1 basic formulas
TRANSCRIPT
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CHAPTER ONE
BASIC FORMULAS
Pressure Gradient
Pressure gradient, psi/ft, using mud weight, ppg
psi/ft = mud weight, ppg x 0.052
Example: 12.0 ppg fluidpsi/ft = 12.0ppg x 0.052psi/ft = 0.624
Pressure gradient, psi/ft, using mud weight, lb/ft3
psi/ft = mud weight, lb/ft3 x 0.006944
Example: 100 lb/ft3 fluidpsi/ft = 1001b/ft3 x 0.006944psi/ft = 0.6944
OR
psi/ft = mud weight, lb/ft3 -s- 144
Example: 100 lb/ft3 fluidpsi/ft = 1001b/ft3 + 144psi/ft = 0.6944
Pressure gradient, psi/ft, using mud weight, specific gravity (SG)
psi/ft = mud weight, SG x 0.433
Example: 1.0 SG fluidpsi/ft = 1.0SG x 0.433psi/ft = 0.433
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Metric calculations
Pressure gradient, bar/m = drilling fluid density kg/1 x 0.0981Pressure gradient, bar/1 Om = drilling fluid density kg/1 x 0.981
S.I. units calculations
Pressure gradient, kPa/m = drilling fluid density, kg/m3 -5-102
Convert pressure gradient, psi/ft, to mud weight, ppg
ppg = pressure gradient, psi/ft + 0.052
Example: 0.4992 psi/ftppg = 0.4992psi/ft -s- 0.052ppg = 9.6
Convert pressure gradient, psi/ft, to mud weight, lb/ft3
lb/ft3 = pressure gradient, psi/ft + 0.006944
Example: 0.6944psi/ftlb/ft3 = 0.6944psi/ft + 0.006944lb/ft3 = 100
Convert pressure gradient, psi/ft, to mud weight, SG
SG = pressure gradient, psi/ft -s- 0.433
Example: 0.433 psi/ftSG = 0.433psi/ft + 0.433SG = 1.0
Metric calculations
Drilling fluid density, kgA = pressure gradient, bar/m -s- 0.0981Drilling fluid density, kg/1 = pressure gradient, bar/lOm *- 0.981
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S.I. units calculations
Drilling fluid density, kg/m3 = pressure gradient, kPa/m x 102
Hydrostatic Pressure (HP)
Hydrostatic pressure using ppg and feet as the units of measure
HP = mud weight, ppg x 0.052 x true vertical depth (TVD), ft
Example: mud weight = 13.5ppgtrue vertical depth = 12,000 ft
HP = 13.5ppg x 0.052 x 12,000ftHP = 8424psi
Hydrostatic pressure, psi, using pressure gradient, psi/ft
HP = psi/ft x true vertical depth, ft
Example: pressure gradient = 0.624 psi/fttrue vertical depth = 8500ft
HP = 0.624psi/ft x 8500ftHP = 5304psi
Hydrostatic pressure, psi, using mud weight, Ib/ft3
HP = mud weight, lb/ft3 x 0.006944 x TVD, ft
Example: mud weight = 90 lb/ft3
true vertical depth = 7500 ftHP = 901b/ft3 x 0.006944 x 7500ftHP = 4687psi
Hydrostatic pressure, psi, using meters as unit of depth
HP = mud weight, ppg x 0.052 x TVD, m x 3.281
Example: mud weight = 12.2 ppgtrue vertical depth = 3700 meters
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HP = 12.2ppg x 0.052 x 3700 x 3.281HP = 7701psi
Metric calculations
Hydrostatic _ drilling fluid w n n o 0 1 ^ true vertical
pressure, bar density, kg/I depth, m
S.I. units calculations
Hydrostatic _ drilling fluid density, kg/m3pressure, kPa " m X t r u e v e r t i c a l d e p t h ' m
Converting Pressure into Mud Weight
Convert pressure, psi, into mud weight, ppg, using feet asthe unit of measure
Mud weight, ppg = pressure, psi -s- 0.052 -s- TVD, ft
Example: pressure = 2600 psitrue vertical depth = 5000 ft
Mud, ppg = 2600psi - 0.052 - 5000ftMud = lO.Oppg
Convert pressure, psi, into mud weight, ppg, using meters as the unitof measure
