@Rosier - Well Control for the Directional Driller
Transcript of @Rosier - Well Control for the Directional Driller
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Well Control for the Directional Driller
C.Rosier
Technical Training InstructorD&M Schlumberger
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2 C.R.
5/2/2002
ObjectivesAfter completion of this module you will be able to:
Calculate Gradientand Hydrostatic Pressurefor different mudweights and depths.
Define Pore Pressure and be able to identifyNormal
andAbnormalPore Pressure.
Describe the purpose and method of performing a FITand
LOT.
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3 C.R.
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ObjectivesAfter completion of this module you will be able to:
Describe and calculate Maximum Allowable Annular SurfacePressure.
Describe and calculateMaximum Mud Weight
andEquivalentMud Weight.
Understand Equivalent Circulating Densityand why it is of
concern in well control.
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4 C.R.
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ObjectivesAfter completion of this module you will be able to:
Understand the terms Primaryand Secondary Well Control.
Identify the signs of a Kick
Identify the key components of a BOP Stackand describe itsoperation.
Understand the need to Space-out.
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5 C.R.
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Hydrostatic Pressure1ft
1ft
1ft
7.48gallons
7.48
lbf/sq ft
7.48 / 144 = 0.051944 lbf/ sq in.
Hydrostatic Pressure (English Units)
A cubic foot contains 7.48 gallons
and exerts, for a fluid of 1ppg
a force of 7.48 lbsf / sq ft or7.48 / 144 lbsf / sq in.
= 0.051944 lbf / sq in
This is usually rounded to 0.052
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Hydrostatic PressureFor a fluid of a different mud weight we simply multiply thisconstant by the density of the fluid for the gradient and this
by the TVD to obtain the Pressure.
Example for a Mud Wtof 9.8 ppg, depth of 3,800 ft
TVD of 3,118 ft
Mud Wt x Constant = Mud Gradient (psi / ft)
9.8 ppg x 0.052 = 0.5096 psi / ft
Mud Gradient x TVD = Bottom Hole Pressure (psi)
0.5096 psi / ft x 3,118 ft = 1588.93 psi
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Exercise
1. For a Mud weight of 12. 6ppg what is the gradient? Whatis the bottom hole pressure for a 13,256 ft (TVD) well?
2. If my well is 17,678 ft (TVD) and my requires bottom holepressure is 8641psi, what Mud weight do I need? What is
the gradient?
3. What is the increase in bottom hole pressure if I drill from6890 ft (TVD)to 10,975 ft (TVD) with a 10.5 ppg mud?
Calculate for the following:
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Pore Pressure
The pressure of the fluid contained in the pore space in theformation of interest.
Pore Pressure is also referred to as Formation Pressure.
What is the definition of Pore Pressure?
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Normal Pore PressureNormal Pore Pressure is the Hydrostatic Pressure of the fluid
in which the sedimentation took placeDepending on the salinity and purity of the fluid (water) the
normal pressure gradient will vary from 0.433 psi / ft to 0.465
psi / ft.
For normal formation pressure to exist the overburden weight
of the formations above is supported by the grains in therock.
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Abnormal Pore PressureAbnormal Pore Pressure is when the Hydrostatic Pressure of
the fluid in which the sedimentation took place is less than,the Pore Pressure
Abnormal Pore Pressure is usually caused by interruption to
the percolation of the fluids being driven from the porespace during compaction. This causes the fluid to supportpart of the overburden of the formations at shallowerdepths.
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Abnormal Pore PressureAbnormal Pore Pressure is also caused by:
Faults
Salt Domes
Formation dips Erosion of the overburden
Formations with Pore Pressure Gradients below 0.433 psi / ftare described as having Subnormal Formation Pressure.
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Formation Fracture Pressure
Every formation has a limit to the pressure that it can
withstand before it permanently deforms or fractures. Thislimit needs to be determined so that it is not exceeded inwell control operations.
There are two systems for determining the upper pressurelimit during well killing operations:
The Leak Off Test (LOT) The Formation Integrity Test (FIT)
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The Leak Off Test
The Leak Off Test is used to accurately determine the
pressure capacity at the Shoe.Because overburden increases with depth, the shallowest
formation is usually the weakest.
