guide to pigging.pdf
TRANSCRIPT
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PIPELINE ENGINEERING
Applying Science to the Art of Pigging
Welcome to Pipeline Engineering
As the Managing Director and a major shareholder in Pipeline Engineering I
am committed to ensuring that we meet and fulfil the needs of our customers,our employees and our shareholders.
As technology in our industry advances the needs of our customers areconstantly changing. Every pipeline is unique and each pigging system hasto be carefully designed to ensure maximum efficiency and performance andto closely match the needs of our customers
To meet this challenge it is my intention to ensure that Pipeline Engineeringprovide the best and most cost effective pigging system solution. This meansmaking available to our customers the best design, material, construction andservice facilities.
To make this happen and on behalf of Pipeline Engineering I will ensure that:
Our employees are trained to achieve the highest
standards in the industry
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standards in the industry
PIPELINE ENGINEERING
Applying Science to the Art of Pigging
PIPELINE ENGINEERING
Since our formation in 1969, we have been supplying pipeline related
products and services to the oil, gas and petrochemical industries throughoutthe world.
By focusing on our users requirements we have acquired a reputation forhigh quality products, reliable deliveries and a real concern for customerneeds. We are considered by many to be Europes leading manufacturer ofpigs, spheres, scraper traps, pressure vessels and assemblies.
OWNERSHIP
Pipeline Engineering is a private limited company registered in England.Following a management buy out in 1997 the Company shareholders are asfollows:
Quester Venture Capital Trust managed by London based Quester CapitalManagement Limited are one of the UK's leading independent venture capitalgroups devoted to providing finance and support to smaller unquoted
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Applying Science to the Art of Pigging
Willy Watson Managing Director of the Company, is an engineering graduateand a Cranfield MBA. He spent 15 years in the multinational BICCengineering group mostly in international marketing and general
management. More recently he has been involved as managing directorturning around smaller engineering businesses. He joined PE in August1996 and has returned the company to profits after a number of difficultyears. Willy Watson holds 26% of the equity.
With a strong balance sheet and shareholders that are actively involved inthe day to day running of the business, our customers, suppliers andemployees can be assured of a total commitment to this business.
COMPANY STRUCTURE
Pipeline Engineering is structured into five departments:
Quality Assurance
Sales and Marketing
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PIPELINE ENGINEERING
Applying Science to the Art of Pigging
LOCATION
We are located in the North East of England
Airports Teesside (25minutes)Leeds (1 hour)Newcastle (1 hour)
Railway Darlington(15minutes)London Edinburgh Main Line
Road 2 Minutes from A1London Edinburgh Main Trunk RoadEdinburgh
Aberdeen
Pipeline Engineering
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PIPELINE ENGINEERING
Applying Science to the Art of Pigging
PRODUCT RANGE
Pipeline Engineering offers solutions to various pipeline problems through pig
and pigging related activities. Some of these areas are as follows:
Design and Manufacture of:
Pipeline Pigs and Spheres
Pig Traps
Trap Closure Doors
Pig And Sphere Signallers Pipeline Isolation Systems
Sub-Sea and On-Shore Sphere Flow Tees suitable forthe passage of spheres and all intelligent pig vehicles
Sub-sea and On-Shore Piggable Wye Pieces
Project Management, Engineering and Fabrication of:
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PIPELINE ENGINEERING
Applying Science to the Art of Pigging
POLYURETHANE
Our sister company - Polyurethane Engineering - possesses vast technical
and practical experience in formulating and processing urethanes.
This means that we can produce urethanes for specific applications; and donot have to rely on standard urethanes which may not be the best for acritical job. Many pigging operations, which may have been impossible usingstandard rubbers and urethanes, have been carried out successfully afterresearch has resulted in the development of a special urethane for thatparticular application.
Physical and chemical characteristics, such as high tear strength, highresilience, low compression set, high flex life, high heat resistance, highsolvent and hydrocarbon resistance, high abrasion resistance and lowhysteresis, have all been achieved through our research and developmentprogrammes and have resulted in products of outstanding quality andperformance.
TRACK RECORD
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PIPELINE ENGINEERING
Applying Science to the Art of Pigging
FACILITIES
Pipeline Engineering operates from two factories situated on the same
industrial estate, covering a total area of 20,000 square feet.
Manufacturing is organised into three activities:-
A machine shop which incorporates computer controlled CNCmachines
A polyurethane moulding plant with testing and research
laboratory.
A fabrication shop with metal forming, welding (with coded andqualified welders) assembly and pressure test facilities.
Our manufacturing facilities are supported by fully computerised production,administration, finance, sales & marketing. Design facilities are enhanced bythe use of the latest Computer Aided Design systems
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Applying Science to the Art of Pigging
PERSONNEL
Pipeline Engineering currently employs over 80 people, of which 60% are
directly involved in manufacture.
