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Drilling Engineering – PE 311 Turbulent Flow in Pipes and Annuli

Drilling Engineering – PE 311 Turbulent Flow in Pipes and Annuli. Frictional Pressure Drop in Pipes and Annuli. When attempting to quantify the pressure losses in side the drillstring and in the annulus it is worth considering the following matrix:. Turbulent Flow in Pipes – Newtonian Fluids.

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Drilling Engineering – PE 311 Turbulent Flow in Pipes and Annuli

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  1. Drilling Engineering – PE 311 Turbulent Flow in Pipes and Annuli

  2. Frictional Pressure Drop in Pipes and Annuli When attempting to quantify the pressure losses in side the drillstring and in the annulus it is worth considering the following matrix:

  3. Turbulent Flow in Pipes – Newtonian Fluids Introduction Laminar Flow: In this type of flow, layers of fluid move in streamlines. There is no microscopic or macroscopic intermixing of the layers. Laminar flow systems are generally represented graphically by streamlines. Turbulent Flow: In turbulent flow, there is an irregular random movement of fluid in transverse direction to the main flow. This irregular, fluctuating motion can be regarded as superimposed on the mean motion of the fluid.

  4. Turbulent Flow in Pipes – Newtonian Fluids Definition of Reynolds Number Reynolds number, Re, is a dimensionless number that gives a measure of the ratio of inertial forces to viscous forces. Reynolds number is used to characterize different flow regimes, such as laminar or turbulent flow. Laminar occurs at low Reynolds number, where viscous forces are dominant, and is characterized by smooth, constant fluid motion; turbulent flow occurs at high Reynolds number and is dominated by inertial forces, which tend to produce chaotic eddies, vortices and other flow instabilities. For pipe In field unit:

  5. Turbulent Flow in Pipes – Newtonian Fluids Determination of Laminar/Turbulent Flow If Re < 2,100 Laminar flow Re = 2,100 – 4,000 Transition flow Re > 4,000 Turbulent Note that this critical Reynolds number is correct only for Newtonian fluids

  6. Turbulent Flow in Pipes – Newtonian Fluids Determination of Friction Factor - Laminar Flow Relationship between shear stress and friction factor: Pipe flow under laminar conditions: Therefore, Newtonian fluids flow in pipe under laminar flow conditions: Hence, This equation will be used to calculate the friction factor of Newtonian fluids flow in pipe under laminar flow conditions.

  7. Turbulent Flow in Pipes – Newtonian Fluids Determination of Friction Factor - Turbulent Flow For turbulent flow, the friction factor can be calculated by using Colebrook correlation. Where e is the absolute roughness. e/d is the relative roughness. For smooth pipe, the relative roughness e/d < 0.0004, the following equations can be used to calculate the friction factor in turbulent flow Re = 2,100 – 100,000: Blasius approximation: Re = 2,100 – 100,000:

  8. Turbulent Flow in Pipes – Newtonian Fluids Determination of Friction Factor

  9. Turbulent Flow in Pipes – Newtonian Fluids Determination of Friction Factor

  10. Turbulent Flow in Pipes – Newtonian Fluids Determination of the Frictional Pressure Loss From equation: , an equation of dp/dL can be expressed as In field unit: . This equation can be used to calculate the frictional pressure drop gradient for Newtonian and non-Newtonian fluids. Combining this equation and the Blasius approximation gives Note that the Moody friction factor is four times higher than the Fanning friction factor.

  11. Turbulent Flow in Pipes – Newtonian Fluids Example Example: Determine the frictional pressure drop in 10000ft of 4.5-in commercial steel drillpipe having an internal diameter of 3.826in. If a 20 cp Newtonian fluid having a density of 9 lbm/gal is pumped through the drillpipe at a rate of 400 gal/min Solution: Mean velocity: Reynolds number: Since Re > 2,100, the flow is under turbulent flow conditions.

  12. Turbulent Flow in Pipes – Newtonian Fluids Example From table 4.5, the absolute roughness for commercial steel pipe is e = 0.000013 inches. The relative roughness e/d = 0.000013/3.826 = 0.0000034 < 0.0004 --> smooth pipe Solve this equation for the Fanning friction factor: f = 0.00666 Thus the frictional pressure loss can be obtained by

  13. Turbulent Flow in Pipes – Newtonian Fluids Example Using Blasius approximation ,the equation becomes Pressure drop: DP = dp/dL x D = (0.0777)(10,000) = 777 psi

  14. Turbulent Flow in Pipes – Newtonian Fluids Example Using Blasius approximation ,the equation becomes Pressure drop: DP = dp/dL x D = (0.0777)(10,000) = 777 psi

  15. Turbulent Flow in Pipes/Annuli – NonNewtonian Fluids Equivalent Diameter for Annular Geometry – Hydraulic Diameter Method Hydraulic diameter is defined as: Equivalent diameter by using hydraulic diameter method:

