Instrumentation and Pigging
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Transcript of Instrumentation and Pigging
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1PE 607: Oil & Gas Pipeline Design, Maintenance & Repair
Dr. Abdel-Alim Hashem
Professor of Petroleum EngineeringMining, Petroleum & Metallurgical Eng. Dept.
Faculty of Engineering – Cairo University
[email protected]@yahoo.com
Part 7: Instrumentation and Pigging
Oil and Gas Pipeline Design,
Maintenance and Repair
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2PE 607: Oil & Gas Pipeline Design, Maintenance & Repair
PIGGING OPERATIONS
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4PE 607: Oil & Gas Pipeline Design, Maintenance & Repair
REASONS FOR PIGGING
• Batch or separate dissimilar products
• Displacement purposes
• Internal inspection.
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6PE 607: Oil & Gas Pipeline Design, Maintenance & Repair
SELECTION CRITERIA
The purpose:
• Type, location, and volume of the
substance to be removed or displaced in
conventional pigging applications,• Type of information to be gathered from an
intelligent pig run,
• Objectives and goals for the pig run
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8PE 607: Oil & Gas Pipeline Design, Maintenance & Repair
SELECTION CRITERIA
Characteristics of the pipeline
• The minimum and maximum internal line
sizes,
• Maximum distance pig must travel,• Minimum bend radius, and bend angles,
• Additional features such as valve types,
branch connections, and the elevation
profile.
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11PE 607: Oil & Gas Pipeline Design, Maintenance & Repair
UTILITY PIGS
Foam pigsMandrel pigs
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13PE 607: Oil & Gas Pipeline Design, Maintenance & Repair
IN LINE INSPECTION TOOLS
• In Line Inspection provides information on
the condition of the pipe and/or itscontents.
• With few exceptions, the In Line InspectionTool itself is simply the tool which gathers
the data, which is then analyzed by the
engineers and technicians to determineand report on the condition of the line.
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17PE 607: Oil & Gas Pipeline Design, Maintenance & Repair
GEL PIGS• Gel pigs are a series of gelled
liquid systems which have been
developed for use in pipelineoperations, either during initialcommissioning, or as a part of acontinuing maintenance program.
• Most pipeline gels are water-based, but a range of chemicals,solvents, and even acids can begelled.
• Some chemicals can be gelled as
the bulk liquid and others onlydiluted in a carrier.
• Gelled diesel used as a carrier ofcorrosion inhibitor in gas lines.
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18PE 607: Oil & Gas Pipeline Design, Maintenance & Repair
TYPES OF GEL
• Batching, or separator gel
• Debris pickup gel
• Hydrocarbon gel
• Dehydrating gel
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19PE 607: Oil & Gas Pipeline Design, Maintenance & Repair
PRINCIPLE APPLICATION OF GEL PIGS
• Product separation
• Debris removal• Line filling/hydro testing
• Dewatering and drying• Condensate removal from gas lines
• Inhibitor and biocide lay down
• Special chemical treatment• Removal of stuck pigs
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20PE 607: Oil & Gas Pipeline Design, Maintenance & Repair
DUAL DIAMETER PIGS
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21PE 607: Oil & Gas Pipeline Design, Maintenance & Repair
DUAL DIAMETER PIGS
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22PE 607: Oil & Gas Pipeline Design, Maintenance & Repair
DUAL DIAMETER PIGS
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23PE 607: Oil & Gas Pipeline Design, Maintenance & Repair
MULTI DIAMETERS PIGS
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24PE 607: Oil & Gas Pipeline Design, Maintenance & Repair
WHY DO PIG STUCK?