Key people you may wish to contact are:-
Managing Director Willy Watson
Works Manager Geoff Nathan
Financial Controller Jo Benn
Product Quality Manager John Spraggon
Projects Department Manager Kevin Wilson
Sales Office Manager (Internal) Fred Feenan
Export Sales Manager (Middle East) Nigel Baxter
Export Sales Manager (South-East Asia) Jason Tuer
Contracts Manager John Fisher
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PIPELINE ENGINEERING
Applying Science to the Art of Pigging
TECHNOLOGY
Pipeline Engineering is a market leader in the design and development of
pipeline pigging equipment being responsible for several industry firsts.These have been achieved in association with our customers or as adevelopment in our own right. Notable amongst these developments are thefollowing:
The first inflatable single-moulding pipeline sphere for generalmeter prover use, thereby overcoming the risk of splitting
Hyperbaric spheres for use in sub-sea completions, in co-operation with Shell Expro and Comex Diving Company
Patented composite pig cups to provide good sealing withadequate support for large, heavy pigs travelling longdistances
Patented low maintenance, magnetically actuated pig andsphere detector
S b i d h d t t
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PIPELINE ENGINEERING
Applying Science to the Art of Pigging
PROJECT ENGINEERING
Whilst being known world-wide for supplying a complete range of pigging
products, we also have a department integral within our BS EN ISO9001:1994 Quality network to provide a specialised product tailoring service.
Following 29 years of experience in the pipeline and pigging industry we havean enormous amount of experience to draw upon when confronted withspecial problems and needs. These highly qualified engineers workingtogether with experienced field personnel ensure a precise and practicalsolution to even the most demanding of requirements. This means clients
can be sure that multi product packages can be designed, manufactured,tested, commissioned and certified from a single source.
Our customers are closely involved in this process being constantly informedof the progress on their individual job.
This is made possible in part by the use of sophisticated computerisedsystems in the following areas
V l d i
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QUALITY CONTROL
Regular monitoring of materials and manufacturing output ensures that all of
our standard products are manufactured to the highest. This ensures thatoperators can use our products over and over again and still be sure thatthey will give excellent performance.
We have introduced a Quality Assurance system to monitor and controlmaterials, welding standards, assembly, testing and documentation. Thisprogramme more than satisfies the requirements of the industries it serves.
QUALITY ASSURANCE
High quality standards and continued product reliability have resulted inaward of the following recognised quality certificates:
BS EN ISO 9001:1994
Part I (ISO 9001) incorporates specification fordesign/development, production and servicing.
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CONTENTS - SECTION 1.0
1.1 Tools and Techniques
1.1.1 Description (What are Pigs?)
1.1.2 Function (What do pigs do?)
1.1.3 Description of Pigging Functions
1.1.4 Method (How do pigs work?)
1.1.5 Selection (How do I choose a pig?)
1 2 Pi li D i F t
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TOOLS AND TECHNIQUES
1.1.1 DESCRIPTION (What are Pigs?)
1.1.1.1 OVERVIEW
Pipeline Engineerings formidable reputation is based on the high specification andquality of its pigs, traps and related equipment which have been used to maintain
pipelines world-wide for many years.
But, what is a pig. The name refers to a mechanical device that can be inserted intoa pipeline and used to carry out pre-defined tasks (depending upon its construction)at critical points, or along the full length of the pipeline.
Pigs are driven by pressurising the pipeline behind them or, in most cases, insertingthem into the existing product flow, using specialised laundering equipment.
Whilst the potential applications for pigs are limited only by the imagination of thespecifier and the manufacturer, most tasks have now been defined and accepteddesign characteristics are used by all the major suppliers.
Pigs and spheres must be suitably equipped to carry out a function or task. Thesetasks are given names (cleaning, gauging, separation, drying, etc.) but the demandsof any individual task may require very different qualities from the pig depending uponthe stage in the development of the pipeline (pipeline development stage) at which
th i i t b d ( t ti i i i i i i t )
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There are two types of pigs at the highest level:
1. In-line inspection tools (Intelligent Pigs)2. Utility pigs
1. In-Line Inspection Tools (I.L.I)
Because of the complexity of these pigs (which make extensive use of on-board
electronics, they fall outside the scope of this manual.
2. Utility Pigs
Utility pigs include all categories except intelligent pigs. They can be divided into 5sub-groups based on their construction characteristics:
1. Metal bodied pigs (often referred to as mandrel pigs) sealing componentsaxially mounted on a tubular or solid metal body.
2. Solid cast pigs single piece polyurethane casting usually dumb-bell shaped3. Foam pigs moulded polyurethane foam, usually in 3 densities: soft; medium;
hard.4. Spheres manufactured from cast polyurethane and various rubbers according
to task5. Special pigs construction is similar to metal bodied pigs.
Specialised categories are allocated according to function (the task, or type of work
th t th i ill b i d t f ) Alth h f ti f d t
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Solid cast pigs are constructed entirely from polyurethane whilst spheres can be madfrom several types of elastometric material:
Polyurethanes
Rubbers: Neoprene; Nitrile; Silicon; Viton Seals
There are 3 types of detachable seal:
Discs Standard Cups
Conical Cups
Seals made from polyurethane are specified for most pigging functions it possessesexcellent physical characteristics which can be formulated for specific applications.However, there are good reasons for specifying some rubbers, which are given later.
