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let 80- 0S
Formation Testing Service Report
middot I
HALLIBURTON SERVICES DUNCAN OKLAHOMA
~~
Ticket 00 FLU I D SAMPLE DATA 6-17-80 696590 0
Dote Number 2shy~
Sampler Pressure PSIG at Surface Kind Halliburton 0
0
Recovery Cu Ft Go of DST OPEN HOLE Location POWELL = ~o
K TKUUIH cc Oil 9
ce Woter Tester B WILSON Witness
ce Mud N Drilling Tot liQuid cc Contractor LOFFLANO ORILLING Ie
Gravity API F EQUIPMENT amp H 0 L E DATA (J1
GasOil Ratio cu ft bbl Formation Tested Nugget Vgt
RESISTIVITY CHLORIDE Elevotion 6753 Ft CONTENT 100
Net Productive Interval Ft
Recovery Woter __ __ F ppm Ke11 y Bushin9 6781 1
All Depths Measured From Recovery Mud __ __ F ppm Total Depth 12475 Ft rn
Recovery Mud Filtrate __ __ F ppm Moin HoleCasing Size 8 12 Mud Pit Sample __ __ F Drill COllar length 6215 ID 250
ppm 1171309 JD 3826
Mud Pit Sample Filtrate F Drill Pipe Length ppm 12370 12375 Packer Depth(s) - Fe Mud Weight vis sec Depth Tester Valve 1234559 Ft
TYPE AMOUNT Depth Bock Surface Bottom 34Cushion Water 5000 Ft Pres Valve Choke 18 Choke
Recovered Feet of ~~
lt g~bullp
Recovered Feet of ~ a 3
Recovered Feet of Ii E ~ -rshylt Cl
Recovered Feet of 0 0shybull t shy
-I Recovered Feet of
Remarks - MISRIJN - NO PACKER SFAT -
_ lt~~ PRonllrTTON T~ltT nATAltH~FT _
- 0 a lt
Gouge No 326 Gauge No 7485 Gouge No 202 TIME TEMPERATURE
1lt~O 1lt~4 12472 (0000-2lt100 hrs) 0Death Ft Denth Ft Denth Ft t shy
4 Hour Clock 24 Hour Clock 24 Hour Clock Tool -Est F Blanked Off Nn Blanked Off Nn Blanked Off Yes Ooened 840 0gt 0
Opened c
Actuol 221 F Pressures Pressures Pressures Bypass
Field Office Field Office Field Office Reported Computed
Initiol Hydrostatic 58882 59169 59664 Minutes Minutes f-Initiol - shy - shy ~
E] Flow lt - Finol ~ ~
C1~scd in -
Initiol Cl Co Flow t-Smiddot Finol r Ifi 0
Closed in
Initial - shy - shy
~g Flow Final
~tf Closed in
Final Hydrostatic ~RRR 5916 Q 5966 4
I nlNUO IN us FORMATION TEST DATA mo ~
shy r shyr
shyr-
~Vgt o a Om
0Crshyrn deg3 c ~3
lt0 zo e 3 o 0t shy
z -lt
fOIM 111_U _
0-1
Casing perfs Bottom choke
Gos gravity Oil gravity
Spec gravity Chlorides
INDICATE TYPE AND SIZE OF GAS MEASURING DEVICE USED
Surf temp
GOR
ppm Res
of
Ticket No
of
696590
Dote
Time
2200
am pm
Choke Size
Surface Pressure
pgti
Go Rate MCF
liquid Rote BPD
On location
Remarks
2400 Picked up tools
0130 Started in hal e
Ran 5000 of water cushion
0800 Pi cked up control head - rigged up
manifol d
0840 Opened tool - 51 i gh t blow in bubble
bucket - lost packer seat 3 minutes
into flow period Pulled off bottom
Tried to reset packers - wouldnt hole
0930 Sta rted out of hole
1200 Reversed out water cushion
1330 Started out of hole
1630 Out of hole - laid down tools
1700 Job completed
PRODUCTION TEST DATA
eDrill Pipe or Tubing
Drill CollorsIII Reersing Sub Woter Cushion Valve