• Pigs plug a pipe and cause a blockage
• Build up of wax in front of a pig causing a wax plug• Unidirectional bypass leading to a stuck pig with
product flowing past to it
• Jack knifing of a dual module pig
• Excessive wear leading to failure of seals and drive
• Mechanical damage
• Failure due to environment material selection
• Others that do not fail in the categories above
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25PE 607: Oil & Gas Pipeline Design, Maintenance & Repair
SPHERE JAMMED IN OFF TAKE
Cause
• Due to flow diversion, Flowfrom branch line
Solution
• Require to provide a bararrangement in receivers orspecial flow/sphere tees inthe pipeline
• The bearing arrangementshould be checked
• In dual diameter line, specialbearing arrangement maybe necessary
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27PE 607: Oil & Gas Pipeline Design, Maintenance & Repair
INCORRECT SIZED PIG COMPONENTS
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28PE 607: Oil & Gas Pipeline Design, Maintenance & Repair
INCORRECT VALVE/VALVE NOT OPENCause
• Use of incorrect valve in line, valves are not fully open
• Happens in smaller diameter line 12 in and smaller Solution
• Checks in the operating procedures should be in place tocheck opening the valve
• Pig design should consider this eventually
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29PE 607: Oil & Gas Pipeline Design, Maintenance & Repair
INSUFFICIENT INFORMATION
(wrong bend radius)
Cause
• Insufficient informationregarding pipeline design,
especially older one
Solution
• Pigs must be designed for
the line
• Some conservative
assumptions must be madeand agreed
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30PE 607: Oil & Gas Pipeline Design, Maintenance & Repair
PIG PUSHING ON PIG IN FRONTCause
• when one pig pushes into the rear of another pig. It actson the seals, forcing them harder against the pipe wall
Solution
• Have a bumper noses, both front and rear
• This be provided even if it is not only planned to haveone pig in the line
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31PE 607: Oil & Gas Pipeline Design, Maintenance & Repair
COLLIDING PIGS
Causes
• Possibility of pigs to meet atwyes or tees in complex lines
Solution
• Good communication andpigging operation procedures
• One pig may be made
sacrificial
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32PE 607: Oil & Gas Pipeline Design, Maintenance & Repair
HIGH FRICTION PIGSCause
• Change from thin wall to
thick wall pipe, lead toserious damage of theseals
Solution• All pigs should be
designed to deal with allinternal diameters of the
line and if in doubt, a testperformed
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34PE 607: Oil & Gas Pipeline Design, Maintenance & Repair
DEPRIS IN THE LINECause
• Depris such as sand lift the pig up andcause rapid wear
Solution
• Provide strong and sufficient bypass to the
pig
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35PE 607: Oil & Gas Pipeline Design, Maintenance & Repair
FLOW AROUND THE PIGCause
• Pipeline features suchas branches andofftakes, wyes etc.which can lead to a
stalled pig if thebypass system isincorrect
Solution• Consider the position
of the offtakes
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36PE 607: Oil & Gas Pipeline Design, Maintenance & Repair
INSUFFICIENT SEALING LENGTHCause
• Components such as wyes and teesSolution
• A dual pig should be used to span the
component
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39PE 607: Oil & Gas Pipeline Design, Maintenance & Repair
PROXIMITY OF COMPONENTS
Cause
• Too close line components which makes a risk of bypass
as the sealing is incorrectSolution
• The configuration of the pig must be considered andsufficient length between line components should be
allowed
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41PE 607: Oil & Gas Pipeline Design, Maintenance & Repair
REDUCER LENGTHCause
• When the diameter of the pipe is reduced from a large
diameter to a smaller diameter Solution
• The reducer length should be as long as possible withinspection pigging compared with utility pigging where it
should be as short as possible
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43PE 607: Oil & Gas Pipeline Design, Maintenance & Repair
DRIVING DUAL MODULE PIG ON REARCause
• Bends makes the pigstend to move laterally,results in seal flapping