Careful formulation of urethanes allows characteristics such as harness, tearstrength, abrasion resistance, hydrocarbon and hydrolysis resistance, flex life andcompression set to be modified.
There are 2 types of polyurethane:
Ethers (Good hydrolysis resistance; high resilience; low compression set).
Esters (Better physical properties than ethers).
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The pig body is manufactured from steel tube in pigs 8 and above and a steel bar inpigs below 8. Other materials, including aluminium and polyurethane, are also used.Flanges are welded to the body at both ends of the pig for seals and spacers; studsand pads are provided for attachment of fittings.
These pigs incorporate discs, standard cups and conical cups, manufacturedprimarily from polyurethane, although discs can also be supplied in several types ofrubber, as previously described. The quantity and type of seal depends upon the
pigging function and operating conditions.
Metal-bodies pigs allow the greatest range of fittings to be attached. This rangecovers fittings of all types and includes brushes, scrapers, plough blades, transmittedhousings, gauging plates, magnets and many other types necessary for specifictasks.
Solid Cast Pigs
These pigs are made from a single polyurethane casting. Therefore, the sealingelements are not interchangeable or replaceable. All seals are disc-type andcomprise 4 sealing and 2 support discs. They are designed, primarily, for small-borepipelines of approximately 2 to 12 nominal diameter.
The one-piece construction method limits the choice of fittings. However, brushes,gauging plates and magnets (for tracking and location purposes) can be fitted to thistype of pig.
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Spheres
The spherical elastomeric body of a sphere forms a single-line seal in the pipe.Therefore, there are no independent sealing elements to consider. Spheres do notaccept fittings (with the exception of some spheres which have magnets cast intothem for tracking and location purposes).
There are 2 types of sphere (with typical uses given):
Solid automated pigging programmes; batching; condensate removal
Inflatable meter proving; batching; condensate removal
Once the type has been decided, the characteristics of the pig are dependent uponthe formulation of the material from which the spheres are constructed. This willinfluence properties such as sealing efficiency, rate of wear, operating temperaturelimits and chemical resistance.
Inflatable spheres have a removable valve and are usually filled with water or awater/glycol mixture. Meter proving spheres are produced in hardnesses of 65-70Shore A while, for most other operational purposes, spheres tend to be specified withhardnesses of approximately 65 75 Shore A.
Special Pigs
Special pigs define those pigs usually metal-bodies which have to be significantly
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1.1.2 FUNCTION (What Do Pigs Do?)
1.1.2.1 OVERVIEW
Pigs must first be selected to carry out a specific function (task). This results in a pigwhich can generally be described by its function type. e.g cleaning pig, gauging pig,de-watering pig (section 1.4.0 explains this principle in more detail). For now, thescope of pigging functions is set out as follows:
1.1.2.2 PIGGING FUNCTIONS
As a result of the experience gained in pigging operations world-wide, most functionsare now pre-defined and can be found somewhere within the following list:
Debris removal
Cleaning
Gauging Filling
De-watering
Drying
Separation (batching)
Condensate removal
Meter proving
Product displacement
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1.1.2.3 PIPELINE DEVELOPMENT STAGE
Pigging function depends upon the stage in the operational life of a pipeline at whichthe pig must carry out its task. Most stages in the development of a pipeline can befound in the following list:
Construction
Pre-commissioning (including hydrostatic testing)
Commissioning On-line operations
Inspection
Maintenance and repair
Renovation and rehabilitation
Decommissioning
Some pre-defined functions can take place at several stages in the development of
the pipeline. However, pigs designed to carry out tasks at one stage of pipelinedevelopment may not possess features that are suitable to enable them to carry outthe same task at other stages. This is due to a combination of the following factors:
Pigging distance
Frictional resistance of the materials in contact
Lubrication
Pigging speeds
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Compressed air operations impose several conditions on the pig no lubrication isavailable and pigging occurs in a series of high speed excursions between localisedrestrictions. The pig stops and the pressure builds until there is sufficient energy tolaunch the pig past the obstacle. As the pig moves forward rapidly, the pressure isdissipated until the pig reaches the next restriction, causing the process to berepeated.
1.1.3.2 CLEANING
The specification of cleaning pigs depends upon the pipeline development stage atwhich cleaning is required usually at one of the following:
Pre-commissioning
On-line operations
Inspection
Renovation and rehabilitation
Decommissioning
Cleaning at each stage imposes a different set of demands on the pig. This could,but would not automatically, require variations in pig design. There are 2 mainrequirements for cleaning irrespective of the type of pig.
