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Directional
Data given:
Water depth = 430 ft MSL
Rig floor elevation = 70 ft MSL
Hydrogen Sulphide = 0 mol%
Carbon Dioxide = 0 mol%
N ft | E ft | TVD ft brt | |
Surface location of rig | 0.00 | 0.00 | 0.00 |
Target location | 5320.00 | 0.00 | 9500.00 |
TD | 5320.00 | 0.00 | 10250.00 |
KOP (immediately below surface) = 2.00 deg/100 ft
DOP (where needed to be) = 4.00 deg/100 ft
Calculation of the radius of curvature:
V1 = 1000 ft TVD brt
V4 = 9500 ft TVD brt
D3 = 5320 ft
V5 = 10250 ft
Manual profile has to be chosen:
R1 + R2 = 2865+1432 = 4297 ft, which is less than 5320 ft, i.e. R1 + R2 < total target distance.
Line X = D3 – (R1 + R2) = 5320 – 4297 = 1023 ft
= = 7406 ft
Angle = Angle FOG + = 30.1 + 6.9 = 370
End of build
Measured depth = V1 + = 1000 + = 2850 ft
Vertical depth (V2) = V1 + R1 = 1000 + 2865*sin(370) = 2724 ft
Displacement (D1) = R1 (1-cos ) = 2865*(1-0.798) = 577 ft
Start of drop
Measured depth = V1 + + OG = 2850 + 7406 = 10256 ft
Vertical depth (V3) = V2 + OG*cos = 2724 + 7406*cos370 = 8639 ft
Displacement (D2) = D1 + OG*sin = 577 + 7406*sin370 = 5034 ft
End of drop
Measured depth = V1 + + OG + = 1000 + + 7406 + = 11181 ft
V4 = 9500 ft
D3 = 5320 ft
“S” profile design
“S” profile | MD ft | Inc 0 | Azi 0 | TVD ft | N ft | E ft | DLS 0/100ft |
Tie-in | |||||||
KOP | |||||||
End of build | |||||||
Start of drop | |||||||
End of drop | |||||||
TD |
Casing
Data given:
Rig floor elevation (RFE) = 430 ft
Water depth (WD) = 70 ft
Density of sea water (ρsw) = 0.45 psi/ft
where:
ρr: density of return fluid
ρf: density formation
The value of ρr is obtained by adding density of cuttings to seawater density, so it is 9.1 ppg, or 0.476 psi/ft. Convergent factor of 0.052 was used. From the information of fracture gradient at certain depth, ρf is calculated:
In order to find the depth of conductor, the following equation is used:
Casing | Conductor | Surface | Intermediate | Production | Production Liner |
ft TVD brt | |||||
ft TVD brt |
Measured Depth from directional plan
Conductor’s MD remains the same as TVD. Adding rig floor elevation and water depth, afterwards subtracting the result from TVDbrt surface casing, the measured depth of surface casing is obtained. 1000 – (430+70) = 500 ft SS.
In order to calculate the Measured Depth for intermediate casing, subsea length of the end of build was obtained, it is 2850 – 500 = 2350 ft MDSS. The difference in TVD subsea from final point of intermediate casing to the TVD point end of build and angle were used to get second part of intermediate casing: (4200-2224)/cos370 = 2474 ft. For the purpose of calculating the Measured Depth of intermediate casing we add these values together:
2350 + 2474 = 4824 ft MD ft subsea.
Measured Depth of production casing is taken from question 1 (i.e. “S” design profile), and the rig floor elevation and water depth values were subtracted: 11181 – 500 = 10681 MD ft subsea.
Measured Depth of production liner is calculated using the same way: 11931 – 500 = 11431 MDftSS.
API 5C2 was examined and wt/ft of J-55 with 20̋ outer diameter and wt/ft of P-110 were used to select the nominal weights. Drift diameter (DD) is considered as minimum allowable assured diameter, therefore attention needs to be paid for that. In order to reduce uncertainties, the inner diameters should be close to next diameter.