X-OVerDrill Pipe X-OVerDrill Collars
Horldling Sub amp Choke Assembly X-Over Dual ClP Valve
Duol C1P Sampler
Hydro_Spring Tester
Multiple CIP Sampler
III Extension Joint if
AP Running Case I III Hydroulk Jar
Ilj VR Sofety Joint (0 Pressure Equalizing Crossover
II I
Packer Assembly
Distributor
Packer Assembly
Flush JOint Anchor
Pressure Equalizing Tube
Blanked-Off BT Running Case
Drill Collors
Anchor Pipe Safety Joint
Packer Assembly
Distributor
Packer Assembly
X-Over I Anchor Pipe Safety Joint X-Over
Ivl Side Wall Anchor Drill Co11ars X-Over
Drill Collars X~Over
Flush Joint Anchor
Blanked-Off BT Running Case
Totol Depth
5
5
5
511
511
7 34
7 34
5 5 11 16 6 all
6 34 5 78 5 34
5
5
1 D
3826 250
250 2 716 2 516 2 18
87
75
375
375
1 75
100
1 53
153
1 50 11
2 18
TICKET NO 696590
LENGTH
1171309 5905
DEPTH
1230374
3deg675I 10 I 0
70 1233859
00
4 12 6 34
4 38 60 5 34 4 34
5 50
40
40
50
260
580
580
4 0 1 0
2 71 6 1 0
250 6150 3 516 1 0 2 S1l6 10
2 37 250
2 75 11 4 0
1234559
1235059
1235459
12370
1237581
12472
12475
0 _12 _ NYU) IN ~SA EQUIPMENT DATA
NOMENCLATURE
b == Approximate Radius of Investigation middot Feet
b 1 == Approximate Radius of Investigation (Net Pay Zone hi) middot Feet
DR == Damage Ratio
EI == Elevation middot Feet
GO == BT Gauge Depth (from Surface Reference) Feet
h == Interval Tested Feet
h _ Net Pay Thickness middot Feet
K Permeability _bullbull md
Permeability (From Net Pay Zone hI) md
m Slope Extrapolated Pressure Plot (Psi1Jcycie Gas) middot psicycle
OF 1 == Maximum Indicated Flow Rate MCFD
OF 2 == Minimum Indicated Flow Rate MCFD
OF3 == Theoretical Open Flow Potential withDamage Removed Max MeFfO
OF4 = Theoretical Open Flow Potential withDamage Removed Min MeFfD
== Extrapolated Stotic Pressure Psig
Final Flow Pressure Psig
Potentiometric Surface (Fresh Watermiddot ) Pot - Feet
Q = Average Adjusted Production Rate During Test bblday
Q 1 = Theoretical Production w Damage Remo ed middot bblday
Q = Measured Gas Production Rate MCFD
R == Corrected Recovery bbl
= Radius of Well Bore Feet
t = Flow Time bullbull Minutes
t bull = Total Flow Time Minutes
T Temperature Rankine OR
Z = Compressibility Factor
p Viscosity Gas or liquid middot CP
Log - Common log
bull Potentiometric Surface Reference to Rotary Table When Elevation Not Given Fresh Woter Corrected to 100 F
~~
Ticket 00 FLU I D SAMPLE DATA 6-17-80 696590 0
Dote Number 2shy~
Sampler Pressure PSIG at Surface Kind Halliburton 0
0
Recovery Cu Ft Go of DST OPEN HOLE Location POWELL = ~o
K TKUUIH cc Oil 9
ce Woter Tester B WILSON Witness
ce Mud N Drilling Tot liQuid cc Contractor LOFFLANO ORILLING Ie
Gravity API F EQUIPMENT amp H 0 L E DATA (J1
GasOil Ratio cu ft bbl Formation Tested Nugget Vgt
RESISTIVITY CHLORIDE Elevotion 6753 Ft CONTENT 100
Net Productive Interval Ft
