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Harold Vance Department of Petroleum Engineering. Drilling System - Pressure Loss Calculations . Read:MI Chapter 5Multimedia Program
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1. Lesson 6 Drilling System - Pressure Loss Calculations
2. Harold Vance Department of Petroleum Engineering Drilling System - Pressure Loss Calculations Read: MI Chapter 5
Multimedia Program # 3 & 4
3. Harold Vance Department of Petroleum Engineering Drilling System - Pressure Loss Calculations Hydrostatics
Buoyancy
Flow through pipes and annuli
Flow path
Pressure loss calculations
4. Harold Vance Department of Petroleum Engineering Hydrostatics Liquid columns
Gas columns
Complex Columns
5. Harold Vance Department of Petroleum Engineering Hydrostatics in Liquid Columns 1 cu.ft. of water
62.4 lb/cuft
Area = 12x12
=144 sq.in
62.4 / 144 = .433 psi/ft
.433psi/ft/8.333 ppg
0.051962
~0.052 psi/ft/ppg
HSP = 0.052 x MW x TVD
6. Harold Vance Department of Petroleum Engineering Hydrostatics in Liquid Columns
7. Harold Vance Department of Petroleum Engineering Hydrostatics in Gas columns
8. Harold Vance Department of Petroleum Engineering Hydrostatics in Complex Columns
9. Harold Vance Department of Petroleum Engineering Hydrostatics in Complex Columns
10. Harold Vance Department of Petroleum Engineering Equivalent Density Concept EMW = Pressure/ (0.052 x TVD)
Equivalent mud weight is the total pressure imposed at a given depth expressed in ppg equivalent
e.g. 5946/ (0.052 x 10000) = 11.43 ppg
11. Harold Vance Department of Petroleum Engineering Buoyancy The net effect of hydraulic pressure acting on a foreign material immersed in the well fluid.
12. Harold Vance Department of Petroleum Engineering Buoyancy F1 = p1A = 0.052 x MW x D x A = Downward force
F2 = p2A = 0.052 x MW (D + h)A = Upward Force
The resultant buoyant force:
Fbo = F2 - F1 = 0.052 x MW x A (D+h-D)
= 0.052 x MW x A x h
13. Harold Vance Department of Petroleum Engineering Buoyancy Fbo = Weight of a the fluid displaced.
The effective weight of the submerged object is:
We = W - Fbo = W[1-(rm/rs)]
14. Harold Vance Department of Petroleum Engineering Flow through pipes and annuli
15. Harold Vance Department of Petroleum Engineering Flow through pipes and annuli
16. Harold Vance Department of Petroleum Engineering Flow path
17. Harold Vance Department of Petroleum Engineering Pressure loss calculations
18. Harold Vance Department of Petroleum Engineering Turbulence - Newtonian Onset of turbulence occurs at a Reynolds number of 2100
Table 4.6 gives equations for Reynolds number
19. Harold Vance Department of Petroleum Engineering Friction Factor - Newtonian
20. Harold Vance Department of Petroleum Engineering Turbulence -Bingham Plastic
21. Harold Vance Department of Petroleum Engineering Turbulence - Power Law
22. Harold Vance Department of Petroleum Engineering Velocity & Flow Behavior Parameters
23. Harold Vance Department of Petroleum Engineering Turbulence Criteria
24. Harold Vance Department of Petroleum Engineering Laminar Flow Frictional Pressure
25. Harold Vance Department of Petroleum Engineering Turbulent Flow Frictional Pressure
26. Harold Vance Department of Petroleum Engineering
27. Harold Vance Department of Petroleum Engineering Example 4.21 Given:
MW = 9.0 ppg Newtonian fluid
Viscosity = 15 cp
Depth = 10,000
Hole size = 7
DP size = 5
q = 80 gpm
Required:
Static and circulating BHP (assume Laminar)
28. Harold Vance Department of Petroleum Engineering Solution Static BHP
0.052 x 9 x 10,000 = 4680 psig
29. Harold Vance Department of Petroleum Engineering Solution Frictional pressure
30. Harold Vance Department of Petroleum Engineering Solution Circulating BHP = HSP + Friction
= 4680 + 51 = 4731 psig.
31. Harold Vance Department of Petroleum Engineering Turbulence? Critical Reynolds number = 2100
What is the critical velocity
32. Harold Vance Department of Petroleum Engineering Critical Velocity?