Casing | Grade | Nominal weight, lb/ft | Di (inside diameter), inch | Do (outer diameter), inch | DD (drift diameter) inch | Collapse resistance, psi | Pipe body yield, 1000 lb | DB, (diameter of bit), inch |
Surface | J-55 | 18.73 | 18.542 | 17.5 | ||||
Intermediate | P-110 | 12.415 | 13.375 | 12.259 | 12.25 | |||
Production | P-110 | 8.681 | 9.625 | 8.525 | 8.5 | |||
Production liner | P-110 | 6.184 | 6.059 |
Cementing
Data given:
Top Lead | Height of tail | Shoe track length | Outer diameter | Inner diameter | |
Conductor | n/a | seabed | 40 ft | ||
Surface casing | seabed | 500 ft | 40 ft | API 5C2 | |
Intermediate casing | 500 ft | 80 ft | 13 3/8 | API 5C2 | |
Production casing | n/a | 500 ft | 80 ft | 9 5/8 | API 5C2 |
Production liner | n/a | entire length | 160 ft | API 5C2 |
TVDSS conductor = 186 ft
Tail yield = 1.15 cuft/sack
Lead yield = 1.5 cuft/sack
In order to calculate conductor tail cement volume we have to use:
1. Annulus volume between diameter of drill bit and outer diameter of conductor casing;
2. Volume of shoe track.
Drill bit diameter is not given; however, initial diameter of borehole is usually 36 inches.
Volume of conductor tail cement = annulus volume + volume of shoe track =
Except conductor, cementation volume is generally taken from iHandbook software. For surface cementing, annulus volume is 472.65 ft3 and shoe track volume is 76.53 ft3.
Volume of surface tail cement = annulus volume + volume of shoe track + height of conductor
So, volume = 472.65 + 76.53 + 333.74 = 882.92 ft3
Volume of intermediate tail cement = 414.55 ft3, volume of intermediate lead cement = 3125 ft3.
Volume of production tail cement = 189.46 ft3, volume of production lead cement = 3268.67.5 ft3.
Volume of production liner tail cement = 128.47 ft3.
Number of sacks is calculated by dividing the volume to the yield.
Casing | Volume of tail, ft3 | Volume of lead, ft3 | Sack number of tail | Sack number of lead |
Conductor | 560.77 | |||
Surface | 882.92 | |||
Intermediate | 414.55 | |||
Production | 189.46 | 3268.67 | ||
Production liner | 128.47 | |||
Total |
Drilling fluids
Since there is no problems were reported, drilling fluid for conductor is chosen as water based. It is economically valuable.
Flow of the mud to the aquifer should be prevented by controlling loss of drilling mud. For the surface borehole, water based mud is chosen as well. However, it is not pure water, with different additives (e.g. viscosifiers, fluid loss control).
Reactive shales are present in production borehole. To drill intermediate borehole, main issues could be selected as instability of the borehole and shale reactiveness. Silicate based mud is chosen for this borehole. It is economically valuable as well.
Natural fractured layers are evident in production borehole drilling which arise some problems. Again, water based mud type is essential here.
Production liner indicates good reservoir quality, because of high poroperm values. The drilling fluid flows to formation and cuttings, that’s why it is very important not to damage somehow permeability during the drilling processes. Mud is likely to be oil based.
Mud density values are read from Chart 1.
Borehole | Mud density (ppg) | Mud type |
Conductor | 8.9 | Water based |
Surface | 8.9 | Water based |
Intermediate | 10.2 | Silicate based |
Production | 15.5 | Water based |
Production liner | 13.9 | Oil based |
Shale shakers are used as equipment that removes drilled cuttings from the mud. When the used drilling mud comes to the surface it is directed to the shale shakers where the process begins. Consequently, drilling mud is moved to the mud tanks where the further solids control facilities remove finer solid. These finer solids are eliminated by desander and desilter.
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