Recovery Woter __ __ F ppm Ke11 y Bushin9 6781 1
All Depths Measured From Recovery Mud __ __ F ppm Total Depth 12475 Ft rn
Recovery Mud Filtrate __ __ F ppm Moin HoleCasing Size 8 12 Mud Pit Sample __ __ F Drill COllar length 6215 ID 250
ppm 1171309 JD 3826
Mud Pit Sample Filtrate F Drill Pipe Length ppm 12370 12375 Packer Depth(s) - Fe Mud Weight vis sec Depth Tester Valve 1234559 Ft
TYPE AMOUNT Depth Bock Surface Bottom 34Cushion Water 5000 Ft Pres Valve Choke 18 Choke
Recovered Feet of ~~
lt g~bullp
Recovered Feet of ~ a 3
Recovered Feet of Ii E ~ -rshylt Cl
Recovered Feet of 0 0shybull t shy
-I Recovered Feet of
Remarks - MISRIJN - NO PACKER SFAT -
_ lt~~ PRonllrTTON T~ltT nATAltH~FT _
- 0 a lt
Gouge No 326 Gauge No 7485 Gouge No 202 TIME TEMPERATURE
1lt~O 1lt~4 12472 (0000-2lt100 hrs) 0Death Ft Denth Ft Denth Ft t shy
4 Hour Clock 24 Hour Clock 24 Hour Clock Tool -Est F Blanked Off Nn Blanked Off Nn Blanked Off Yes Ooened 840 0gt 0
Opened c
Actuol 221 F Pressures Pressures Pressures Bypass
Field Office Field Office Field Office Reported Computed
Initiol Hydrostatic 58882 59169 59664 Minutes Minutes f-Initiol - shy - shy ~
E] Flow lt - Finol ~ ~
C1~scd in -
Initiol Cl Co Flow t-Smiddot Finol r Ifi 0
Closed in
Initial - shy - shy
~g Flow Final
~tf Closed in
Final Hydrostatic ~RRR 5916 Q 5966 4
I nlNUO IN us FORMATION TEST DATA mo ~
shy r shyr
shyr-
~Vgt o a Om
0Crshyrn deg3 c ~3
lt0 zo e 3 o 0t shy
z -lt
fOIM 111_U _
0-1
Casing perfs Bottom choke
Gos gravity Oil gravity
Spec gravity Chlorides
INDICATE TYPE AND SIZE OF GAS MEASURING DEVICE USED
Surf temp
GOR
ppm Res
of
Ticket No
of
696590
Dote
Time
2200
am pm
Choke Size
Surface Pressure
pgti
Go Rate MCF
liquid Rote BPD
On location
Remarks
2400 Picked up tools
0130 Started in hal e
Ran 5000 of water cushion
0800 Pi cked up control head - rigged up
manifol d
0840 Opened tool - 51 i gh t blow in bubble
bucket - lost packer seat 3 minutes
into flow period Pulled off bottom
Tried to reset packers - wouldnt hole
0930 Sta rted out of hole
1200 Reversed out water cushion
1330 Started out of hole
1630 Out of hole - laid down tools
1700 Job completed
PRODUCTION TEST DATA
eDrill Pipe or Tubing
Drill CollorsIII Reersing Sub Woter Cushion Valve
X-OVerDrill Pipe X-OVerDrill Collars
Horldling Sub amp Choke Assembly X-Over Dual ClP Valve
Duol C1P Sampler
Hydro_Spring Tester
Multiple CIP Sampler
III Extension Joint if
AP Running Case I III Hydroulk Jar
Ilj VR Sofety Joint (0 Pressure Equalizing Crossover
II I
Packer Assembly
Distributor
Packer Assembly
Flush JOint Anchor
Pressure Equalizing Tube
Blanked-Off BT Running Case
Drill Collors
Anchor Pipe Safety Joint
Packer Assembly
Distributor
Packer Assembly
X-Over I Anchor Pipe Safety Joint X-Over
Ivl Side Wall Anchor Drill Co11ars X-Over
Drill Collars X~Over
Flush Joint Anchor