Mud weight, ppg = pressure, psi -s- 0.052 + TVD, m -s- 3.281
Example: pressure = 3583 psitrue vertical depth = 2000 meters
Mud wt, ppg = 3583psi - 0.052 -* 2000 m - 3.281Mud wt = 10.5 ppg
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Metric calculations
Equivalent drilling _ pressure, ^ ^ ^ 1 ^ true verticalfluid density, kg/1 bar ' depth, m
S.I. units calculations
Equivalent drilling _ pressure, ^ t r u e verticalfluid density, kg/m3 ~ kPa ' depth, m
Specific Gravity (SG)
Specific gravity using mud weight, ppg
SG = mud weight, ppg H- 8.33
Example: 15.0ppg fluidSG = 15.0ppg H- 8.33SG = 1.8
Specific gravity using pressure gradient, psi/ft
SG = pressure gradient, psi/ft * 0.433
Example: pressure gradient = 0.624 psi/ftSG = 0.624psi/ft + 0.433SG = 1.44
Specific gravity using mud weight, Ib/ft3
SG = mud weight, lb/ft3 + 62.4
Example: mud weight = 120 lb/ft3
SG = 1201b/ft3 H- 62.4SG = 1.92
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Convert specific gravity to mud weight, ppg
Mud weight, ppg = specific gravity x 8.33
Example: specific gravity = 1.80Mud wt, ppg = 1.80 x 8.33Mud wt = 15.0ppg
Convert specific gravity to pressure gradient, psi/ft
psi/ft = specific gravity x 0.433
Example: specific gravity = 1.44psi/ft = 1.44 x 0.433psi/ft = 0.624
Convert specific gravity to mud weight, lb/ft3
lb/ft3 = specific gravity x 62.4
Example: specific gravity = 1.92lb/ft3 = 1.92 x 62.4lb/ft3 = 120
Equivalent Circulating Density (ECD), ppg
(annular "\ , * . - >.ECD, ppg = pressure
+ 0.052 + TVD, ft + fmud w e i g h Mf Vm use, ppg JUoss, psij v F F & y
Example: annular pressure loss = 200 psitrue vertical depth = 10,000 ftmud weight = 9.6ppg
ECD, ppg = 200psi + 0.052 + 10,000ft + 9.6ppgECD = lO.Oppg
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Metric calculation
Equivalent drilling = annular pressure + + m + m u d
fluid density, kg/1 loss, bar
S.I. units calculations
Equivalent circulating annular pressure loss, kPa x 102 . ,density, kg/1 = T V D ^ + m u d d e n S l t y ' ^
Maximum Allowable Mud Weight from Leak-off Test Data
_ Heak-off ^ _ n n
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Decimal equivalent = 95 - 100 = 0.95
PO@95% = 0.142884bbl/stk x 0.95PO@95% = 0.13574bbl/stk
Formula 2
PO, gpm = [3(D2 x 0.7854) S] 0.00411 x SPM
where D = liner diameter, in.S = stroke length, in.SPM = strokes per minute
Example: Determine the pump output, gpm, for a 7-in. by 12-in. triplexpump at 80 strokes per minute:
PO, gpm = [3(72 x 0.7854) 12] 0.00411 x 80PO, gpm = 1385.4456 x 0.00411 x 80PO = 455.5 gpm
Duplex Pump
Formula 1
0.000324 x {!!ner t . f x (f\t . ) = bbl/stk
^diameter, m.J v length, m.J-0.000162 x frd
t . f x f f 0 ^ . ) = bbl/stkV diameter, m.J [length, m.J
pump output @ 100% eff = bbl/stk
Example: Determine the output, bbl/stk, of a 5-1/2 in. by 14-in. duplexpump at 100% efficiency. Rod diameter = 2.0in.:
0.000324 x 5.52 x 14 = 0.137214bbl/stk-0.000162 x 2.02 x 14 = 0.009072bbl/stk
Pump output 100% eff = 0.128142 bbl/stk
Adjust pump output for 85% efficiency:Decimal equivalent = 85 + 100 = 0.85
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PO@85% = 0.128142bbl/stk x 0.85PO@85% = 0.10892 bbl/stk
Formula 2
PO, bbl/stk = 0.000162 x S [2(D)2 - d2]
where S = stroke length, in.D = liner diameter, in.d = rod diameter, in.
