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8. BASIC WELL CONTROL 
Habiburrohman abdullah 1
Basic Well Control 
• Origin of overpressure 
• Kick recognition 
• Shut-in procedure 
• Kill Procedure 
2
Kick Detection and Control 
• Primary well control involves efforts at 
preventing formation fluid influx into the 
wellbore. 
• Secondary well control involves detecting an 
influx and bringing it to the surface safely. 
3
Basic Well Control 
Two primary objectives: 
1. To kill the well safely 
2. To minimize borehole stresses 
4
Blow Out Preventer (BOP) 
5
Successful Well Control 
• Keep the BHP constant throughout using the 
choke. 
6
Slow Pump Rate 
• The pump rate at which the system pressure 
loss is recorded for purposes of well control is 
called the slow pump rate, slow pump 
pressure, kill rate, or reduced circulating 
pressure 
• Also called slow pump rate, slow pump 
pressure, kill rate, reduced circulating 
pressure or slow circulating rate 
7
Slow Pump Rate: When To Take 
• Every tour 
• After repairing the pumps or when the liner is 
changed 
• When the mud properties are changed 
• Every 500 ft of new hole drilled 
• BHA changes 
• When the bit nozzles are changed 
8
SIDPP 
• Shut-in DP Pressure is the measure of the 
difference between the formation pressure 
and the hydrostatic column of the mud in the 
drillstring. 
• Gives a direct reading of the formation 
pressure 
9
Formation Pressure / Kill MW 
• FP (ppg) = (SIDPP / (0.0519 x TVD)) + 
Original MW 
• BHP = ((SIDPP x 19.23) / TVD) + Original 
MW 
10
SICP 
• Shut-in Casing Pressure is the measure 
of the difference between the formation 
pressure and the hydrostatic column of 
the fluids in the annulus during a kick. 
• Not an good indicator of the formation 
pressure. 
FP = HPmud + HPkick + SICP 
11
Pressure at the Casing Shoe 
• Pcsg = SICP + 0.052 x MW x Casing 
shoe TVD 
12
U Tube 
Annulus side 
Kick 
DP side 
SIDPP + HPmud = 
SICP + HPmud + HPkick = 
Fm Pressure 
13
Materials to Weight Up Mud 
• Barite 
• Ilmenite 
• Fe oxide (Hematite) 
• Galena 
14
Materials to Weight Up 
Completion Fluids 
• KCl 
• NaCl 
• CaCl2 
• CaBr2 
• ZnBr 
15
Barite 
• The amount of barite necessary to increase 
the MW to the kill MW is: 
Sx/100 bbl mud = 1490 x ((Kill MW – Old 
MW)/(35.8 – Kill MW) Or 
100-lb sx of barite = (Mud vol x 14.7 x (KMW 
– OMW)) / (35 – KMW) 
• The volume of increase caused by weighting 
up: 
(100 x (Kill MW – MW)) / (35.8 – Kill MW) Or 
Vol incr = sx of Barite / 14.7 
16
Shut-In Procedures 
• Hard shut-in 
• Soft shut-in 
• Shut-in while tripping 
• Shut-in with diverter in use 
• Shut-in while running casing 
17
Hard Shut-in 
• Assure beforehand the choke manifold line is 
open to preferred choke and choke is in 
closed position. 
• After a kick is indicated, pick up the string and 
position tool joint above rotary table. 
• Shut off pump. 
• Flow check. 
• If flow is verified, shut the well in by closing 
the BOP using annular preventer. 
• Open the HCR valve (hydraulically controlled 
remote valve) to the choke manifold. 18
Hard Shut-in 
• Close the choke if open. 
• Notify supervisor (company drilling 
supervisor, toolpusher or rig manager). 
• Read and record SIDPP, SICP, pit gain, TVD 
and time. 
• Rotate the drillstring through the closed 
annular preventer if feasible. 
• Prepare to implement kill procedures. 
19
Soft Shut-in 
• Assure beforehand choke manifold line is 
open to preferred choke and choke in in open 
position. 
• After kick is indicated, pick up string & 
position tool joint above rotary table. 