1. Pigs must be fitted with cleaning devices brushes (circular or spring mounted;scrapers; ploughs.
2 B t b i t d d th i d i ti l th b h
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1.1.3.3 GAUGING
Gauging is commonly carried out at the following stages:
Construction
Maintenance and repair
Decommissioning
It is necessary for 2 reasons:
To check that there are no unintended intrusions into the Pipeline Engineering
To confirm that the ovality of the pipeline is within acceptable limits (tolerances)
Metal-bodied pigs (uni-directional or bi-directional) are fitted with a circular aluminiumgauging plate (steel plates can also be used), which is usually machines to 95% ofthe smallest internal pipeline diameter. Foam pigs can also be adapted to accept
gauging plates but they are not often used for this purpose.
At the construction stage, gauging operations are usually conducted with compressedair. As with all other operations using compressed air as the pigging medium, it isextremely dangerous and less effective.
1.1.3.4 FILLING
Filli i i d t t th f ll i t
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1.1.3.5 DE-WATERING
After hydrostatic testing the water must be removed from the pipeline prior to dryingand subsequent commissioning. This is done by a series of pigs pushed through thepipeline using compressed air.
The same qualities are required for de-watering as for filling the most importantcharacteristic again being the ability to maintain an effective seal in order to minimise
leakage. All relevant pipeline design factors should be considered.
Soft foam pigs (swabs) are often run after de-watering to swab away any waterremaining on the pipe walls, or which has accumulated at low points in the pipeline.
1.1.3.6 DRYING
In on-shore pipelines, foam swabs are pigged with extremely dry compressed air (-
90F atmospheric dew point temperature). Together with pigs and the air pick up theremaining water leaving behind a dry pipeline. However, it takes more than oneswab to do this and is, of course, dependent on the length of the pipeline. Severalhundred swabs may be required to fully dry a pipeline.
After the pipeline is dry, brush pigs must be run to remove the rust, mill scale and anydeposits that have settled out from the hydrostatic test. Again, several hundredswabs may be required to remove the material loosened by the brush pigs. Theseswabs will then be run until the air reaches a specified dewpoint.
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1.1.3.9 METER PROVING
Meter proving describes the procedure for calibrating flow meters (e.g turbine andpositive displacement meters) in which pigs are used to batch a known volume ofproduct through the meter. This volume is then compared against the volumeindicated by the meter.
Early meter provers were simply a measured mile of pipe in which batching pigs
were used to push the product through the meter in one direction only. When thepigs had completed the task they were transported back to the launcher to be usedagain. To save on transportation and handling costs, bi-directional pigs began to beused as these pigs could be returned simply by reversing the flow of the pipeline.
The next development saw spheres used in a continuous pipeline loop with aninterchange valve closing the top from the bottom. These interchange valvessubsequently proved to be inadequate and bi-directional meter provers became
standard.
In their simplest forms, meter provers consist of an internally coated pipe containingan inflatable sphere. Electrical pig signallers and a scraper trap (for launching andreceiving spheres) are installed at each end of the pipe. The volume of productcontained in the pipe between the detectors is accurately calibrated against certifiedcolumetric tanks and the meter to be proved s connected in series with the meterprover system.
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1.1.3.11 PRODUCT DISPLACEMENT
The same qualities are required for displacement as for filling and de-watering duties.Product displacement is carried out whenever the pipeline contents have to beevacuated, particularly at the decommissioning stage.
1.1.3.12 PRODUCT CONVERSION
This involves sterilising the pipeline prior to running other products which maybecome contaminated. Pigs used for this purpose require similar quantities to pigs
used for filling and de-watering duties.
1.1.3.13 GEL PIGGING
This technique does not involve utility pigs. A jelly-like substance is either injecteddirectly into the pipeline or moulded into cylindrical pigs. The jelly picks up andholds within it deposits found in the pipeline. It is bio-degradable and can be brokenup under pressure.
1.1.3.14 COATING APPLICATION
There are 2 pigging phases involved in the application of in situ pipeline coatings:
1 Cleaning2 Coating application
1. Cleaning
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1.1.4 METHOD (How Do Pigs Work?)
1.1.4.1 PROPULSION METHODS
Pigs travel through the pipeline under pressure from the pigging medium beingpumped behind them. This medium takes on of two forms:
1 Gas2 Liquid
Whatever the medium is gas or liquid has a dramatic effect on operational piggingcharacteristics, especially in terms of the pigs velocity profile.
Irrespective of the type of pigging medium, pig velocity has a profound effect onpigging efficiency. Pigs are designed to work most efficiently within a limited velocityrange which may be difficult to achieve, depending upon the pigging medium or otherfactors, such as the ability to regulate existing product flow rates.
1.1.4.2 PIGGING WITH A GAS
A stationary pig requires increased pressure to start it moving. Once this pressure isreached, the pig moves forward very quickly as the pressure begins to decreasebehind it. Eventually the pig comes into contact with an obstruction, such as a weldbead, the pressure is insufficient to keep it moving forward and the pig stops. Thecycle then begins again.
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The differential pressure contributes to the efficiency of pigging operations in the
following ways:
It improves sealing efficiency by forcing the seals against the pipe wall, makingthem act like non-return valves.