Example: Determine the output, bbl/stk, of a 5-1/2-in. by 14-in. duplexpump @ 100% efficiency. Rod diameter = 2.0in.:
PO @ 100% = 0.000162 x 14 x [2 (5.5)2 - 22]PO @ 100% = 0.000162 x 14 x 56.5PO @ 100% = 0.128142bbl/stk
Adjust pump output for 85% efficiency:PO@85% = 0.128142bbl/stk x 0.85PO@85% = 0.10892 bbl/stk
Metric calculation
Pump output, liter/min = pump output, liter/stk x pump speed, spm
S.I. units calculation
Pump output, mVmin = pump output, liter/stk x pump speed, spm
Annular Velocity (AV)
Annular velocity (AV), ft/min
Formula 1
AV = pump output, bbl/min * annular capacity, bbl/ft
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Example: pump output = 12.6bbl/minannular capacity = 0.1261 bbl/ft
AV = 12.6bbl/min -s- 0.1261 bbl/ftAV = 99.92ft/min
Formula 2
where Q = circulation rate, gpmDh = inside diameter of casing or hole size, in.Dp = outside diameter of pipe, tubing or collars, in.
Example: pump output = 530 gpmhole size = 12-l/4in.pipe OD = 4-l/2in.
AV = lOOft/min
Formula 3
Example: pump output = 12.6bbl/minhole size = 12-1/4 in.pipe OD = 4-l/2in.
AV = 99.92 ft/min
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Annular velocity (AV), ft/sec
Example: pump output = 12.6bbl/minhole size = 12-l/4in.pipe OD = 4-1/2 in.
AV = 1.6656 ft/sec
Metric calculations
Annular velocity, m/min = pump output, liter/min * annular volume, IAn
Annular velocity, m/sec = pump output, liter/min -s- 60 -s- annular volume, 1/m
S.I. units calculations
Annular velocity, m/min = pump output, m3/min -* annular volume, m3/m
Pump output, gpm, required for a desired annular velocity, ft/min
Pump output, gpm =
where AV = desired annular velocity, ft/minDh = inside diameter of casing or hole size, in.Dp = outside diameter of pipe, tubing or collars, in.
Example: desired annular velocity = 120 ft/minhole size = 12-1/4 in.pipe OD = 4-1/2 in.
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PO = 635.8gpm
Strokes per minute (SPM) required for a given annular velocity_ annular velocity, ft/min x annular capacity, bbl/ft
pump output, bbl/stk
Example: annular velocity = 120 ft/minannular capacity = 0.1261 bbl/ftDh = 12-1/4 in.Dp =4-1/2 in.pump output = 0.136 bbl/stk
_ 120ft/min x 0.1261bbl/ft0.136bbl/stk
SPM = 111.3
Capacity Formulas
Annular capacity between casing or hole and drill pipe, tubing,or casing
Dh2 - Dp2a) Annular capacity, bbl/ft =
Example: Hole size (Dh) = 12-l/4in.Drill pipe OD (Dp) = 5.0in.
12 252 - 5 O2Annular capacity, bbl/ft = : '-
Annular capacity = 0.12149bbl/ft
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1029.4b) Annular capacity, ft/bbl = -^"2\
Example: Hole size (Dh) = 12-l/4in.Drill pipe OD (Dp) = 5.0in.
1029 4Annular capacity, ft/bbl = ^2 _' 5 02\
Annular capacity = 8.23ft/bbl
c) Annular capacity, gal/ft = 24.51
Example: Hole size (Dh) = 12-1/4 in.Drill pipe OD (Dp) = 5.0in.
A i uft 1 2 - 2 5 2 - 5 - 2Annular capacity, gal/ft =Z*r.J 1
Annular capacity =5.1 gal/ft
24 51d) Annular capacity, ft/gal =
2 ^ p
Example: Hole size (Dh) = 12-1/4 in.Drill pipe OD (Dp) = 5.0in.
Annular capacity, ft/gal = ^2 '_ 5 Q2X
Annular capacity = 0.19598 ft/gal
Dh2 - Dp2e) Annular capacity, ft3/linft =
183.35Example: Hole size (Dh) = 12-1/4 in.