Blanked-Off BT Running Case
Totol Depth
5
5
5
511
511
7 34
7 34
5 5 11 16 6 all
6 34 5 78 5 34
5
5
1 D
3826 250
250 2 716 2 516 2 18
87
75
375
375
1 75
100
1 53
153
1 50 11
2 18
TICKET NO 696590
LENGTH
1171309 5905
DEPTH
1230374
3deg675I 10 I 0
70 1233859
00
4 12 6 34
4 38 60 5 34 4 34
5 50
40
40
50
260
580
580
4 0 1 0
2 71 6 1 0
250 6150 3 516 1 0 2 S1l6 10
2 37 250
2 75 11 4 0
1234559
1235059
1235459
12370
1237581
12472
12475
0 _12 _ NYU) IN ~SA EQUIPMENT DATA
NOMENCLATURE
b == Approximate Radius of Investigation middot Feet
b 1 == Approximate Radius of Investigation (Net Pay Zone hi) middot Feet
DR == Damage Ratio
EI == Elevation middot Feet
GO == BT Gauge Depth (from Surface Reference) Feet
h == Interval Tested Feet
h _ Net Pay Thickness middot Feet
K Permeability _bullbull md
Permeability (From Net Pay Zone hI) md
m Slope Extrapolated Pressure Plot (Psi1Jcycie Gas) middot psicycle
OF 1 == Maximum Indicated Flow Rate MCFD
OF 2 == Minimum Indicated Flow Rate MCFD
OF3 == Theoretical Open Flow Potential withDamage Removed Max MeFfO
OF4 = Theoretical Open Flow Potential withDamage Removed Min MeFfD
== Extrapolated Stotic Pressure Psig
Final Flow Pressure Psig
Potentiometric Surface (Fresh Watermiddot ) Pot - Feet
Q = Average Adjusted Production Rate During Test bblday
Q 1 = Theoretical Production w Damage Remo ed middot bblday
Q = Measured Gas Production Rate MCFD
R == Corrected Recovery bbl
= Radius of Well Bore Feet
t = Flow Time bullbull Minutes
t bull = Total Flow Time Minutes
T Temperature Rankine OR
Z = Compressibility Factor
p Viscosity Gas or liquid middot CP
Log - Common log
bull Potentiometric Surface Reference to Rotary Table When Elevation Not Given Fresh Woter Corrected to 100 F
Casing perfs Bottom choke
Gos gravity Oil gravity
Spec gravity Chlorides
INDICATE TYPE AND SIZE OF GAS MEASURING DEVICE USED
Surf temp
GOR
ppm Res
of
Ticket No
of
696590
Dote
Time
2200
am pm
Choke Size
Surface Pressure
pgti
Go Rate MCF
liquid Rote BPD
On location
Remarks
2400 Picked up tools
0130 Started in hal e
Ran 5000 of water cushion
0800 Pi cked up control head - rigged up
manifol d
0840 Opened tool - 51 i gh t blow in bubble
bucket - lost packer seat 3 minutes
into flow period Pulled off bottom
Tried to reset packers - wouldnt hole
0930 Sta rted out of hole
1200 Reversed out water cushion
1330 Started out of hole
1630 Out of hole - laid down tools
1700 Job completed
PRODUCTION TEST DATA
eDrill Pipe or Tubing
Drill CollorsIII Reersing Sub Woter Cushion Valve
X-OVerDrill Pipe X-OVerDrill Collars
Horldling Sub amp Choke Assembly X-Over Dual ClP Valve
Duol C1P Sampler
Hydro_Spring Tester
Multiple CIP Sampler
III Extension Joint if
AP Running Case I III Hydroulk Jar
Ilj VR Sofety Joint (0 Pressure Equalizing Crossover
II I
Packer Assembly
Distributor
Packer Assembly
Flush JOint Anchor