It is used as by-pass in cleaning operations
1.1.4.4 BENEFITS OF BY-PASS
By-Pass is the controlled flow of pigging medium, gas or liquid, through and/or pastthe pig. It has two effects:
It reduces the pressure (P1) behind the pig and hence the differential pressure(delta P) across the pig variations in the differential pressure effects the speedof the pig. The pig slows down as the differential pressure decreases.
It provides a very necessary jetting action which increases the efficiency of
cleaning pigs by preventing brushes from becoming blocked with looseneddeposits and holding these deposits in suspension in front of the pig rather thanallowing them to form into a solid slug. These slugs are difficult to deal with atthe receiver but, more importantly, may cause the pig to become stuck.
Studies have shown that it is better to drive the pig in the pipe using the front sealsonly, the rear seals act as support. Pluggable by-pass ports are built into the pigbody for this purpose and allow the pressure to flow through the pig body and be
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2. Cleaning
During cleaning operations, especially was removal, the deposits on the pipe wallvery quickly build up in the brush reducing its effectiveness. To prevent thishappening, limited by-pass can be used to create a flow path of pipeline productthrough and around the brushes. This tends to prevent the deposits removed fromthe pipe wall from building up in the brush by holding them in suspension within theproduct flow created by the by-pass.
Pigs are often fitted with jetting nozzles (also known as spider noses) which arepositioned in front of the leading set of seals. The nozzle jets are directed backtowards the leading discs or brushes (depending on the pig type) and again are usedto create a flow of product that is designed to hold in suspension any depositsremoved from the pipe wall.
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1.1.5 SELECTION (How Do I Chose A Pig?)
1.1.5.1 OVERVIEW
There are 3 fundamental questions to ask when selecting the appropriate type of pig:
1. What is the function, of task of, the pig?2. At what state in pipeline development will the task be performed3. Which pipeline design factors are relevant and to what extent will they influence
pig design
This approach will establish:
1. The most suitable type of pig and consequent arrangement of body, seals andfittings
2. The extent of any modifications and additions to the body, seals and fitting ofstandard pigs (resulting in the basis of a design or a special pig).
All pre-defined tasks will be carried our by one of the following 5 types of pig:
1. Metal-bodied pigs2. Solid cast pigs3. Foam pigs4. Spheres5. Special pigs
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The way in which some fittings are mounted will influence the pigging direction. The
following table refers to those fittings which do influence the pigging direction:
Uni-Directional Bi-Directional
Brushes U-spring mounted Circular Cantilever Mounted Arch-spring mounted
Blades U-spring mounted Arch-spring mounted
Cantilever Mounted
Scrapers U-spring mounted Arch-spring mountedCantilever Mounted
Each pig type incorporated very different design characteristics which are examinedin more detail below:
1.1.5.2 METAL-BODIED PIGS
Metal-bodied pigs are divided into 2 groups according to their directional ability withinthe pipeline. This can be selected or, more likely, will be imposed by the operatingconditions;
Uni-directional pigs travel through the pipeline in one direction only
Bi-directional pigs travel through the pipeline in either direction
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Cups
Standard cost effective design
Conical greater flexibility of use
Selection depends on the pipeline design factors detailed in section 2.0.0. However,conical cups do offer one particular advantage over standard cups an increasedability to pass restrictions in the pipeline (up to 20% of minimum pipeline internaldiameter compared to 5% with standard cups).
Other Factors
After ensuring that the pig will travel through the pipeline, selection is based on thepigging function, particularly when the function relies on the qualities of the seal (e.g.de-watering, filling, pigging long distances)
Unless operating conditions dictate otherwise, the pig body will be constructed
relative to the diameter and length of the pig. This ratio is as follows and variesbetween pig types it does not include spheres:
Length of pig = nominal pipe diameter x n(The value of n varies between approximately 1.4 2.0 according to pig type)
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1.1.5.4 FOAM PIGS
Foam pigs are initially selected according to pigging functions the following typesare commonly available for the task specified:
Bare swabbing displacement
Fully polyurethane coated displacement
Criss-cross polyurethane coated displacement/light cleaning
Wire brush spiral pattern cleaning
Wire brush fully covered cleaning (long run) Silicon gritted heavy cleaning/scale removal
The characteristics of foam pigs are more closely matched to the task by specifyingthe density of the open cell polyurethane foam:
Soft approximately 2lb/ft3
Medium approximately 5lb/ft3
Hard approximately 8lb/ft3
Hard foam pigs assist aggressive cleaning whilst Soft foam pigs improve swabbingcharacteristics.
Foam pigs are often specified as an alternative to metal-bodies pigs as they haveseveral advantages.
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1.1.5.5. SPHERES
Spheres play a vital role in pigging operation due, particularly, to their shape. Itallows them to be pre-loaded into launcher magazines and used to carry outautomated pigging operations (e.g. batching, condensate removal in untreated gaslines) where the launching facilities are un-manned for long periods.
