aerated annular pressures

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document.xls MITCHELL ENGINEERING PROGRAMS Page COPYRIGHT 1990 MITCHELL ENGINEERING, PO BOX 1492. GOLDEN, CO, 80402, USA (303) 273 3744 Aerated Annular Pressures WHILE CIRCULATING AERATED MUD THE HUGHES TOOL CO. - H B WOODS EQUATION REF: Bobo, Ormsby, Hoch; "Phillips Tests Air-Mud Drilling",OIL AND GAS JOURNAL, Feb. 7, 1955, p. 108 SELECTED INPUT VARIABLES Symbols Values Descriptions of Input Variables -------- -------- ------------------------------------------------- Qm 16.957 cu ft of mud circulated/minute; scf/m Qa 678.261 cu ft of std. air circulated/minute; cf/m rho air .07642 density of free atmospheric air; lb/cf rho mud 65.824 density of mud; lb/cf Dh 8.500 diameter of hole; in Dp 4.500 OD of drillpipe; in Po 14.7 pressure at the flow line entry; psia Temp 60 temperature of atmospheric air; deg F AV 60 desired annular velocity of mud; ft/m Air/mud 40 air/mud injection ratio; scf/cf COMPUTED INTERMEDIATE VARIABLES A .488 '= 0.00708*((C9/C8)*C10+C11) B 600.300 '= 15*((C9/C8)+0.02) C .00115 '= 0.00063*C8^2*((C9/C8)*C10+C11) /((C12-C13)*(C12^2-C13^2)^2) A+C .48883 '= C18+C20 C*B .69249 '= C20*C19 A*C .00056 '= C18*C20 radian 57.29578 '= 180/PI() TABLE OF PRESSURE V. DEPTH Pressure Depth Gradient 'Depth' at which pressure occurs; ft 15 5 1.15 /($B$21*$B$14^2+2*$B$22*$B$14+$B$22^2))) 100 1491 1.10 -(2*$B$19*SQRT($B$23)/$B$21^2) 200 2482 1.44 *($B$24*ATAN(($B$21*B34+$B$22) 800 5373 2.81 /($B$19*SQRT($B$23)))-$B$24 1,600 7853 3.89 *ATAN(($B$21*$B$14+$B$22) 1,800 8405 4.09 /($B$19*SQRT($B$23))))) 2,000 8943 4.27 2,500 10238 4.67

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Page 1: Aerated Annular Pressures

document.xls MITCHELL ENGINEERING PROGRAMS

Page

COPYRIGHT 1990 MITCHELL ENGINEERING, PO BOX 1492. GOLDEN, CO, 80402, USA (303) 273 3744

Aerated Annular PressuresWHILE CIRCULATING AERATED MUD

THE HUGHES TOOL CO. - H B WOODS EQUATION

REF: Bobo, Ormsby, Hoch; "Phillips Tests Air-Mud

Drilling",OIL AND GAS JOURNAL, Feb. 7, 1955, p. 108

SELECTED INPUT VARIABLESSymbols Values Descriptions of Input Variables

-------- -------- -----------------------------------------------------------

Qm 16.957 cu ft of mud circulated/minute; scf/m

Qa 678.261 cu ft of std. air circulated/minute; cf/m

rho air .07642 density of free atmospheric air; lb/cf

rho mud 65.824 density of mud; lb/cf

Dh 8.500 diameter of hole; in

Dp 4.500 OD of drillpipe; in

Po 14.7 pressure at the flow line entry; psia

Temp 60 temperature of atmospheric air; deg F

AV 60 desired annular velocity of mud; ft/m

Air/mud 40 air/mud injection ratio; scf/cf

COMPUTED INTERMEDIATE VARIABLESA .488 '= 0.00708*((C9/C8)*C10+C11)

B 600.300 '= 15*((C9/C8)+0.02)

C .00115 '= 0.00063*C8^2*((C9/C8)*C10+C11)

/((C12-C13)*(C12^2-C13^2)^2)

A+C .48883 '= C18+C20

C*B .69249 '= C20*C19

A*C .00056 '= C18*C20

radian 57.29578 '= 180/PI()

TABLE OF PRESSURE V. DEPTHPressure Depth Gradient 'Depth' at which pressure occurs; ft

15 5 1.15 /($B$21*$B$14^2+2*$B$22*$B$14+$B$22^2)))

100 1491 1.10 -(2*$B$19*SQRT($B$23)/$B$21^2)

200 2482 1.44 *($B$24*ATAN(($B$21*B34+$B$22)

800 5373 2.81 /($B$19*SQRT($B$23)))-$B$24

1,600 7853 3.89 *ATAN(($B$21*$B$14+$B$22)

1,800 8405 4.09 /($B$19*SQRT($B$23)))))

2,000 8943 4.27

2,500 10238 4.67

Page 2: Aerated Annular Pressures

document.xls MITCHELL ENGINEERING PROGRAMS

Page

Air Pressure Loss in Rig Piping

Press of Compressed Air 100 psig

Temp of Compressed Air 100 °F

Flow Rate 1500 c.f.m.

Pipe ID 3 in

Length of Pipe 100 ft

Flow Rate of Compressed Air 207.0 c.f.m.

Velocity of Compressed Air 70.3 f.p.s.

Density of Air @ P & T 0.5535 lbs/ft³

Friction Factor 0.0105

Pressure Drop of Compressed Air 1.24 psi/100ft

Compressor Horsepower OutputNumber of Stages 3Compressor Intake Pressure 14.7 psia

Compressor Discharge Pressure 350 psia

Compressor Intake Air Temperature 530 deg R

Metered Air Flow Rate 600 scf/m

Metered Air Temperature 540 deg R

Metered Air Pressure 348 psia

Compressor Horsepower 219 hp

intake

dischargemetercompressor

injection