SURGE AND SWAB PRESSURES

Wellbore Pressures Produced By Drillpipe Movement


INPUT   DATA

Title  

Mud weight ppg
Plastic viscosity cps
Yield point lb/100ft2
Hole diameter in
Drill pipe OD in
Drill pipe ID in
Drill pipe length ft
Drill collar OD in
Drill collar ID in
Drill collar length ft
Bit Nozzle diameter inch
Number of Nozzles  
Pipe running speed ft/min.


     Reset


OUTPUT   VARIABLES   &   GRAPHS

Pressure losses
psi
Closed Pipe  Open Pipe 
  Annulus Annulus Inside 
 ♦  Drill pipe
 ♦  Drill collar
 ♦  Bit nozzle
 ♦  Total
 ♦  Surge/Swab
 ♦  Mud weight (ppg)

THEORY  &   FORMULAE

Surge and Swab Pressures Produced By Drillpipe Movement

During tripping, pipe run into the wellbore too fast may generate large surge pressures inside the hole which can lead to lost circulation and formation fracture. On the other hand, when pipe is pulled out too fast, it may generate large swab (negative surge) pressures that can lead to kicks and blowouts.

Surge pressures are generally calculated using the steady-state model developed by Burkhardt. The method is based on the Bingham plastic behavior of drilling mud, and essentially involves estimating and summing the frictional pressure losses arising from the normal circulation of mud inside and outside the drill string components. These pressures losses are added to the mud's hydrostatic pressure in the hole to obtain the Surge pressure, and subtracted to obtain Swab pressure. There are 2 string configurations to consider: Closed pipe or Open pipe.

CLOSED-PIPE: Here, the pressure losses due to annular flow around the drillpipe and collars are considered. Laminar flow is assumed around the pipe and turbulent flow around the collar. The relevant equations are:

 -  drillpipe pressure losses:

        

 -  drillcollar pressure losses:

        

Where:

   Vp = pipe velocity, ft/minute
   Vm = max pipe velocity, ft/min.
   Ps = pressure loss, psi
   ρ = mud weight, ppg
   n = derived parameter of mud, dimensionless
   K = derived parameter of mud, dimensionless
   θ300 = 300 viscometer dial reading
   θ600 = 600 viscometer dial reading
   θ300 = PV + YP;
   θ600 = θ300 + PV
   PV = plastic viscosity of mud, cps
   YP = yield point of mud, lb/100ft2
   L = length of pipe, ft
   TVD = true vertical depth, ft
   Dh = hole diameter, inches
   Dp = drill pipe or collar OD, inches
   Di = drill pipe or collar ID, inches

OPEN-PIPE: Here, the relative flow in the annulus and in the drillstring are considered separately. That is, the pressure losses attendant to a) annular flow over the drillpipe plus collars, and b) drillstring flow through the pipe plus the collars plus the drillbit nozzles. The mean of a) and b), or the max (larger) of a) and b) can be considered representative of the surge pressure. Laminar flow is assumed inside and outside the pipe. Turbulent flow is assumed in and outside the collars and also in the nozzles.

The expressions for annular pressure losses is similar to that of the closed-pipe, except that the fluid velocity is now lower and includes the pipe's inner diameter term:

        

The following equations are employed to estimates pressure losses inside the drillstring components:

 -  inside drillpipe:

        

 -  inside drill collars:

        

 -  inside drillbit nozzles:

        

Surge pressure can be converted to the equivalent mud weight increment via the expression:

       ρ = 19.23*Psurge / TVD.

BIBLIOGRAPHY