There are 2 types of sphere:
Solid Inflatable
Solid spheres can be made from various elastomer materials:
Polyurethane
Nitrile rubber
Neoprene rubber
Solid spheres are used for batching and condensate removal from unmannedlaunching stations
Inflatable spheres made from polyurethane are always specified for use in meterprover loops because the sphere can be precisely inflated to give a constant seal asthe sphere wears with use. Meter prover spheres are softer than standard spheres(65-70 Shore A compared to 70 75 Shore A for standard spheres). Making the
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1.1.5.5 SPECIAL PIGS
If standard pigs must be modified to such an extent that they no longer comply withan ideal standard model in order to perform a function, then a special pig must bedesigned.
This usually involves changing the dimensions of a pig relative to the nominal pipelinediameter. The body dimensions may be changed or constructed in two modules(articulated), and the fittings and seals may also be suitably adapted. In some
instances, the dimensions of the pig remain unchanged with modifications beingconfined to altering the specification of the materials used in the construction of thepig.
Pigs designed for one-off tasks (tasks for which there is unlikely to be any furtherdemand) can also be classified as special pigs.
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PIPELINE DESIGN FACTORS
1.2.1 INTERNAL CONDITIONS (What Are Conditions Inside the Pipe?)
This section considers the potential problems posed by factors such as the chemicalcompatibility of the pipeline product with the materials used in the construction of thepig. It also considers the contributory effects of temperature, pressure, flow andpipeline deposits on the pig and its components.
1.2.1.1. PIPELINE PRODUCTS
Most pipelines carry one or more of the products listed below:
Hydrocarbons
Petrochemicals
Chemicals
Water
Food Products Gases
Each of these product groups has an effect on polyurethanes and rubbers to agreater or lesser extent. (Pig body materials are also effected by pipeline product).
The typical effect of chemical incompatibility with polyurethanes and rubber leads toblistering, cracking and chemical breakdown (Material is described as having a
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1.2.1.3 PRESSURE
Pressure does not have a significant effect on the construction of utility pigs whichcontain no sealed units. In-Line (I.L.I) pigs do have sealed units and pipelinepressure has a much more significant effect on this type of equipment.
The general effect of pressure is to move the pig in the pipeline. If this movement issmooth and constant then pigging will be much more efficient. In pipelinestransporting liquids, this characteristic movement is not difficult to achieve. However,
it is much more difficult in gas pipelines or where pigging is being carried out usingcompressed air.
Minimum pressure levels need to be achieved in order to keep pigs moving pastobstacles (typically weld beads) without stopping. IF a pig does stop, pressure willincrease until it is sufficient to launch the pig past the obstacle. Initial acceleration willbe rapid and overall velocity will be high with consequent safety implications, possibledamage to pipelines and fittings and much lower pigging efficiency. These problems
can be relieved by pressurising the pipeline ahead of the pig and venting at thereceiver.
Recommended minimum pigging pressures are often requested but are not easy tosupply as they are a compound of many factors: function, pipeline, condition,deposit, lubricant, seal material and type, liquid or gas pigging.
1.2.1.4 PRODUCT FLOW
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Condensates and water are swabbed our using pigs with seal discs, spheres or foampigs.
Polyurethane ploughs and scrapers are recommended for removing soft and hardwaxes respectively. Scale and mineral deposits often have to be removed usingfoam stud pigs to break up the hard scale initially then followed using cleaning pigsequipped with brushes.
Rust (corrosion) can be removed using brush-equipped cleaning pigs, possibly withmagnets fitted to pick up the ferrous debris. Foam pigs gritted with silicon carbide
can be used to burnish the pipeline, which will improve frictional losses and which, inturn, lead to increased pipeline output.
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1.2.2 PIPELINE SPECIFICATIONS (What Are the Pipeline Dimensions and
Materials?)
1.2.2.1 PIPELINE LENGTH
It is not the overall pipeline length that is of interest but the maximum piggingdistance the distance between launching and receiving stations. This factorinfluences the wear rate of the seals along with several other factors:
Pipe wall condition Pipe wall lining (if any)
Product compatibility
Seal material
Pigging medium
Presence of lubricant
Pigging speed
Throughout the world, pigging distances range from a few metres to hundreds ofkilometres. Whilst the pig design for the two extremes may possibly involve similarcharacteristics, it is essential that, along with the factors mentioned above, themaximum pigging distance is specified.
1.2.2.2 PIPELINE DIAMETER
Most pipelines have a constant external diameter while their wall thickness changes
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1.2.2.4 PIPELINE MATERIALS
Pipelines are made from many different materials:
Steel, including stainless steel.
Cast iron
Wrought iron
Cement
Reinforced concrete
Plastic
Whilst there are many reasons for selection of the line pipe, compatibility with theproposed product is extremely important. If the product is particularly aggressive, thepipe can be lined (this also improves the flow characteristics of the product in thepipe.
1.2.2.5 INTERNAL LININGS
Linings minimise corrosion of the pipe walls and improve the flow characteristics ofthe product. They can be applied when the pipe is constructed or after it has beenlaid.