Pressure Equalizing Tube
Blanked-Off BT Running Case
Drill Collors
Anchor Pipe Safety Joint
Packer Assembly
Distributor
Packer Assembly
X-Over I Anchor Pipe Safety Joint X-Over
Ivl Side Wall Anchor Drill Co11ars X-Over
Drill Collars X~Over
Flush Joint Anchor
Blanked-Off BT Running Case
Totol Depth
5
5
5
511
511
7 34
7 34
5 5 11 16 6 all
6 34 5 78 5 34
5
5
1 D
3826 250
250 2 716 2 516 2 18
87
75
375
375
1 75
100
1 53
153
1 50 11
2 18
TICKET NO 696590
LENGTH
1171309 5905
DEPTH
1230374
3deg675I 10 I 0
70 1233859
00
4 12 6 34
4 38 60 5 34 4 34
5 50
40
40
50
260
580
580
4 0 1 0
2 71 6 1 0
250 6150 3 516 1 0 2 S1l6 10
2 37 250
2 75 11 4 0
1234559
1235059
1235459
12370
1237581
12472
12475
0 _12 _ NYU) IN ~SA EQUIPMENT DATA
NOMENCLATURE
b == Approximate Radius of Investigation middot Feet
b 1 == Approximate Radius of Investigation (Net Pay Zone hi) middot Feet
DR == Damage Ratio
EI == Elevation middot Feet
GO == BT Gauge Depth (from Surface Reference) Feet
h == Interval Tested Feet
h _ Net Pay Thickness middot Feet
K Permeability _bullbull md
Permeability (From Net Pay Zone hI) md
m Slope Extrapolated Pressure Plot (Psi1Jcycie Gas) middot psicycle
OF 1 == Maximum Indicated Flow Rate MCFD
OF 2 == Minimum Indicated Flow Rate MCFD
OF3 == Theoretical Open Flow Potential withDamage Removed Max MeFfO
OF4 = Theoretical Open Flow Potential withDamage Removed Min MeFfD
== Extrapolated Stotic Pressure Psig
Final Flow Pressure Psig
Potentiometric Surface (Fresh Watermiddot ) Pot - Feet
Q = Average Adjusted Production Rate During Test bblday
Q 1 = Theoretical Production w Damage Remo ed middot bblday
Q = Measured Gas Production Rate MCFD
R == Corrected Recovery bbl
= Radius of Well Bore Feet
t = Flow Time bullbull Minutes
t bull = Total Flow Time Minutes
T Temperature Rankine OR
Z = Compressibility Factor
p Viscosity Gas or liquid middot CP
Log - Common log
bull Potentiometric Surface Reference to Rotary Table When Elevation Not Given Fresh Woter Corrected to 100 F
eDrill Pipe or Tubing
Drill CollorsIII Reersing Sub Woter Cushion Valve
X-OVerDrill Pipe X-OVerDrill Collars
Horldling Sub amp Choke Assembly X-Over Dual ClP Valve
Duol C1P Sampler
Hydro_Spring Tester
Multiple CIP Sampler
III Extension Joint if
AP Running Case I III Hydroulk Jar
Ilj VR Sofety Joint (0 Pressure Equalizing Crossover
II I
Packer Assembly
Distributor
Packer Assembly
Flush JOint Anchor
Pressure Equalizing Tube
Blanked-Off BT Running Case
Drill Collors
Anchor Pipe Safety Joint
Packer Assembly
Distributor
Packer Assembly
X-Over I Anchor Pipe Safety Joint X-Over
Ivl Side Wall Anchor Drill Co11ars X-Over
Drill Collars X~Over
Flush Joint Anchor
Blanked-Off BT Running Case
Totol Depth
5
5
5
511
511
7 34
7 34
5 5 11 16 6 all
6 34 5 78 5 34
5
5
1 D
3826 250
250 2 716 2 516 2 18
87
75
375
375
1 75
100
1 53
153