• Shut off pump. 
• Flow check. 
• If flow is verified, open the HCR. 
• Close the BOP using the annular preventer. 
20
Soft Shut-in 
• Close the choke if open. 
• Notify supervisor (company drilling 
supervisor, toolpusher, rig manager). 
• Read and record SIDPP, SICP, pit gain, TVD 
and time. 
• Rotate the drillstring through the closed 
annular preventer if feasible. 
• Prepare to implement kill procedures. 
21
Shut-in While Tripping 
• Set the slips below the tool joint. 
• Stab a full opening valve (TIW) and close it. 
• Open the HCR and close the BOPs and 
choke. 
• Pick up and stab the kelly/TDS or pump-in 
line. 
• Open the safety valve. 
• Notify the supervisors. 
• Read and record SIDPP, SICP, pit gain, TVD 
of the well, TVD of the bit and time. 
• Prepare to implement kill procedures. 22
Shut-in with Diverters in Use 
• When a shallow kick occurs a full opening 
diverter valve is opened to divert the flow 
away from the rig. 
• The low pressure annular is then closed. 
23
Shut-in While Running Casing 
• Lower the casing until the swage and a valve 
can be stabbed. 
• Close the casing rams or annular preventer. 
• Stab the swage and valve. 
• Notify the supervisors. 
• Read and record the pressures, TVDs, pit 
gain and time. 
• Prepare to implement kill procedures. 
24
Well Kill Procedures 
• Kill equations 
• 3 Major Kill Procedures 
• Other Kill Procedures 
25
Initial Circulating Pressure (ICP) 
• ICP = system pressure loss at kill rate + 
SIDPP 
Note: 
• When we start to circulate, the DP will increase due to the 
friction loss and the pressured drop across the bit. 
• BHP = HSPDP + Circulating DPP – DP press loss 
• In order to utilize the DP gauge we have to know the DP press 
loss. The DP press loss = SPP 
• Circulating DPP = BHP – HSPDP + SPP 
• Since SIDPP =BHP – HSPDP 
• Circ DPP = SIDPP + SPP 26
Final Circulating Pressure (FCP) 
• FCP = System pressure loss x (Kill MW/Old 
MW) 
• Note: 
• As the KMW is circulated through the bit the circ DP Press will 
decrease until the KMW will reach the bit. At the bit the SIDPP 
will be zero. The circ DP pressure with the KMW at the bit is the 
FCP. 
27
ICP and FCP Relationship 
• In a vertical well the circulating drillpipe 
pressure will decrease linearly from the ICP 
to the FCP. 
28
Major Kill Procedures 
• Engineer’s or Wait and Weight Method 
• Driller’s or Two Circulation Method 
• Concurrent or Circulate and Weight Method 
29
Introduction To Kick Killing 
Procedures 
• Introduction 
The purpose of any well kill procedure is to maintain the BHP constant at a level 
equal to or slightly greater than the FP. Since the drill pipe pressure is a direct 
bottom hole pressure indicator, the drill pipe pressure can be manipulated in a 
systematic manner, and the well can be controlled. 
• There are three well kill procedures in common usage. These are: 
Wait and Weight Method – After the well is shut-in, the surface mud system is 
weighted up to the required kill mud weight. The kill mud is then pumped and the 
well is killed in one complete circulation. This method is also called the 
Engineer’s or the One Circulation Method. 
Driller’s Method – After the well is shut-in and the readings are recorded, 
pumping is begun immediately. The influx is pumped from the wellbore without 
any prior weighting up of the mud. Once the influx has been pumped from the 
well, the well is shut-in, and the surface mud system is weighted up to the kill 
mud weight. The lighter mud is then displaced by the kill mud. This method is 
sometimes called the Two Circulation Method. 