Drill pipe OD (Dp) = 5.0 in.12 252 5 O2Annular capacity, ft3/linft = ' '
Annular capacity = 0.682097ft3/linft
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f) Annular capacity, linft/ft3 = --: ^-
Example: Hole size (Dh) = 12-1/4 in.Drill pipe OD (Dp) = 5.0in.
Annular capacity, linft/ft3 = '_ Q
Annular capacity = 1.466 linft/ft3
Annular capacity between casing and multiple strings of tubing
a) Annular capacity between casing and multiple strings of tubing, bbl/ft:
Dh 2 - [(T1)2 + (T2)2IAnnular capacity, bbl/ft = -
Example: Using two strings of tubing of same size:Dh = casing7.0 in.29 lb/ft ID = 6.184 in.T1 = tubing No. 12-3/8 in. OD = 2.375 in.T2 = tubing No. 22-3/8 in. OD = 2.375 in.
. l i r 6.1842 - (2.3752 + 2.3752)Annular capacity, bbl/ft = -
A T uuiift 38 .24-11 .28Annular capacity, bbl/ft =
Annular capacity = 0.02619 bbl/ft
b) Annular capacity between casing and multiple strings of tubing, ft/bbl:
1029.4Annular capacity, ft/bbl = = ^ Dh 2 - [(T1)2 + (T2)2]
Example: Using two strings of tubing of same size:Dh = casing7.0 in.29 lb/ft ID = 6.184 in.T1 = tubing No. 12-3/8 in. OD = 2.375in.T2 = tubing No. 22-3/8 in. OD = 2.375 in.
1029 4Annular capacity, ft/bbl = ^ _ ^ 3 7 5 2 + ^37fi)
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1029 4Annular capacity, ft/bbl = :
F y 38.24-11.28
Annular capacity = 38.1816ft/bbl
c) Annular capacity between casing and multiple strings of tubing,gal/ft:
Dh 2 - [(T1)2 + (T2)2IAnnular capacity, gal/ft = -
Example: Using two tubing strings of different size:Dh = casing7.0 in.29 lb/ft ID = 6.184 in.T1 = tubing No. 12-3/8 in. OD = 2.375 in.T2 = tubing No. 23-1/2in. OD = 3.5in.
A 1 U I/ft 6 ' 1 8 4 2 " I 2 ' 3 7 5 ' + 3 - 5 ' )Annular capacity, gal/ft = - -
A i ,/* 3 8 . 2 4 - 1 7 . 8 9Annular capacity, gal/ft =
24.51Annular capacity = 0.8302733gal/ft
d) Annular capacity between casing and multiple strings of tubing,ft/gal:
Annular capacity, ft/gal = =' rrDh 2 - [(T1)2 + (T2)2]
Example: Using two tubing strings of different sizes:Dh = casing7.0 in.29 lb/ft ID = 6.184 in.T1 = tubing No. 12-3/8 in. OD = 2.375in.T2 = tubing No. 23-1/2in. OD = 3.5in.
Annular capacity, ft/gal = ^ 2 _ ^ 5 2 + 3 ^
Annular capacity, ft/gal = 3 8 2 4 '_ 1 ? 8 9
Annular capacity = 1.2044226 ft/gal
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e) Annular capacity between casing and multiple strings of tubing, ft3/linft:
Dh 2 - [(T1)2 + (T2)2IAnnular capacity, fr/linft = -
183.35Example: Using three strings of tubing:
Dh = casing9-5/8 in.471b/ft ID = 8.681 in.T1 = tubing No. 13-1/2in. OD = 3.5in.T2 = tubing No. 23-1/2in. OD = 3.5 in.T3 = tubing No. 33-1/2in. OD = 3.5in.
A , . 8.6812 - (3.52 + 3.52 + 3.52)Annular capacity = -
183.35
Annular capacity, ft3/linft = '
Annular capacity = 0.2105795 ft3/linftf) Annular capacity between casing and multiple strings of tubing, linft/ft3:
Annular capacity, linft/ft3 = '- Dh 2 - [(T1)2 + (T2)2]
Example: Using three strings tubing of same size:Dh = casing9-5/8 in.471b/ft ID = 8.681 in.T1 = tubing No. 13-1/2in. OD = 3.5in.T2 = tubing No. 23-1/2in. OD = 3.5in.T3 = tubing No. 33-1/2in. OD = 3.5in.