Solution
• Pressure should betransferred to the frontmodule via bypassports on the rear
• This allows the rearmodule to be towed
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44PE 607: Oil & Gas Pipeline Design, Maintenance & Repair
DUAL MODULE PIG WITH LEAKAGECause
• Low density gas leaksthrough a dual modulepig, differentialpressure is set up
across the pig andlateral movement canresult
Solution
• Use better support forthe pig and correctsizing of the seals
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45PE 607: Oil & Gas Pipeline Design, Maintenance & Repair
WEAR
Cause
• Abrasion cause wear due to large distanceSolution
• Determine the maximum piggable distancedepending on: pig velocity, fluid type, pig
differential pressure, pipeline nominal
diameter, pipe surface type
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46PE 607: Oil & Gas Pipeline Design, Maintenance & Repair
VELOCITY EXCURSIONSCause
• Large accelerationand velocities dueto thecompressibility of
the systemSolution
• Take into
considerationduring pigselection
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47PE 607: Oil & Gas Pipeline Design, Maintenance & Repair
COUPLING DAMAGECause
• In dual module pig,
compression and tensionon coupling betweenmodule
Solution
• Strong coupling selection
• Joint must be capable ofopening to the correct
angle to allow the pig tonegotiate the linefeatures
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49PE 607: Oil & Gas Pipeline Design, Maintenance & Repair
TEARING SEALS OUT OF BOLTHOLES
Cause
• Highly oversizedsealing discs
Solution
• Oversize needs to becarefully selected andthe boltingarrangement such that
the discs is properlyclamped to the pig
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50PE 607: Oil & Gas Pipeline Design, Maintenance & Repair
PIGS IN FREE FALL
Cause
• Steep sections such asrisers, lead to high
velocity
Solution
• Slow the pig down
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51PE 607: Oil & Gas Pipeline Design, Maintenance & Repair
ENVIRONMENTAL ISSUESCause
• Line temperature (degradation of the sealmaterials, expansion of metallic parts
• Line pressure (Cavities, explosion, decompression)
• Line contents (incompatibility with the sealmaterials)
• Immersion time
Solution• Check such aspects with pig suppliers
UNUSUAL DAMAGE TO 10” X 16” PIG
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52PE 607: Oil & Gas Pipeline Design, Maintenance & Repair
UNUSUAL DAMAGE TO 10 X 16 PIG
DURING TESTING
• As an example of the need to “Expect the
Unexpected”, the following photographshows a 10” x 16” pig stuck in the straight
10” line at a flange and offtake
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UNUSUAL DAMAGE TO 10” X 16” PIG
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54PE 607: Oil & Gas Pipeline Design, Maintenance & Repair
DURING TESTING
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56PE 607: Oil & Gas Pipeline Design, Maintenance & Repair
Ff
Vp
P1 P2
Pipe Wall Pig
PIG MOTION ANALYSIS
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57PE 607: Oil & Gas Pipeline Design, Maintenance & Repair
PIG MOTION ANALYSIS (Cont.)• The drag force is equal in magnitude but
opposite direction of the contact friction force
• The equation shows that the pig velocity is
smaller than fluid velocity by Vd
N F F f D η ==
AC
N V WhereV V V
D
d d p ρ
η 2=−=
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58PE 607: Oil & Gas Pipeline Design, Maintenance & Repair
• The leakage ratio is given by:
• Leakage = 1-Vp/V
• Where• CD = Drag coefficient
• A = Area
• Ρ = Fluid density
• η = Contact friction coefficient
• N = Angular speed, rpm
• kd = Diameter ratio of the disk
( )
4
22
4
1
d d D d
d
k DC k
Dk
= =
−
PIG MOTION ANALYSIS (Cont.)
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59PE 607: Oil & Gas Pipeline Design, Maintenance & Repair
Example• A pig with two end disks having an
effective disk diameter of Dd=0.98 D isused in a 10 in steel pipe for cleaning thepipe interior. The fluid is water flowing at 6
fps. The pig being squeezed into the pipeexerted a total normal force of 400 lb onthe pipe wall and the contact friction
coefficient between the pig and the pipe iso.6. Find the velocity of the pig and thepercentage of the leakage flow
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