  16. Turbulent Flow in Pipes/Annuli – nonNewtonian Fluids Equivalent Diameter for Annular Geometry – From Momentum Equation From the momentum equation, frictional pressure drop for Newtonian fluid in the annulus is For pipe flow, d1 --> 0 then Comparing these two equations, the equivalent diameter an annulus can be obtained

  17. Turbulent Flow in Pipes/Annuli – nonNewtonian Fluids Equivalent Diameter for Annular Geometry – Narrow Slot Approximation From the narrow slot approximation, frictional pressure drop for Newtonian fluid in the annulus is For pipe flow Comparing these two equations, the equivalent diameter an annulus can be obtained

  18. Turbulent Flow in Pipes/Annuli – nonNewtonian Fluids Equivalent Diameter for Annular Geometry – Crittendon Correlation A fourth expression for the equivalent diameter of an annulus was developed by Crittendon. When using Crittendon correlation, a fictitious average velocity also must be used in describing the flow system.

  19. Turbulent Flow in Pipes/Annuli – nonNewtonian Fluids Bingham Plastic Model or Obtain apparent viscosity by combining the frictional pressure loss in pipe (or annulus) for both Newtonian and Bingham Plastic models Use apparent viscosity to determine Reynolds Number

  20. Turbulent Flow in Pipes/Annuli – nonNewtonian Fluids Bingham Plastic Model Another way to determine the flow regime (critical Reynolds number) is to use the Hedstrom number In field unit

  21. Turbulent Flow in Pipes/Annuli – nonNewtonian Fluids Bingham Plastic Model Turbulent

  22. Turbulent Flow in Pipes/Annuli – nonNewtonian Fluids Power Law Model Apparent Viscosity for use in the Reynolds Number is obtained by comparing the laminar flow equations for Newtonian and Power Law fluids Pipe flow: Annular flow:

  23. Turbulent Flow in Pipes/Annuli – nonNewtonian Fluids Power Law Model Reynolds number for power law fluids in pipe: Reynolds number for power law fluids In annulus: Friction factor for power law fluids under turbulent flow conditions

  24. Turbulent Flow in Pipes/Annuli – nonNewtonian Fluids Power Law Model

  25. Summary

  26. Summary Newtonian Model Bingham Plastic Model Power Law Model

  27. Summary Newtonian Model Bingham Plastic Model Power Law Model

  28. Summary Newtonian Model Bingham Plastic Model Power Law Model

  29. Example – Newtonian Fluid in Annulus Example 1: A 9.0 lbm/gal brine having a viscosity of 1.0 cp is being circulated in a well at a rate of 200 gal/min. Apply the all the criteria for computing equivalent diameter. Determine the flow pattern and frictional pressure gradient. The drillpipe has an external diameter of 5.0 in. and the hole has a diameter of 10 in. Solution:

  30. Example – Newtonian Fluid in Annulus

  31. Example – Newtonian Fluid in Annulus

  32. Example – Newtonian Fluid in Annulus Hydraulic Method Momentum Mothod Narrow Slot Method Crittendon Method Note that the Crittendon correlation is applied for the fourth method. In this method, we need to calculate the equivalent diameter based on Crittendon correlation and the fictitious average velocity.

  33. Example – BHF - Annulus Example 2: A 10 lbm/gal mud having a plastic viscosity of 40 cp and a yield point of 15 lbf/100ft2 is circulated at a rate of 600 gal/min. Estimate the frictional pressure loss in the annulus opposite the drill collars if the drill collars are in a 6.5-in hole, have a length of 1,000 ft, and a 4.5 in. OD. Check for turbulence using both the apparent viscosity concept and the Hedstrom number approach. Use an narrow slot equivalent diameter to represent the annular geometry.

  34. Example – BHF - Annulus Equivalent diameter using narrow slot approximation Reynolds number based on apparent viscosity

  35. Example – BHF - Annulus Reynolds number for a plastic viscosity of 40 cp Using the graph for Hedstrom number, the critical Reynolds number is 3,300. The flow is turbulent

  36. Example – BHF - Annulus Using Blasius approximation with Re = 3,154, the friction factor is f = 0.0098 Frictional pressure loss is given:

  37. Example – BHF - Annulus

  38. Example – PL - Annulus Example 3: A 15.6 lbm/gal cement slurry having a consistency index of 335 eq cp and a flow behavior index of 0.67 is being pumped at a rate of 672 gal/min between a 9.625-in. hole and a 7.0-in.casing. Determine the frictional pressure loss per 100 ft of slurry. Use the equivalent diameter based on the narrow slot approximation. Solution: The mean velocity: Reynolds number:

  39. Turbulent Flow in Pipes/Annuli – nonNewtonian Fluids Power Law Model

  40. Example– PL - Annulus

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