casing design for a deep gas test well in the dripping

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Section 6-T14N-R94W Sweetwater County, Wyoming 13000’ Almond Test April 24 th , 2010 James Benson Kristin Carter Patrick Gardner Brandon Heiner Aaron Bounds

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Page 1: Casing design for a deep gas test well in the Dripping

Section 6-T14N-R94WSweetwater County, Wyoming

13000’ Almond Test

April 24th, 2010

James BensonKristin CarterPatrick GardnerBrandon HeinerAaron Bounds

Page 2: Casing design for a deep gas test well in the Dripping

Introduction

Health, Safety and Environmental

Geology / Hazards

Mud program

Casing Design criteria

Casing Program

Economics

Conclusion, Q&A

Page 3: Casing design for a deep gas test well in the Dripping

Purposes of casing:◦ Protects and isolates wellbore and surrounding

formations

Prevents contamination of water sources and, vice versa, keeps unnecessary water out of the produced fluids

◦ Strengthens wellbore

Can hold back weak formations from sloughing into wellbore and also keeps overweighted drilling fluids from fracturing and entering weak formations

Page 4: Casing design for a deep gas test well in the Dripping

Casing pipe itself is basically a standardized large-diameter pipe◦ Casing grades are denoted with a letter for tensile

yield and an abbreviated number for yield strength

“J-55” grade steel can withstand 55,000 psi before it starts to fail

In general, stronger casing (like P-110, for example) is more susceptible to hydrogen sulfide (H2S) embrittlement due to the metallurgy

Page 5: Casing design for a deep gas test well in the Dripping

Safety procedures put in place can be the weight of the mud, additional rams, a larger gas buster, and a flare. The heavier the mud weight the more pressure is placed on the recovered product. The weight must be balanced with the pressure of the formation and the product. Too heavy mud can cause fractures in the formation which can also be problematic.

The additional rams may be put in place to ensure that if there is a well control issue then the BOP can be closed.

If a well is high pressure there stands the potential for a large amount of gas, increasing the size of the buster may help when that gas is coming to surface.

The flare will be used in conjunction with the buster to destroy the gas and help relieve pressure.

Page 6: Casing design for a deep gas test well in the Dripping

Six named formations must be traversed before reaching the Almond

Page 7: Casing design for a deep gas test well in the Dripping

Mixed oil shales, coals and sandstones◦ Possibility of losing circulation to natural fractures

◦ Supplies Wamsutter with municipal water

◦ Shallow formation (roughly 1500’)

Page 8: Casing design for a deep gas test well in the Dripping

Mudstone with sandstone lenses and coal seam cap◦ Lost circulation common

◦ Depth of roughly 3000’

Page 9: Casing design for a deep gas test well in the Dripping

Mixed sandstones, shales and coal seams◦ Weak formation

Washouts common

◦ Many coal seams can lead to lost circulation

◦ Depth: 5800’

Page 10: Casing design for a deep gas test well in the Dripping

Mixed shale, siltstone, sandstone and coal seams◦ lost circulation is an issue

◦ Depth approximately 9200’

Page 11: Casing design for a deep gas test well in the Dripping

Sandstone◦ Known to contain uranium in other parts of the

country , unknown here

◦ Depth of roughly 10,200 feet

Page 12: Casing design for a deep gas test well in the Dripping

Shale with bentonite stringers◦ Possible wellbore stability problems

◦ Known to be a transition zone to higher (abnormal) pressures

◦ Depth: 10,500 ft

Page 13: Casing design for a deep gas test well in the Dripping

Target zone

Mixed sandstone, bentonitic shale, coal seams◦ Known to be overpressured

◦ Coal seams can take mud

◦ Depth approximately 12,600 feet

Page 14: Casing design for a deep gas test well in the Dripping

Standard 8.5 ppg mud until about 6000 ft

Escalate mud weight to 10 ppg at 10,000 ft

Lewis formation (10,450 ft) is expected to be transition to overpressured zones◦ Increase mud weight to control formation pressures

◦ Final mud weight should be between 14-16 ppg

Page 15: Casing design for a deep gas test well in the Dripping

Casing Design Criteria:

•Account for swab and surge pressures by adding a margin on both gradients•Work from the bottom to top, starting at TD and using the least number of different casing sizes possible while staying between the gradient margins

0

2000

4000

6000

8000

10000

12000

14000

16000

8 10 12 14 16 18

De

pth

(ft

)

Equivalent Mud Weight

GradientProfile

frac gradient

Page 16: Casing design for a deep gas test well in the Dripping

Industry standard of 1.12◦ Using tensile load as a factor to derate collapse

pressure rating from Halliburton “Red Book” (or similar source)

Page 17: Casing design for a deep gas test well in the Dripping
Page 18: Casing design for a deep gas test well in the Dripping

As the length of a casing string increases, the weight of lower pipe adds to tensile stress and derates the pressure capability (as above)◦ Industry standard is a TDF of 1.8

TDF= Joint Strength / Tension Load

Page 19: Casing design for a deep gas test well in the Dripping

0

2000

4000

6000

8000

10000

12000

14000

16000

8 10 12 14 16 18

De

pth

(ft

)