Annular capacity = 8.6812 _ ( 3 . " " 3.52 + 3.52)
Annular capacity, linft/ft3 = 7 5 3 5 9 1 3 6 7 5
Annular capacity = 4.7487993 linft/ft3
Capacity of tubulars and open hole: drill pipe, drill collars, tubing,casing, hole, and any cylindrical object
a) Capacity, bbl/ft = 1^j
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Example: Determine the capacity, bbl/ft, of a 12-1/4 in. hole:
Capacity, bbl/ft = ^^~F y 1029.4
Capacity = 0.1457766 bbl/ft
b) Capacity, ft/bbl = 19A
Example: Determine the capacity, ft/bbl, of 12-1/4 in. hole:1029 4
Capacity, ft/bbl = ~ r
Capacity = 6.8598ft/bbl
c) Capacity, gal/ft = ^
Example: Determine the capacity, gal/ft, of 8-1/2 in. hole:8 52Capacity, gal/ft = - ^ j -
Capacity = 2.9477764 gal/ft
d) Capacity, ft/gal = ~ - ^
Example: Determine the capacity, ft/gal, of 8-1/2 in. hole:
Capacity, ft/gal = '8.5
Capacity = 0.3392 ft/gal
ID2e) Capacity, ftVlinft = - ^ ^
Example: Determine the capacity, ftVlinft, for a 6.0 in. hole:
Capacity, ft3/linft = ^ ^
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Capacity =0.1963 ft 3/linft
183 35f) Capacity, linft/ft3 = | -^
Example: Determine the capacity, linft/ft3, for a 6.0 in. hole:
Capacity, linft/ft3 = ^ f ^
Capacity = 5.09305 linft/ft3
Amount of cuttings drilled per foot of hole drilled
a) BARRELS of cuttings drilled per foot of hole drilled:
Barrels = (1 - % porosity)
Example: Determine the number of barrels of cuttings drilled for onefoot of 12-l/4in.-hole drilled with 20% (0.20) porosity:
Barrels = ! ^ ( 1 - - 2 0 )
Barrels = 0.1457766 x 0.80Barrels = 0.1166213
b) CUBIC FEET of cuttings drilled per foot of hole drilled:
Dh2Cubic feet = x 0.7854 (1 - % porosity)
144Example: Determine the cubic feet of cuttings drilled for one foot of
12-1/4 in. hole with 20% (0.20) porosity:Cubic feet = )2^L
x 0.7854(1 - 0.20)144
Cubic feet = 1 5 0 6 2 6 x 0.7854 x 0.80144
Cubic feet = 0.6547727
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c) Total solids generated:W c g -350ChXL(I -P)SG
where Wcg = solids generated, poundsCh = capacity of hole, bbl/ftL = footage drilled, ftSG = specific gravity of cuttingsP = porosity, %
Example: Determine the total pounds of solids generated in drilling100ft of a 12-l/4in. hole (0.1458bbl/ft). Specific gravity ofcuttings = 2.40gm/cc. Porosity = 20%.
Wcg = 350 x 0.1458 x 100(1 - 0.20) x 2.4Wcg = 9797.26 pounds
Control Drilling
Maximum drilling rate (MDR), ft/hr, when drilling large diameterholes (14-3/4 in. and larger)
rn fmudwt _ mud wt^ j (circulation^MDR ft/hr = lout, ppg in, ppg J {rate, gpm J
Dh2
Example: Determine the MDR, ft/hr, necessary to keep the mud weightcoming out at 9.7 ppg at the flow line:
Data: Mud weight in = 9.0ppgCirculation rate = 530 gpmHole size = 17-1/2 in.
