow with account for the heat exchange with surroundings

.

Model equally works for wellbore flow, ground, on-ground and bottom-water pipelines.

Outputs

LaTeX Math Inline
bodyT(t, l)

Along-hole Temperature Profile

...

where 

LaTeX Math Inline
bodyt

Flowing duration

LaTeX Math Inline
body

T_b(l)Background temperature

l

Length along pipe


Inputs

LaTeX Math Inline
body

q

T_s

Intake

flowrate

temperature

LaTeX Math Inline
body

a

T_

b

e(l)

Thermal diffusivity of
Background temperature of the surroundings

LaTeX Math Inline
body

r_f

\dot m

Mass flowrate

Flowing pipe radius

LaTeX Math Inline
body\lambda_b(l)

Thermal Conductivity of the surroundings

LaTeX Math Inline
body

r_wWellbore radius LaTeX Math Inlinebody

U

(l)

Heat Transfer Coefficient (HTC) between pipe fluid and surroundings

where 

LaTeX Math Inline
body

lwellbore trajectory Measured Depth with reference to Earth's surface (

a_e

Thermal Diffusivity of the surroundings

LaTeX Math Inline
body

l=0)

Assumptions

Constant rateConstant intake temperature

r_f

Flowing pipe radius

LaTeX Math Inline
body

--uriencoded--q_s(t) = q_s = %7B\rm const%7D

\lambda_e

Thermal Conductivity of the surroundings

LaTeX Math Inline
body

T_s(t) = T_s = \rm const

r_w

Wellbore radius


Equations

bigbigt_D(t) = \frac{a_e \, t}{r_w^2}


LaTeX Math Block
anchorTf_Ramey
alignmentleft
T(t, l) = T_be(l) - R(t) \, G_be(l)  +  \left(Big[ T_s - T_be(0) + R(t) \, G_be(l) \right)Big]  \,cdot e^{ - l/R(t)} 



LaTeX Math Block
anchorGb
alignmentleft
G_be = \frac{dT_be}{dl}




LaTeX Math Block
anchort_D
alignmentleft
t_D(t) = \frac{a_e \, t}{r_w^2}



LaTeX Math Block
anchorRelaxationRamey
alignmentleft
R(t) = \frac{q_s\dot m \, c_p}{2 \pi \, a\lambda_e} \,cdot \left( T_D(t) + \frac{\lambda_e}{r_f \, U} \right)



LaTeX Math Block
anchorT_D
alignmentleft
T_D(t) = \ln \
Big[ e^{-0.2 \, t_D} + (1.5 - 0.3719 \, e^{-t_D}) \, \sqrt{t_D} \
Big]  
LaTeX Math Block
anchort_D
alignmentleft



Assumptions

Intake Flowrate is constant in time

Intake Temperature is constant in time

LaTeX Math Inline
body--uriencoded--q_s(t) = q_s = %7B\rm const%7D

LaTeX Math Inline
bodyT_s(t) = T_s = \rm const

Thermal diffusivity of the surroundings is constant along-hole

Thermal Conductivity of the surroundings is constant along-hole

LaTeX Math Inline
bodya_e(l) = a_e = \rm const

LaTeX Math Inline
body\lambda_e(l) = \lambda_e = \rm const

Flowing pipe radius is constant along-holeWellbore radius is constant along-hole

LaTeX Math Inline
bodyr_f(l) = r_f = \rm const

LaTeX Math Inline
bodyr_w(l) = r_w = \rm const

Heat Transfer Coefficient (HTC) between pipe fluid and surroundings is constant along-hole

LaTeX Math Inline
bodyU(l) = U = \rm const


See Also

...

Physics / Fluid Dynamics / Pipe Flow Dynamics / Pipe Flow Simulation / Temperature Profile in Pipe Flow @model / Temperature Profile in Homogenous Pipe Flow @model


References

...


Show If
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Panel
bgColorpapayawhip
titleARAX

Ramey, H. J. (1962, April 1). Wellbore Heat Transmission. Society of Petroleum Engineers. doi:10.2118/

...

Show If
grouparax
Panel
bgColorpapayawhip
titleARAX

SPE-96-PA.pdf