There are several types of lining:
Epoxy linings
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1.2.2.8 BUNDLES
Bundles allow several pipes to be laid together. The operational pipelines arecontained within a large conduit that is laid as a single pipeline in the normal manner.Bundled pipelines do not present any problems to utility pigging.
1.2.2.9 RELATIVE POSITION FEATURES
This refers to the minimum distance between any two significant pipeline featuresthat might influence the efficiency of a pig or cause it to become stuck.
These features are as previously listed and are particularly relevant to the positioningof:
Valves
Offtakes (tees and laterals)
Bends
The general rule is that a minimum distance of 3 x pipeline diameters should beallowed between any two features.
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1.2.3 FITTINGS AND EQUIPMENT (What Components Are Fitted to thePipe?)
1.2.3.1 VALVES
Valves present major obstacles to successful pipeline pigging. There are severaltypes:
Ball valves
Gate vales
Check valves Butterfly valves
Plug type valves
Some types cannot be pigged but others can. Certain features can be included in thevalve design to assist pigging. Only those valves which can be pigged are illustrated,with relevant features noted.
There are two types of valve that cannot be pigged:
Butterfly/Plug type
There are three types of valve that can be pigged:
1. Ball valves2. Gate vales
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Possibly the single most important factor applies to all valves, irrespective of type.
They must all be OPEN. Appropriate mechanisms or checking procedures must bein place to ensure that this happens as the consequences of not doing so involvegreat expense.
Valves should always be fully specified as there will usually be some compromisewith regard to the most effective pig design for the function. Specialised componentsmay need to be added to the pig to improve its ability to pass safely through anyvalves.
1.2.3.2 OFFTAKES
All offtakes present a potential hazard to pigging. It is easy for pigs, especiallyspheres, to be diverted into an offtake and become stuck or continue their journeydown the offtake with obvious and expensive implications. Alternatively, if the sizeand relative positioning of offtakes are not offered for consideration at the pig designstage, it is possible that the pig may stall at the offtake as a flowpath opens up forproduct/pressure to bypass the pig. Spheres are particularly vulnerable as theyincorporate a single line seal (the circumference of the sphere I contact with thepipe).
Offtakes are sub-divided into 2 groups:
1. Offtakes which connect to the main pipeline at 90 - Tees2. Offtakes which connect to the main pipeline at other anges Laterals
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Sphere Tees allow product flow into and out of the offtake through slots around the
inner sleeve preventing the sphere from pushing into the offtake.
2. Laterals
Laterals are offtakes that connect to the main pipeline at angles other than 90. Theyare either barred or unbarred although, when designing pipelines for pigging, theyshould always be barred. Laterals present an increased opening when compared toTees. Therefore, pig design must take account of this. Pigs have to be made long
enough to span the opening to prevent stalling.
1.2.3.3 WYES
For the purpose of pigging, wyes join two lines together, both of which must bepigged. The pig emerges from a branch pipeline into the main pipeline (main andbranch do not imply any difference in pipe diameter) where it changes direction bybouncing off the opposite wall of the pipeline into which it has emerged. Theconvergence angle between the two pipelines is between 22 - 30.
Wyes can be pigged on one direction only and there is therefore no requirement forthe pigs to be bi-directional although disc-type pigs offer the most popular solutions.
There are two types of wye, each of which requires a pig possessing different designcharacteristics:
1. Wyes with parallel bores
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1.2.3.4 DIVERTERS
Diverters are designed to guide pigs from a main pipeline into a branch (lateral) theopposite of wye pigging. The pipeline product is not diverted only the pig.
Most diverters use mechanical methods but some divert pigs by means of magnetswhich attract the metal bodied pigs.
1.2.3.5 BENDS
There are three types of bend:
1. Forged (or factory) bends2. Field bends3. Mitred bends
1. Forged (Factory) Bends
Forged bends are classified according to their bend radius which is expressed interms of diameters or D. Standard sizes are produced as follows:
ID or short radius bend should not be included in a system designed for pigging.However, if they are present, it may be possible to manufacture special pigs tocope.
1D or long radius bend suitable for: spheres, foam pigs, specified metalbodied pigs
3D most utility pigs are suitable
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The minimum bend radius is almost always the first piece of information requested bythe pig manufacturer after establishing the pipeline diameter and pigging function. It
is important that as much relevant information as possible is made available.
1.2.3.6 TRAPS AND PIG HANDLING EQUIPMENT
To some extend, pig design is dependent upon the type of launching and receivingequipment installed. Some systems will only accept their own specially designedpigs and some systems will allow pig design within the limits of the trap dimensions.These systems may be specified in applications where complex industrial pigging
strategies are necessary or where trap size must be restricted because of spacelimitations.
Where there are no such restrictions, the following points should be considered:
Are handling facilities adequate for pig types and weights?
Are the traps sufficiently oversize to allow the pigs to be properlylaunched/received?
Are the traps large enough to meet the requirements of the pigging programme? Do the traps have the necessary characteristics for launching and receiving?