Concurrent Method – After the well is shut-in, pumping is begun immediately 
and the mud weight is raised while the kick is being circulated out. The use of 
this method may require several circulations before the well is fully killed. This 
method is also called the Circulate and Weight Method. 30
Engineer’s Method: Procedure 
1. Shut-in well and record SIDPP, SICP, pit gain 
2. Compute kill MW and compute pump sked. Build kill mud 
3. Hold casing press constant and bring pump to kill rate (DPP = 
ICP) 
4. Follow pump schedule when displacing DP. The choke 
opening is varied as required to keep the drill pipe pressure 
regulated. 
5. Once DP filled, poss. to shut-in well, SIDPP = 0 
6. Hold casing press constant using choke and bring pump to kill 
rate, (DPP = FCP) 
7. Hold at FCP until kill mud at surface 
8. Shut down pumps, shut-in well. Check for remaining pressure. 
9. If no more pressure, crack choke and FLC. 
10. If no flow, open BOP. The well is dead. 
31
32 
32
Pressure Schedule For Drillpipe 
• Calculate the number of strokes required to 
displace the drillpipe with the kill mud 
• Calculate ICP and FCP 
• Plot the mud volume (bbls or strokes) along 
the horizontal axis and the DP pressures 
along the vertical axis 
• The plot can be completed by plotting the ICP 
at 0 strokes and connecting it to the FCP at 
the number of strokes required to displace 
the drill pipe. 
33
Pump Schedule: Problem 1 
• Assume the following: 
– SIDPP = 500 psi 
– Kill rate pressure = 1000 psi 
– Original MW = 10 ppg 
– Kill MW = 11 ppg 
– Strokes to displace DP = 500 strokes 
• Problem: Fill in the drill pipe pressure 
schedule. 
34
Pump Schedule: Problem 1 
35 
Strokes Pumped DP Pressure 
0 
100 
200 
300 
400 
500
Pump Schedule: Solution 
• ICP = Kill rate pressure + SIDPP 
– ICP = 1000 psi + 500 psi = 1500 psi at 0 
strokes 
• FCP = (Kill rate pressure x Kill MW) / 
Original MW 
– FCP = (1000 psi x 11 ppg) / 10 ppg = 1100 
psi after 500 strokes 
36
Pump Schedule: Solution 
37 
Strokes Pumped DP Pressure 
0 1500 
100 
200 
300 
400 
500 1100
Pump Schedule: Solution 
• Drill pipe decrease per stroke = (ICP – 
FCP) / Strokes to displace DP with kill 
mud 
– Drill pipe decrease per stroke = (1500 psi – 
1100 psi) / 500 strokes = 0.8 psi /stroke 
38
Pump Schedule: Solution 
39 
Strokes Pumped DP Pressure 
0 1500 
100 1420 
200 1340 
300 1260 
400 1180 
500 1100 
Note: This method eliminates any errors that may occur as a result of reading drill 
pipe pressures from a graph incorrectly.
Pump Schedule: Solution 
2000 
1900 
1800 
1700 
1600 
1500 
1400 
1300 
1200 
1100 
• ICP = Kill rate pressure + SIDPP = 1000 psi + 500 psi = 1500 psi at 0 strokes 
• FCP = (Kill rate pressure x Kill MW) / Original MW = (1000 psi x 11 ppg) / 10 ppg = 1100 
psi after 500 strokes 
• Plot 1500 psi at 0 strokes and plot 1100 psi at 500 strokes. Connect the two points. 
40 
DP Pressure Schedule 
1000 
0 100 200 300 400 500 600 
Strokes Pumped 
Pressure, psi
Driller’s Method 
• TWO complete circulations 
– Circulate kick out of hole using old 
mud 
– Circulate old mud out of hole using 
kill weight mud 
41
Driller’s Method: Procedure 
1. Shut-in well and record SIDPP, SICP, pit gain 
2. Compute kill MW 
3. Hold choke pressure constant and pump at kill rate 
4. Hold DP pressure steady at ICP until kick out of 
hole 
5. Shut-in well and build kill MW 
6. Hold casing pressure steady and pump at kill rate 
7. DP pressure is allowed to decline as per pump 
sked. Once DP full, observe FCP 
8. Keep pumping at kill rate and constant FCP until kill 
mud at surface. 
9. Shut down pumps, shut-in well. Check for remaining 
pressure. 