Equivalent Mud Weight

GradientProfile

fracgradient

This shows why a single

piece of casing will not

suffice.-One string will not allow

adequate pressure control during

the entire length of the wellbore

even ignoring surge and swab

pressure margins

Page 20: Casing design for a deep gas test well in the Dripping

0

2000

4000

6000

8000

10000

12000

14000

16000

8 10 12 14 16 18D

ep

th (

ft)

Equivalent Mud Weight

GradientProfile

frac gradient

GradientProfile lesstrip margin

FracGradientless kickmargin

Page 21: Casing design for a deep gas test well in the Dripping

Using the above chart:

Bottomhole pressure will be around 9500 psi◦ For 5 ½ in. casing, P-110 grade (20 lb/ft)

withstands 11,080 psi

◦ This casing becomes “overkill” at about 10,000 ft

Could change casing to a smaller size or lighter grade steel to save money

Page 22: Casing design for a deep gas test well in the Dripping

From the pore pressure chart, the next casing should be designed around a “bottom” pressure of around 6200 psi◦ Needs to accommodate a 6 ½ inch bit

◦ 7 ⅝ inch C-95 casing at 33.7 lb/ft withstands 9,380 psi

Appears to be overdesigned for pressure

Also need to consider tensile load – may be the limiting factor

Page 23: Casing design for a deep gas test well in the Dripping

Casing

Size

Bottom

Depth

Top

Depth Length

Casing

Grade,

weight Weight

Tension

at top

Minimum

Tension

Strength TDF

Collapse

Pressure

at

bottom

Collapse

resistance

(Tension) CDF

10 3/4 1520 Surface 1520 K-55, 40.5 61560 61560 450 7.31 711 1580 2.2

7 5/8 10500 7900 2600 C-95,33.7 87620 87620 772 8.8 6006 7042 1.17

7900 4900 3000 N-80,33.7 101100 188720 674 3.57 4519 5970 1.32

4900 1900 3000 N-80, 29.7 79200 267920 490 1.83 2803 3880 2.69

1900 Surface 1900 C-95, 26.4 50160 318080 560 1.76 1087 2931 2.69

5 1/2 13000 10000 3000 P-110, 20 60000 60000 548 9.13 9464 11080 1.17

Standard: > 1.8 > 1.12

Page 24: Casing design for a deep gas test well in the Dripping

0

2000

4000

6000

8000

10000

12000

14000

16000

8 10 12 14 16 18

De

pth

(ft

)

Equivalent Mud Weight

GradientProfile

frac gradient

GradientProfile lesstrip margin

Frac Gradientless kickmargin

Page 25: Casing design for a deep gas test well in the Dripping

The 2-string designs average $500k in materials

3-string design runs $800k just for materials, on top of extra rig time (tripping, cement setup and crew, casing crew and other labor)

Page 26: Casing design for a deep gas test well in the Dripping

Modified casing sizes for economics

◦ Supported by other wells in the area

◦ Used data from nearby wells

Formation data

Gas data

Production data

Page 27: Casing design for a deep gas test well in the Dripping

Tubing Size Grade Price / ft Length Total Price

10 3/4 J/K-55 $29.85 1520 $45,372.00

7 5/8 HCP-110 $35.00 10500 $367,500.00

5 1/2 P-110 $14.70 3000 $44,100.00

Tubing: 2 7/8 N/L-80 $6.00 13000 $78,000.00

Design (#2) Total $534,972.00

Tubing Size Grade Price / ft Length Total Price

9 5/8 J-55 $23.10 1520 $35,112.00

7 HCP-110 $28.80 10500 $302,400.00

4 1/2 P-110 $13.14 3000 $39,420.00

Tubing: 2 3/8 N/L-80 $4.60 13000 $59,800.00

Design (Final) Total $436,732.00

Savings: $98, 240

Page 28: Casing design for a deep gas test well in the Dripping

0

1000

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3000

4000

5000

6000

7000

8000

9000

10000

0 2 4 6 8 10

Pw

f (p

sia

)

q (MMscf/d)

IPR

2 3/8 tubing

2 7/8 tubing

Page 29: Casing design for a deep gas test well in the Dripping

1000

1100

1200

1300

1400

1500

1600

1700

1800

1900

2000

5.5 5.7 5.9 6.1 6.3 6.5

Pw

f (p

sia

)

q (MMscf/d)

IPR

2 3/8 tubing

2 7/8 tubing

Page 30: Casing design for a deep gas test well in the Dripping

Saves almost $100k on materials, will not have significant effect on production ability

Surface casing: 9 ⅝ in. J-55 36 lb/ft to 1520 feet

String #1: 7 in. HCP-110 to 10,500 feet

String #2: 4 ½ in. P-110 from 10,000 to 13,000 feet

Tubing: 2 ⅜ in. L-80 from 13,000 feet to surface

Page 31: Casing design for a deep gas test well in the Dripping

-Generated from

Schlumberger’s I-Handbook

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waterplan.state.wy.us/plan/green/techmemos/muniuse.pdf

Halliburton Cementing Tables, April 1999

Applied Drilling Engineering, Bourgoyne et al, SPE 1991

Wyoming Oil and Gas Conservation Commission, wogcc.state.wy.us/

Toolpushers Supply Company, www.truecos.com/Toolpushers/default.htm

Devon Energy, www.devonenergy.com