Leak Off Test
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MAASPWhen the FITor MOThas been performed there becomes a
requirement to use the results in a format that is
independent of depth, as the plan is to drill ahead.
For this we use the Maximum Allowable Annular Surface Pressure
or MAASP:MAASP = Surface Pressure @ Mud Wt
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Maximum Mud Weight
An alternative to the MAASP that facilitates comparison, based
on the Equivalent Mud Weightis the Maximum Mud WeightorMMW. This states the Mud Gradientas a Mud Weight
Example:
LOT BHP = 6,534.6 psi
MMW = 6,534.6 / 9,500 / 0.052 = 13.23 ppg
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Equivalent Mud Weight
The Equivalent Mud Weightis calculated in the same way as
MMW but is for the anticipated BHP or actual BHP and notat the pressure that will cause break down of the formation.
Example:
EMW = (Surf Press / 0.052 / Depth (TVD) ) + MWt ppg
= (1,450psi / 0.052 / 8,500) + 8.9
= 12.18ppg
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Equivalent Circulating Density
The Equivalent Circulating Densityor ECDis the sum of the
Hydrostatic Pressureand the Annular Pressure Losswhencirculating.
In well control we are concerned with this because it is
possible to drill into a new formation with sufficient ECD tohold back the formation fluids, only to take a kick when westop for a connection.
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Primary Well Control
Primary Well Control is the use of the drilling fluid to
contain formation fluids by means of applied HydrostaticPressure.
To do this we need to maintain a full column of drilling fluid
at sufficient weight to overbalance the formation.
The most common causes of kicks indicate what we need tobe monitoring:
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Primary Well Control
Insufficient Fluid Density
Poor Tripping Practices Improper Hole Filling While Tripping
Swabbing / Surging Lost Circulation
Abnormal Formation Pressure
Obstructions in the Wellbore
Cementing Operations
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Primary Well Control
Special Situations:
Subsea Riser Failure Water Flushes
Drill Stem Tests (DST) Failure to Maintain Sufficient Back Pressure when Drilling
Underbalanced
Drilling from Platform Legs
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Detecting a Kick
There are certain indicators that may warn of a possible kick:
Drilling Break Increase in Return Flow
Pit Gain Well Flowing
Increase in Pump Rate
Drop in Standpipe Pressure
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Detecting a Kick
Indicators contd:
Oil Shows Insufficient displacement to / from Trip Tank
String Pulling Wet After Slugging String Weight Change
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Control Equipment
The main components of a Blow Out Preventer Stack are:
The Annular The Rams
The Choke Line The Kill Line
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Control Equipment
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Control Equipment
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Control Equipment
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Control Equipment
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Control Equipment
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Drillpipe
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Pclose
Drillpipe
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Pclose
Closing
Drillpipe
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Pclose
Drillpipe
Closing
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Pclose
Drillpipe
Closing
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Pclose
Drillpipe
Closing
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Pclose
Drillpipe
Closing
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SICP
Pclose
Drillpipe
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SICP
Pclose
Drillpipe
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Control Equipment
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Available with 2 or 3 PumpsHandles High Pressure
Tungsten Carbide Choke Plates
And Extended Wear
Sleeves
Choke
Console
Detail showing
Operation ofChoke
10,000 psi / 20,000 psi
Dual Chokes / Console
Designed for H2S Service
Super Choke
10,000 psi
Control Equipment
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Control Equipment
1 Static Trim2 Dynamic Trim
3 Shuttle4 Position Indicator
5 Casing Pressure6 Set Point Pressure
1
2
3
5
64
Console Control Panel
Super AutoChoke
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Shut In Procedure
The Shut in procedure:
When a kick has been detected the first course of action is toclose the well in. However, because Pipe Rams close on
the tube only, not the tool joints it is important to Space Out
to ensure that the rams do not close on a tool-joint.
At this point the role of the Directional Driller is complete, it istime to leave the drill-floor.