10. If no more pressure, crack choke and FLC. 
11. If no flow, open BOP. The well is dead. 
42
Concurrent Method: Procedure 
1. Shut-in well using preferred shut-in 
procedure and record the SIDPP, SICP and 
the amount of pit gain 
2. Hold casing press constant and bring pump 
to kill rate (DPP = ICP) 
3. Follow schedule when displacing DP 
4. Once DP filled, shut-in well, SIDPP = 0 
5. Hold casing press constant and bring pump 
to kill rate, (DPP = FCP) 
6. Hold at FCP until kill mud at surface 
7. Shut down pumps, shut-in well, check if well 
is dead 
8. If not repeat steps 2 to 9. 43
Major Kill Procedures: Conclusion 
• The Wait and Weight Method using the 
proper kill weight results in the least 
amount of casing pressure and the 
least borehole stresses. 
• The Concurrent Method allows lower 
casing pressure values than the Driller’s 
Method. 
• Overkilling the well has no tangible 
benefit. 
44
Other Calculations 
• Height of the Influx 
• Identification of Influx 
• Choke Line Friction (CLFP) 
• MASCP 
45
Height Of Influx 
• Pit level gain < ann. vol. around the DC: 
Length of kick, ft = kick volume (bbls) / 
((Hole ID2 – DCOD2) x 0.000971) 
• Pit level gain > ann. vol. around the DC: 
Length of kick, ft = Length of DC + 
((kick volume – DC ann. vol.) / ((Hole 
ID2 – DPCOD2) x 0.000971)) 
46
Identification Of Influx Density 
• Influx Density, ppg = MW, ppg – ((SICP-SIDPP)/( 
Height of influx, ft x 0.0519)) 
Note: 
• The influx may either be gas, oil, water or a combination of the three. The 
calculation is an approximation at best because the hole may not be gauge and 
the pit gain may not be necessarily accurately noted. 
• The formula for determining the gradient of the influx fluid is: 
Influx gradient = Mud gradient in DP– ((SICP-SIDPP)/Height of influx) 
Height of influx = bbls gained / annulus volume, bbls/ft 
Influx density (ppg) = Influx gradient / 0.52 
• As a general rule, an influx with an equivalent mud weight of 1 to 3 ppg is 
assumed to be gas, 3 to 5 ppg is assumed to be a mixture of gas and water or 
gas and oil, and 5 to 7 ppg is assumed to be either oil, water or an oil-water 
mixture. 47
Identification Of Influx 
As a general rule: 
• 1 to 3 ppg EMW is assumed to be gas 
• 3 to 5 ppg EMW is assumed to be a 
mixture of gas and water or gas and oil 
• 5 to 7 ppg EMW is assumed to be 
either oil, water or an oil-water mixture 
48
Influx Identification: Problem 1 
• Identify the type of influx assuming the 
following: 
–TVD = 10000 ft 
–MW in DP = 12 ppg 
–Hole ID = 9.875 in 
–DP OD = 5 in 
– SIDPP = 520 psi 
– SICP = 650 psi 
– Pit Gain = 40 bbls 49
Influx Identification: Solution 
• Mud gradient = 12 ppg x .052 = 0.624 
psi/ft 
• Annulus volume, bbl/ft = ((9.875)2 – (5)2) 
/ 1029 = 0.70 bbls/ft 
• Length of influx, ft = 40 bbls / 0.70 
bbls/ft = 571 ft 
50
Influx Identification: Solution 
• Gradient of influx, psi/ft: 
• = 0.624 psi/ft –((650 psi – 520 psi) / 571 ft) 
• = 0.624 psi/ft – (130 psi/571 ft) 
• = 0.624 psi/ft – 0.228 psi/ft = 0.396 psi/ft 
• Influx density, ppg = 0.396 psi/ft / .052 = 7.61 
ppg 
• The influx would probably be oil or water. The 
comparatively high weight means that not 
much gas is associated within the influx. 
