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Single-barrier well completion Heat Transfer Coefficient @model |
Dual-barrier well completion Heat Transfer Coefficient @model |
Examples
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\frac{1}{ d_{ci} \, U} = \frac{1}{d_{ci} \, U_{ci}} + \frac{1}{\lambda_c} \ln \frac{d_c}{d_{ci}} + \frac{1}{\lambda_{\rm cem}} \ln \frac{d_w}{d_c}
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where
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wellbore diameter (with radius
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outer diameter of the casing (with outer radius
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inner diameter of the casing (with inner radius
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thermal conductivity of the casing material
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thermal conductivity of cement
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Nusselt number for the moving wellbore fluid with account of its contact with inner surface of the casing
title | Dual-barrier Completion |
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In case of single-string well completion with flowing fluid in the annulus (see Fig. 3) the HTC is defined by the following equation:
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\frac{1}{ d_{ti} \, U} = \frac{1}{d_{ti} \, U_{ti}} + \frac{1}{\lambda_t} \, \ln \frac{d_t}{d_{ti}} + + \frac{1}{\lambda_{a, \rm eff}} \ln \frac{d_{ci}}{d_t} + \frac{1}{\lambda_c} \ln \frac{d_c}{d_{ci}} + \frac{1}{\lambda_{cem}} \ln \frac{d_w}{d_c} |
where
| outer radius of tubing (with outer radius
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| inner diameter of the tubing (with inner radius
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| tubing wall thickness | |||||||||
| outer radius of casing (with outer radius
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| inner diameter of the casing (with inner radius
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| casing wall thickness | |||||||||
| thermal conductivity of tubing material | |||||||||
| thermal conductivity of fluid moving through the tubing | |||||||||
| effective thermal conductivity of the annulus | |||||||||
| Natural Convection Heat Transfer Multiplier | |||||||||
| thermal conductivity of fluid in the annulus | |||||||||
| heat transfer coefficient (HTC) |
In case the annulus is filled with stagnant fluid the annulus fluid convection will be natural and the Convection Heat Transfer Multiplier
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In case the annulus fluid is moving the annulus fluid convection will be forced and the Convection Heat Transfer Multiplier
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