MDR, ft/hr = 6 7 C 9 - 7 - 9 - 0 ) 5 3 0
17.52
> ft/u 6 7 x 0 . 7 x 5 3 0MDR, ft/hr =
306.25
MDR = 81.16ft/hr
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Buoyancy Factor (BF)
Buoyancy factor using mud weight, ppg
B F = 65.5 - mud weight, ppg65.5
Example: Determine the buoyancy factor for a 15.0ppg fluid:
BF = 65-5 - 15-65.5
BF = 0.77099
Buoyancy factor using mud weight, Ib/ft3
_ 489 - mud weight, lb/ft3B F =
489
Example: Determine the buoyancy factor for a 120 lb/ft3 fluid:
OI7 489 - 120
BF = 0.7546
Hydrostatic Pressure (HP)Decrease When Pulling Pipe out of the Hole
When pulling DRY pipe
Step 1
Barrels n u m b e r average pipe,. . i = of stands x length per x displacement
displaced A x , jf , , , , , ,
^ pulled stand, ft bbl/ftStep 2
HP, psi = barrels displaced x 0 052 x m u d
decrease /casing pipe "\ ' weight, ppgcapacity, - displacement,
[bbl/ft bbl/ft J
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Example: Determine the hydrostatic pressure decrease when pulling DRYpipe out of the hole:
Number of stands pulled = 5Average length per stand = 92 ftPipe displacement = 0.0075 bbl/ftCasing capacity = 0.0773 bbl/ftMud weight = 11.5ppg
Stepl
Barrels 5 s t a n d s x 9 2 f t / s t d x 0.0075 bbl/ft
displacedBarrels ^ 3 4 5displaced
Step 2
HP,psi 3.45 barrelsdecrease = ^.0773 - 0.0075^ X -0 5 2 X 1 L 5 p p g
Ubl/ft bbl/ft JHP,psi 3.45 barrelsA
F = x 0.052 x 11.5ppgdecrease 0.0698
1 P = 29.56psidecrease
When pulling WET pipe
Step 1
R . number average fpipe disp., bbl/ft ^barrels
o f s t a n d g x l e n g t h p e r x +aispiacea
p u l l e d ^ ^ ft ^ p i p e c a p ? b b ] / f t j
Step 2
_ barrels displaced o n s ? mud
'P " ^casing A f pipe disp., bbl/ft^ weight,ppg
capacity, - +(,bbl/ft J l^ pipe cap., bbl/ft J
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Example: Determine the hydrostatic pressure decrease when pullingWET pipe out of the hole:
Number of stands pulled = 5Average length per stand = 92 ftPipe displacement = 0.0075 bbl/ftPipe capacity =0.01776bbl/ftCasing capacity = 0.0773 bbl/ftMud weight = 11.5ppg
Stepl
f 0.0075 bbl/ft i^Barrels
5 s t a n d s x 9 2 f t / s t d x +d l s P l a c e d [o.O1776bbl/ftJBarrels
= H^6 1 9 6displaced
Step 2
HP, psi 11.6196 barrels
Ibbl/ft J [0.01776bbl/ftJHP, psi 1L6196, ^ = x 0.052 x 11.5ppg
decrease 0.05204TTp^
1 = 133.52psi
decrease
Loss of Overbalance Due to Falling Mud Level
Feet of pipe pulled DRY to lost overbalance_ overbalance, psi (casing cap. - pipe disp., bbl/ft)
mud wt., ppg x 0.052 x pipe disp., bbl/ftExample: Determine the FEET of DRY pipe that must be pulled to lose
the overbalance using the following data:
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Amount of overbalance = 150psiCasing capacity = 0.0773 bbl/ftPipe displacement = 0.0075 bbl/ftMud weight =11.5 ppg
Feet of pipe pulled WET to lose overbalance
_ overbalance, psi x (casing cap. - pipe cap. - pipe disp.)mud wt., ppg x 0.052 x (pipe cap. + pipe disp., bbl/ft)
Example: Determine the feet of WET pipe that must be pulled to losethe overbalance using the following data:
Amount of overbalance = 150 psiCasing capacity = 0.0773 bbl/ftPipe capacity =0.01776 bbl/ftPipe displacement = 0.0075 bbl/ftMud weight =11.5 ppg
Metric calculations
_ j drilling fluid ^ metal displacement, ^ n nQQ1Pressure drop per , ^ ,
n x ^ x 0.0981A . . ^
F density, kg/1 1/m
meter tripping = r - : r~r;dry pipe, bar/m ^ m g C a p a C l t y ' - t a l d l s P l a c e m e n t '
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, drilling fluid ^ metal displacement, v n nQQ1Pressure drop per , ..
u , x ^ x 0.098I. .