51
Choke Line Friction (CLFP) 
• Used to determine the amount by which 
the casing pressure is to be adjusted to 
maintain BHP = FP when starting the 
pumps on a kill operation. We reduce 
the SICP by the amount of CLFP to 
make allowances for the back pressure 
imposed by the CLFP. 
52
Maximum Allowable Shut-in Casing 
Pressure 
• Surface pressure acting ontop of the current 
hydrostatic pressure that will exceed the 
measured fracture pressure at the casing 
seat. 
• MASCP = 0.0519 x (FGmin – MW) x Dwf 
• Where, 
MASCP = psi 
FGmin = Fracture Gradient of weakest formation, ppg 
MW = ppg 
Dwf = TVD of weakest formation 
53
END 
54

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Basic Well Control

  • 1. 8. BASIC WELL CONTROL Habiburrohman abdullah 1
  • 2. Basic Well Control • Origin of overpressure • Kick recognition • Shut-in procedure • Kill Procedure 2
  • 3. Kick Detection and Control • Primary well control involves efforts at preventing formation fluid influx into the wellbore. • Secondary well control involves detecting an influx and bringing it to the surface safely. 3
  • 4. Basic Well Control Two primary objectives: 1. To kill the well safely 2. To minimize borehole stresses 4
  • 6. Successful Well Control • Keep the BHP constant throughout using the choke. 6
  • 7. Slow Pump Rate • The pump rate at which the system pressure loss is recorded for purposes of well control is called the slow pump rate, slow pump pressure, kill rate, or reduced circulating pressure • Also called slow pump rate, slow pump pressure, kill rate, reduced circulating pressure or slow circulating rate 7
  • 8. Slow Pump Rate: When To Take • Every tour • After repairing the pumps or when the liner is changed • When the mud properties are changed • Every 500 ft of new hole drilled • BHA changes • When the bit nozzles are changed 8
  • 9. SIDPP • Shut-in DP Pressure is the measure of the difference between the formation pressure and the hydrostatic column of the mud in the drillstring. • Gives a direct reading of the formation pressure 9
  • 10. Formation Pressure / Kill MW • FP (ppg) = (SIDPP / (0.0519 x TVD)) + Original MW • BHP = ((SIDPP x 19.23) / TVD) + Original MW 10
  • 11. SICP • Shut-in Casing Pressure is the measure of the difference between the formation pressure and the hydrostatic column of the fluids in the annulus during a kick. • Not an good indicator of the formation pressure. FP = HPmud + HPkick + SICP 11
  • 12. Pressure at the Casing Shoe • Pcsg = SICP + 0.052 x MW x Casing shoe TVD 12
  • 13. U Tube Annulus side Kick DP side SIDPP + HPmud = SICP + HPmud + HPkick = Fm Pressure 13
  • 14. Materials to Weight Up Mud • Barite • Ilmenite • Fe oxide (Hematite) • Galena 14
  • 15. Materials to Weight Up Completion Fluids • KCl • NaCl • CaCl2 • CaBr2 • ZnBr 15
  • 16. Barite • The amount of barite necessary to increase the MW to the kill MW is: Sx/100 bbl mud = 1490 x ((Kill MW – Old MW)/(35.8 – Kill MW) Or 100-lb sx of barite = (Mud vol x 14.7 x (KMW – OMW)) / (35 – KMW) • The volume of increase caused by weighting up: (100 x (Kill MW – MW)) / (35.8 – Kill MW) Or Vol incr = sx of Barite / 14.7 16
  • 17. Shut-In Procedures • Hard shut-in • Soft shut-in • Shut-in while tripping • Shut-in with diverter in use • Shut-in while running casing 17
  • 18. Hard Shut-in • Assure beforehand the choke manifold line is open to preferred choke and choke is in closed position. • After a kick is indicated, pick up the string and position tool joint above rotary table. • Shut off pump. • Flow check. • If flow is verified, shut the well in by closing the BOP using annular preventer. • Open the HCR valve (hydraulically controlled remote valve) to the choke manifold. 18
