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Fig. 1. Dual-barrier well completion schematic



The Heat Transfer Coefficient (HTC) of dual-barrier well completionIn case of dual-barrier single-string completion with flowing fluid in the annulus (see Fig. 3) the HTC is defined by the following equation:

LaTeX Math Block
anchorFZZ1HU
alignmentleft
\frac{1}{ r_{ti} \, U} = \frac{1}{r_{ti} \, U_{ti}} + \frac{1}{\lambdar_t{ti} \, \ln \frac{rU_t}{r_{ti}} +
+ \frac{1}{\lambdad_{a, \rm eff}}ann} \ln \frac{r, U_{ciann}}{r_t} +
\frac{1}{\lambdar_c{ci} \ln \frac{r, U_c}{r_{ci}}  + \frac{1}{\lambdar_c \, U_{cem}} \ln \frac{r_w}{r_c} 

where

LaTeX Math Inline
bodyr_t

outer radius of the tubing

Image Removed

LaTeX Math Inline
body--uriencoded--r_%7Bti%7D

inner radius of the tubing

LaTeX Math Inline
body--uriencoded--h_t = r_t - r_%7Bti%7D

tubing wall thickness

LaTeX Math Inline
bodyr_c

outer radius of the casing

LaTeX Math Inline
body--uriencoded--r_%7Bci%7D

inner radius of the casing

LaTeX Math Inline
bodyh_c = r_c - r_i

casing wall thickness

LaTeX Math Inline
bodyr_w

\lambda_tthermal conductivity of tubing material
wellbore radius by drilling bit

LaTeX Math Inline
body--uriencoded--\displaystyle U_%7Bti%7D = \frac%7B\lambda%7D%7B2 \, r_%7Bti%7D%7D \, %7B\rm Nu%7D_%7Bti%7D

Pipe Flow Heat Transfer Coefficient

LaTeX Math Inline
body--uriencoded--\displaystyle U_t = \frac%7B\lambda

_t%7D%7Br_%7Bti%7D \cdot \ln (r_t/r_%7Bti%7D)%7D

Tubing Wall Conductive Heat Transfer Coefficient
thermal conductivity of fluid moving through the tubing

LaTeX Math Inline
body--uriencoded--\displaystyle U_%7Bann%7D = \frac%7B\lambda_%7Bann%7D%7D%7Bd_

%7Ba

%7Bann%7D%7D \, %7B\rm

eff%7D = \lambda_a \cdot \epsilon_aeffective thermal conductivity of the annulus 

Nu%7D_%7Bann%7D

Annular Flow Heat Transfer Coefficient

LaTeX Math Inline
body--uriencoded--\displaystyle U_c = \frac%7B\lambda_c%7D%7Br_%7Bci%7D \cdot \ln (r_c/r_%7Bci%7D)%7D

Casing Wall Conductive Heat Transfer Coefficient

LaTeX Math Inline
body

\epsilon_aNatural Convection Heat Transfer Multiplier

--uriencoded--\displaystyle U_%7Bcem%7D = \frac%7B\lambda_%7Bcem%7D%7D%7Br_c \cdot \ln (r_w/r_c)%7D

Cement Conductive Heat Transfer Coefficient

LaTeX Math Inline
body--uriencoded--d_%7Bann%7D = r_%7Bci%7D-r_t

annular hydraulic diameter

LaTeX Math Inline
body\lambda

thermal conductivity of fluid moving through the tubing

LaTeX Math Inline
body--uriencoded--\lambda_

a

%7Bann%7D

thermal conductivity of fluid in the annulus

LaTeX Math Inline
body\lambda_t

thermal conductivity of tubing material

LaTeX Math Inline
body\lambda_с

thermal conductivity of casing material

LaTeX Math Inline
body--uriencoded--\

displaystyle U_%7Bti%7D = \frac%7B\lambda%7D%7B2 \, r_%7Bti%7D%7D \, %7B\rm Nu%7D_%7Bti%7D

heat transfer coefficient (HTC)
between inner surface of tubing and moving fluid

lambda_%7Bcem%7D

thermal conductivity of cement


The equation 

LaTeX Math Block Reference
anchorU
 can be written explicitly as:

LaTeX Math Block
anchorFZZ1H
alignmentleft
\frac{1}{ r_{ti} \, U} = \frac{2}{\lambda \, {\rm Nu}_{ti}} + \frac{1}{\lambda_t} \, \ln \frac{r_t}{r_{ti}}
+ \frac{1}{\lambda_{ann} \, {\rm Nu}_{ann}} +
\frac{1}{\lambda_c} \ln \frac{r_c}{r_{ci}} + \frac{1}{\lambda_{cem}} \ln \frac{r_w}{r_c} 


See also

...

Physics / Thermodynamics / Heat Transfer /  Heat Transfer Coefficient (HTC) / Heat Transfer Coefficient (HTC) @model

[ Single-barrier well completion Heat Transfer Coefficient @model ]

[ Thermal conductivity ] [ Nusselt number (Nu) ] [ Natural Convection Heat Transfer Multiplier ]