F F density, bar/m 1/m
meter tripping = : TT.:
, , , casing capacity, metal displacement,dry pipe, bar/m ^ -
y m
f metal disp., 1/m Adrilling fhaid
x + I 0 0 9 8 1Pressure drop per density, kg/1 I j
c k ^ Imeter tripping = ^ - F .
u J
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^ . f T annular capacity, 1/mwet pipe, bar/m v J'
n . , /^ metal disp., 1/m ^drilling fluid I f^
Pressure drop per density, bar/m I 1 {i ymjmeter tripping = , v r-^ ^
. . u , annular capacity,
wet pipe, bar/m .. ^ J9Level drop for _ length of drill collars, m x metal disp., 1/mPOOH drill collars ~ casing capacity, 1/m
S.I. units calculations
drilling fluid metal disp.,Pressure drop per density, kg/m* X mVmmeter tripping =
: ^f -rr.i . , j^ , casing capacity, metal disp., . . .dry pipe, kPa/m & ^ J - x 102m3/m m3/mA -Ii a -A /"metal disp., m3/m "\drilling fluid *_
Pressure drop per density, kg/m3 I p i p e c a p a c i t y ? m 3 / m
meter tripping = ; ^ :
wet pipe, kPa/m anfular c aP a c i ty' x 102nr/m
Level drop for POOH _ length of drill collars, m x metal disp., m3/mdrill collars, m casing capacity, m3/m
Formation Temperature (FT)
fambient ^ ,. x
o _ /temperature |N }
, a C e
+ OA ^increase 0F per ft of depth x TVD, ftJVtemperature, 0Fy v v v y
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Example: If the temperature increase in a specific area is 0.012F/ft ofdepth and the ambient surface temperature is 700F, determinethe estimated formation temperature at a TVD of 15,000ft:
FT, 0F = 700F + (0.012F/ft x 15,000ft)FT, 0F = 700F + 1800FFT = 2500F (estimated formation temperature)
Hydraulic Horsepower (HHP)
HHP = i ^ r
1714where HHP = hydraulic horsepower
P = circulating pressure, psiQ = circulating rate, gpm
Example: circulating pressure = 2950 psicirculating rate = 520 gpm
HHP = 2 9 5 X 5 2 1714
HHP = 1^5 3 4 '0 0 01714
HHP = 894.98
Drill Pipe/Drill Collar Calculations
Capacities, bbl/ft, displacement, bbl/ft, and weight, lb/ft, can becalculated from the following formulas:
Capacity, bbl/ft = 1^-
T^ 1 UUI/ft O D > i n * 2 ~ I D > m ' 2
Displacement, bbl/ft =F 1029.4
Weight, lb/ft = displacement, bbl/ft x 27471b/bbl
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Example: Determine the capacity, bbl/ft, displacement, bbl/ft, and weight,lb/ft, for the following:
Drill collar OD = 8.0in.Drill collar ID = 2-13/16in.Convert 13/16 to decimal equivalent:13 + 16 = 0.8125
2 81252a) Capacity, bbl/ft = ^ 2 9 ^
Capacity = 0.007684 bbl/ft8 O2 - 2 81252
b) Displacement, bbl/ft = :
T .^ 1 m i r 56.089844Displacement, bbl/ft =
y 1029.4
Displacement = 0.0544879 bbl/ftc) Weight, lb/ft = 0.0544879bbl/ftx27471b/bbl
Weight = 149.6781b/ft
Rule of thumb formulas
Weight, lb/ft, for REGULAR DRILL COLLARS can be approximatedusing the following formula:
Weight, lb/ft = (OD, in.2 - ID, in.2) 2.66
Example: Regular drill collarsDrill collar OD = 8.0in.Drill collar ID = 2-13/16in.Decimal equivalent = 2.8125 in.Weight, lb/ft - (8.02 - 2.81252) 2.66Weight, lb/ft = 56.089844 x 2.66Weight = 149.19898 lb/ft
Weight, lb/ft, for SPIRAL DRILL COLLARS can be approximated usingthe following formula:
Weight, lb/ft = (OD, in.2 - ID, in.2) 2.56
-
Example: Spiral drill collarsDrill collar OD = 8.0in.Drill collar ID = 2-13/16 in.Decimal equivalent = 2.8125 in.Weight, lb/ft = (8.02 - 2.81252) 2.56Weight, lb/ft = 56.089844 x 2.56Weight = 143.59 lb/ft
Pump Pressure/Pump Stroke Relationship(Also Called the Roughneck's Formula)
Basic formula
New circulating =
V^i{ x (^ new pump rate, spm V
pressure, psi pressure, psi ^ o l d P u mP r a t e ' s P m '
Example: Determine the new circulating pressure, psi using the follow-ing data:
Present circulating pressure = 1800 psiOld pump rate = 60spmNew pump rate = 30spm
New circulating = 1 8 0 0 j p O s p m f
pressure, psi p V60spmJ
Newcirculating = 1 8 0 s i x Q 2 5
pressure, psiNew circulating
= .