  • 19. Hard Shut-in • Close the choke if open. • Notify supervisor (company drilling supervisor, toolpusher or rig manager). • Read and record SIDPP, SICP, pit gain, TVD and time. • Rotate the drillstring through the closed annular preventer if feasible. • Prepare to implement kill procedures. 19
  • 20. Soft Shut-in • Assure beforehand choke manifold line is open to preferred choke and choke in in open position. • After kick is indicated, pick up string & position tool joint above rotary table. • Shut off pump. • Flow check. • If flow is verified, open the HCR. • Close the BOP using the annular preventer. 20
  • 21. Soft Shut-in • Close the choke if open. • Notify supervisor (company drilling supervisor, toolpusher, rig manager). • Read and record SIDPP, SICP, pit gain, TVD and time. • Rotate the drillstring through the closed annular preventer if feasible. • Prepare to implement kill procedures. 21
  • 22. Shut-in While Tripping • Set the slips below the tool joint. • Stab a full opening valve (TIW) and close it. • Open the HCR and close the BOPs and choke. • Pick up and stab the kelly/TDS or pump-in line. • Open the safety valve. • Notify the supervisors. • Read and record SIDPP, SICP, pit gain, TVD of the well, TVD of the bit and time. • Prepare to implement kill procedures. 22
  • 23. Shut-in with Diverters in Use • When a shallow kick occurs a full opening diverter valve is opened to divert the flow away from the rig. • The low pressure annular is then closed. 23
  • 24. Shut-in While Running Casing • Lower the casing until the swage and a valve can be stabbed. • Close the casing rams or annular preventer. • Stab the swage and valve. • Notify the supervisors. • Read and record the pressures, TVDs, pit gain and time. • Prepare to implement kill procedures. 24
  • 25. Well Kill Procedures • Kill equations • 3 Major Kill Procedures • Other Kill Procedures 25
  • 26. Initial Circulating Pressure (ICP) • ICP = system pressure loss at kill rate + SIDPP Note: • When we start to circulate, the DP will increase due to the friction loss and the pressured drop across the bit. • BHP = HSPDP + Circulating DPP – DP press loss • In order to utilize the DP gauge we have to know the DP press loss. The DP press loss = SPP • Circulating DPP = BHP – HSPDP + SPP • Since SIDPP =BHP – HSPDP • Circ DPP = SIDPP + SPP 26
  • 27. Final Circulating Pressure (FCP) • FCP = System pressure loss x (Kill MW/Old MW) • Note: • As the KMW is circulated through the bit the circ DP Press will decrease until the KMW will reach the bit. At the bit the SIDPP will be zero. The circ DP pressure with the KMW at the bit is the FCP. 27
  • 28. ICP and FCP Relationship • In a vertical well the circulating drillpipe pressure will decrease linearly from the ICP to the FCP. 28
  • 29. Major Kill Procedures • Engineer’s or Wait and Weight Method • Driller’s or Two Circulation Method • Concurrent or Circulate and Weight Method 29
  • 30. Introduction To Kick Killing Procedures • Introduction The purpose of any well kill procedure is to maintain the BHP constant at a level equal to or slightly greater than the FP. Since the drill pipe pressure is a direct bottom hole pressure indicator, the drill pipe pressure can be manipulated in a systematic manner, and the well can be controlled. • There are three well kill procedures in common usage. These are: Wait and Weight Method – After the well is shut-in, the surface mud system is weighted up to the required kill mud weight. The kill mud is then pumped and the well is killed in one complete circulation. This method is also called the Engineer’s or the One Circulation Method. Driller’s Method – After the well is shut-in and the readings are recorded, pumping is begun immediately. The influx is pumped from the wellbore without any prior weighting up of the mud. Once the influx has been pumped from the well, the well is shut-in, and the surface mud system is weighted up to the kill mud weight. The lighter mud is then displaced by the kill mud. This method is sometimes called the Two Circulation Method. Concurrent Method – After the well is shut-in, pumping is begun immediately and the mud weight is raised while the kick is being circulated out. The use of this method may require several circulations before the well is fully killed. This method is also called the Circulate and Weight Method. 30