1 50 11
2 18
TICKET NO 696590
LENGTH
1171309 5905
DEPTH
1230374
3deg675I 10 I 0
70 1233859
00
4 12 6 34
4 38 60 5 34 4 34
5 50
40
40
50
260
580
580
4 0 1 0
2 71 6 1 0
250 6150 3 516 1 0 2 S1l6 10
2 37 250
2 75 11 4 0
1234559
1235059
1235459
12370
1237581
12472
12475
0 _12 _ NYU) IN ~SA EQUIPMENT DATA
NOMENCLATURE
b == Approximate Radius of Investigation middot Feet
b 1 == Approximate Radius of Investigation (Net Pay Zone hi) middot Feet
DR == Damage Ratio
EI == Elevation middot Feet
GO == BT Gauge Depth (from Surface Reference) Feet
h == Interval Tested Feet
h _ Net Pay Thickness middot Feet
K Permeability _bullbull md
Permeability (From Net Pay Zone hI) md
m Slope Extrapolated Pressure Plot (Psi1Jcycie Gas) middot psicycle
OF 1 == Maximum Indicated Flow Rate MCFD
OF 2 == Minimum Indicated Flow Rate MCFD
OF3 == Theoretical Open Flow Potential withDamage Removed Max MeFfO
OF4 = Theoretical Open Flow Potential withDamage Removed Min MeFfD
== Extrapolated Stotic Pressure Psig
Final Flow Pressure Psig
Potentiometric Surface (Fresh Watermiddot ) Pot - Feet
Q = Average Adjusted Production Rate During Test bblday
Q 1 = Theoretical Production w Damage Remo ed middot bblday
Q = Measured Gas Production Rate MCFD
R == Corrected Recovery bbl
= Radius of Well Bore Feet
t = Flow Time bullbull Minutes
t bull = Total Flow Time Minutes
T Temperature Rankine OR
Z = Compressibility Factor
p Viscosity Gas or liquid middot CP
Log - Common log
bull Potentiometric Surface Reference to Rotary Table When Elevation Not Given Fresh Woter Corrected to 100 F
NOMENCLATURE
b == Approximate Radius of Investigation middot Feet
b 1 == Approximate Radius of Investigation (Net Pay Zone hi) middot Feet
DR == Damage Ratio
EI == Elevation middot Feet
GO == BT Gauge Depth (from Surface Reference) Feet
h == Interval Tested Feet
h _ Net Pay Thickness middot Feet
K Permeability _bullbull md
Permeability (From Net Pay Zone hI) md
m Slope Extrapolated Pressure Plot (Psi1Jcycie Gas) middot psicycle
OF 1 == Maximum Indicated Flow Rate MCFD
OF 2 == Minimum Indicated Flow Rate MCFD
OF3 == Theoretical Open Flow Potential withDamage Removed Max MeFfO
OF4 = Theoretical Open Flow Potential withDamage Removed Min MeFfD
== Extrapolated Stotic Pressure Psig
Final Flow Pressure Psig
Potentiometric Surface (Fresh Watermiddot ) Pot - Feet
Q = Average Adjusted Production Rate During Test bblday
Q 1 = Theoretical Production w Damage Remo ed middot bblday
Q = Measured Gas Production Rate MCFD
R == Corrected Recovery bbl
= Radius of Well Bore Feet
t = Flow Time bullbull Minutes
t bull = Total Flow Time Minutes
T Temperature Rankine OR
Z = Compressibility Factor
p Viscosity Gas or liquid middot CP
Log - Common log
bull Potentiometric Surface Reference to Rotary Table When Elevation Not Given Fresh Woter Corrected to 100 F