pressure
Determination of exact factor in above equation
The above formula is an approximation because the factor 2 is a rounded-off number. To determine the exact factor, obtain two pressure readings atdifferent pump rates and use the following formula:
_ log (pressure 1 -*- pressure 2)log (pump rate 1 * pump rate 2)
-
Example: Pressure 1 = 2500 psi @ 315 gpmPressure 2 = 450 psi @ 120 gpm
F a c t o r = log (2500psi + 450psi)log (315gpm + 120gpm)
Factor = to ^ 5 5 5 5 5 5 6 >log (2.625)
Factor = 1.7768
Example: Same example as above but with correct factor:
New circulating _ IOQQ pOspmV'7768pressure, psi " pS1 V60spmJ
New circulating = 18OOpsi x 0.2918299
pressure, psiNew circulating _ ^ c pressure
Metric calculation
new pump pressure with _ current (new SPM^jnew pump strokes, bar ~ pressure, bar ^
old SPM J
S.I. units calculation
new pump pressure with _ current (new SPM^jnew pump strokes, kPa ~ pressure, kPa ^
old SPM J
Cost per Foot
Example: Determine the drilling cost (Cx), dollars per foot, using thefollowing data:
-
Bit cost (B) = $2500Rig cost (CR) = $900/hourRotating time (T) = 65 hoursRound trip time (T) = 6 hours(for depth10,000 ft)Footage per bit (F) = 1300 ft
_ 2500 + 900(65 + 6)T " 1300
= 66,400T ~ 1300
CT = $51.08 per foot
Temperature Conversion Formulas
Convert temperature, Fahrenheit (F) to Centigrade or Celsius (C)
C0F - 32) 50C = ^ - -^- OR 0C = 0F - 32 x 0.5556
Example: Convert 95 0F to 0C:
0C = ( 9 5 ~ 3 2 ) 5 OR 0C = 95 - 32 x 0.5556
0C = 35 0C = 35
Convert temperature, Centigrade or Celsius (C) to Fahrenheit
0F = ( C X 9^ + 32 OR 0F = 0C x 1.8 + 32
Example: Convert 24 0C to 0F
oF = (24>^9) + 3 2 Q R oF = 2 4 x L 8 + 32
0F = 75.2 0F = 75.2
Convert temperature, Centigrade, Celsius (C) to Kelvin (K)0K = 0C H- 273.16
-
Example: Convert 35 0C to 0K:0K = 35 + 273.160K = 308.16
Convert temperature, Fahrenheit (F) to Rankine (R)0R = 0F + 459.69
Example: Convert 2600F to 0R:0R = 260 + 459.690R = 719.69
Rule of thumb formulas for temperature conversion
a) Convert 0F to 0C0C = 0F - 30 * 2
Example: Convert 95 0F to 0C:0C = 95 - 30 + 20C = 32.5
b) Convert 0C to 0F0F = 0C + 0C + 30
Example: Convert 24 0C to 0F:0F = 24 + 24 + 300F = 78
Front MatterTable of Contents1. Basic FormulasPressure GradientHydrostatic Pressure (HP)Converting Pressure into Mud WeightSpecific Gravity (SG)Equivalent Circulating Density (ECD)Maximum Allowable Mud Weight from Leak-off Test DataPump Output (PO)Annular Velocity (AV)Capacity FormulasControl DrillingBuoyancy Factor (BF)Hydrostatic Pressure (HP) Decrease When Pulling Pipe Out of the HoleLoss of Overbalance Due to Falling Mud LevelFormation Temperature (FT)Hydraulic Horsepower (HHP)Drill Pipe/Drill Collar CalculationsPump Pressure/Pump Stroke Relationship (Also Called the Roughneck's Formula)Cost per FootTemperature Conversion Formulas
Index