  • 31. Engineer’s Method: Procedure 1. Shut-in well and record SIDPP, SICP, pit gain 2. Compute kill MW and compute pump sked. Build kill mud 3. Hold casing press constant and bring pump to kill rate (DPP = ICP) 4. Follow pump schedule when displacing DP. The choke opening is varied as required to keep the drill pipe pressure regulated. 5. Once DP filled, poss. to shut-in well, SIDPP = 0 6. Hold casing press constant using choke and bring pump to kill rate, (DPP = FCP) 7. Hold at FCP until kill mud at surface 8. Shut down pumps, shut-in well. Check for remaining pressure. 9. If no more pressure, crack choke and FLC. 10. If no flow, open BOP. The well is dead. 31
  • 32. 32 32
  • 33. Pressure Schedule For Drillpipe • Calculate the number of strokes required to displace the drillpipe with the kill mud • Calculate ICP and FCP • Plot the mud volume (bbls or strokes) along the horizontal axis and the DP pressures along the vertical axis • The plot can be completed by plotting the ICP at 0 strokes and connecting it to the FCP at the number of strokes required to displace the drill pipe. 33
  • 34. Pump Schedule: Problem 1 • Assume the following: – SIDPP = 500 psi – Kill rate pressure = 1000 psi – Original MW = 10 ppg – Kill MW = 11 ppg – Strokes to displace DP = 500 strokes • Problem: Fill in the drill pipe pressure schedule. 34
  • 35. Pump Schedule: Problem 1 35 Strokes Pumped DP Pressure 0 100 200 300 400 500
  • 36. Pump Schedule: Solution • ICP = Kill rate pressure + SIDPP – ICP = 1000 psi + 500 psi = 1500 psi at 0 strokes • FCP = (Kill rate pressure x Kill MW) / Original MW – FCP = (1000 psi x 11 ppg) / 10 ppg = 1100 psi after 500 strokes 36
  • 37. Pump Schedule: Solution 37 Strokes Pumped DP Pressure 0 1500 100 200 300 400 500 1100
  • 38. Pump Schedule: Solution • Drill pipe decrease per stroke = (ICP – FCP) / Strokes to displace DP with kill mud – Drill pipe decrease per stroke = (1500 psi – 1100 psi) / 500 strokes = 0.8 psi /stroke 38
  • 39. Pump Schedule: Solution 39 Strokes Pumped DP Pressure 0 1500 100 1420 200 1340 300 1260 400 1180 500 1100 Note: This method eliminates any errors that may occur as a result of reading drill pipe pressures from a graph incorrectly.
  • 40. Pump Schedule: Solution 2000 1900 1800 1700 1600 1500 1400 1300 1200 1100 • ICP = Kill rate pressure + SIDPP = 1000 psi + 500 psi = 1500 psi at 0 strokes • FCP = (Kill rate pressure x Kill MW) / Original MW = (1000 psi x 11 ppg) / 10 ppg = 1100 psi after 500 strokes • Plot 1500 psi at 0 strokes and plot 1100 psi at 500 strokes. Connect the two points. 40 DP Pressure Schedule 1000 0 100 200 300 400 500 600 Strokes Pumped Pressure, psi
  • 41. Driller’s Method • TWO complete circulations – Circulate kick out of hole using old mud – Circulate old mud out of hole using kill weight mud 41
  • 42. Driller’s Method: Procedure 1. Shut-in well and record SIDPP, SICP, pit gain 2. Compute kill MW 3. Hold choke pressure constant and pump at kill rate 4. Hold DP pressure steady at ICP until kick out of hole 5. Shut-in well and build kill MW 6. Hold casing pressure steady and pump at kill rate 7. DP pressure is allowed to decline as per pump sked. Once DP full, observe FCP 8. Keep pumping at kill rate and constant FCP until kill mud at surface. 9. Shut down pumps, shut-in well. Check for remaining pressure. 10. If no more pressure, crack choke and FLC. 11. If no flow, open BOP. The well is dead. 42
  • 43. Concurrent Method: Procedure 1. Shut-in well using preferred shut-in procedure and record the SIDPP, SICP and the amount of pit gain 2. Hold casing press constant and bring pump to kill rate (DPP = ICP) 3. Follow schedule when displacing DP 4. Once DP filled, shut-in well, SIDPP = 0 5. Hold casing press constant and bring pump to kill rate, (DPP = FCP) 6. Hold at FCP until kill mud at surface 7. Shut down pumps, shut-in well, check if well is dead 8. If not repeat steps 2 to 9. 43
  • 44. Major Kill Procedures: Conclusion • The Wait and Weight Method using the proper kill weight results in the least amount of casing pressure and the least borehole stresses. • The Concurrent Method allows lower casing pressure values than the Driller’s Method. • Overkilling the well has no tangible benefit. 44
  • 45. Other Calculations • Height of the Influx • Identification of Influx • Choke Line Friction (CLFP) • MASCP 45
  • 46. Height Of Influx • Pit level gain < ann. vol. around the DC: Length of kick, ft = kick volume (bbls) / ((Hole ID2 – DCOD2) x 0.000971) • Pit level gain > ann. vol. around the DC: Length of kick, ft = Length of DC + ((kick volume – DC ann. vol.) / ((Hole ID2 – DPCOD2) x 0.000971)) 46
  • 47. Identification Of Influx Density • Influx Density, ppg = MW, ppg – ((SICP-SIDPP)/( Height of influx, ft x 0.0519)) Note: • The influx may either be gas, oil, water or a combination of the three. The calculation is an approximation at best because the hole may not be gauge and the pit gain may not be necessarily accurately noted. • The formula for determining the gradient of the influx fluid is: Influx gradient = Mud gradient in DP– ((SICP-SIDPP)/Height of influx) Height of influx = bbls gained / annulus volume, bbls/ft Influx density (ppg) = Influx gradient / 0.52 • As a general rule, an influx with an equivalent mud weight of 1 to 3 ppg is assumed to be gas, 3 to 5 ppg is assumed to be a mixture of gas and water or gas and oil, and 5 to 7 ppg is assumed to be either oil, water or an oil-water mixture. 47
  • 48. Identification Of Influx As a general rule: • 1 to 3 ppg EMW is assumed to be gas • 3 to 5 ppg EMW is assumed to be a mixture of gas and water or gas and oil • 5 to 7 ppg EMW is assumed to be either oil, water or an oil-water mixture 48
  • 49. Influx Identification: Problem 1 • Identify the type of influx assuming the following: –TVD = 10000 ft –MW in DP = 12 ppg –Hole ID = 9.875 in –DP OD = 5 in – SIDPP = 520 psi – SICP = 650 psi – Pit Gain = 40 bbls 49
  • 50. Influx Identification: Solution • Mud gradient = 12 ppg x .052 = 0.624 psi/ft • Annulus volume, bbl/ft = ((9.875)2 – (5)2) / 1029 = 0.70 bbls/ft • Length of influx, ft = 40 bbls / 0.70 bbls/ft = 571 ft 50
  • 51. Influx Identification: Solution • Gradient of influx, psi/ft: • = 0.624 psi/ft –((650 psi – 520 psi) / 571 ft) • = 0.624 psi/ft – (130 psi/571 ft) • = 0.624 psi/ft – 0.228 psi/ft = 0.396 psi/ft • Influx density, ppg = 0.396 psi/ft / .052 = 7.61 ppg • The influx would probably be oil or water. The comparatively high weight means that not much gas is associated within the influx. 51
  • 52. Choke Line Friction (CLFP) • Used to determine the amount by which the casing pressure is to be adjusted to maintain BHP = FP when starting the pumps on a kill operation. We reduce the SICP by the amount of CLFP to make allowances for the back pressure imposed by the CLFP. 52
  • 53. Maximum Allowable Shut-in Casing Pressure • Surface pressure acting ontop of the current hydrostatic pressure that will exceed the measured fracture pressure at the casing seat. • MASCP = 0.0519 x (FGmin – MW) x Dwf • Where, MASCP = psi FGmin = Fracture Gradient of weakest formation, ppg MW = ppg Dwf = TVD of weakest formation 53