Are the traps suitably equipped for automated pigging programmes?
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HYDROSTATIC TESTERS
CONTENTS - SECTION 2.0
2.1 Introduction
2.2 Description and Purpose
2.3 Function
2.4 Construction
2.5 Selection
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INTRODUCTION
1.0 INTRODUCTION
Testing the integrity of joints in pipelinesystems can be a time consumingbusiness. In many instances, testing a
joint just a few millimetres wide around the
circumference of a pipe involves longhours fitting blind flanges and flooding theentire pipe section with a pressurisingmedium (usually water). This liquid - and it
can be a substantial volume - has then tobe disposed of safely when the test hasbeen completed.
Pipeline Engineering have simplified this process. They have developed specialisedequipment which can be used to test most pipeline joints, in a fraction of the timeand at much less cost when compared to the previous method. Moreover, the tools
can be used time and time again, and - in some instances - are suitable for a rangeof internal pipeline diameters.
Fig 1.
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Flange Weld Testers (fig. 3) are designed totest the weld securing a flange onto the end of apipe spool. They can be used for all types of
flanges, including weld neck types, and can beextended for special applications.
Internal Joint Testers provide solutions for a more diverse range of applications.
Primarily, they allow welds tying two lengths of pipe together to be tested (fig. 4a).However, they can also be used to test pipeline fittings such as valves withouthaving to remove them from the pipeline system (fig. 4b). They can even be used toisolate individual branches of a pipeline system for hydro-testing (fig. 4c).
Fig 4a Fig 4b Fig 4c
Fig 3
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1.2 FUNCTION
All testers work by pressurising a contained volume of test medium (usually water)
between two sealing faces and the pipe wall, thus producing a low volume testcavity. FWTs contain the medium between an expandable elastomeric seal, theface of the tester flange and the pipe wall (fig. 5a). IJTs contain the mediumbetween two expandable elastomeric seals and the pipe
wall (fig. 5b).
Fig 5a Fig 5b
The test medium is introduced through a special fill port, irrespective of the type of
tester. This port is also used to pressurise the medium and complete the test. To dothis reliably a separate vent port is provided in order to expel any air within the testcavity.
When an efficient seal has been created in which to contain the test medium, wesay the tester has been energised. How this is done is depends upon the nominal
Fig 5a
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Flange Weld Testers are, by design, quite specific for their intended purpose andany variations are normally confined to extended body lengths, flange specifications
and installation/handling requirements depending upon the installation orientation ofthe tester (vertical up/down; horizontal).
Internal Joint Testers have much more scope for variation and as specials can be -and have been - articulated, extended and wheeled. Special installation tools can beproduced to allow them to operate further into the pipeline, beyond the scope ofstandard testers.
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All standard Flange Weld Testers (fig. 7) feature:
1. A suitably rated flange connection (typically ANSI)2. Polyurethane (PU), low hysteresis seal
3. Body section (to set the distance between the flange and the seal)4. Expander and pusher components (to deform the seal)5. Filling and venting ports (threaded to customer specifications)6. An energising system (mechanical or hydraulic)
7. Suitable fittings for coupling to pumps etc. (to customer specifications)
8. Orings and antiextrusion rings (to prevent pressure losses betweenadjacent components)
Fig 7.
Flange Weld Tester
h draulicall ener ised
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1. Polyurethane (PU), low hysteresis seal (x 2)2. Body or body/spacer (to set the distance between the seals)
3. Expander and pusher components (to deform the seal)4. A venting chimney5. Filling and venting ports (threaded to customer specifications)
6. An energising system (mechanical or hydraulic)7. Suitable fittings for coupling to pumps etc. (to customer specifications)8. Orings and antiextrusion rings (to prevent pressure losses between
adjacent components)
Fig. 8a
Internal Joint Tester
mechanically energised
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Special Productsare those testers outside the scope of standard testers, although
they may only vary from the standard pattern because, for example, a largediameter tester may be required to perform tests at pressures up to ANSI Class2500.
Pipeline Engineering recommend that only PE-supplied nitrile Orings and PTFEantiextrusion rings be carried as spares and replaced in accordance with theinstructions which accompany all PE testers.
Typical ancillary fittings comprise:
Hydraulic hand pump for energising hydraulic testers Hydraulic hand pump for carrying out hydrotest (all testers) Lifting shackles for vertical applications
Spanners for energising mechanical testers Hosing necessary for connecting pumps to tester Installation/insertion tools (for special applications)
2.0 SELECTION
To provide the user with the most suitable equipment for their application, PE wouldappreciate the following information:
Nominal pipeline diameter
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CONTENTS - SECTION 3.0
3.1 Introduction
3.2 High Pressure Stoppers
3.2.1 Grip Lock Pipe Plugs
3.3 Medium Pressure Stoppers
3.3.1 Compression Pipe Plugs
3.4 Low Pressure Stoppers
3.4.1 Gas Seal Stoppers
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INTRODUCTION
1. INTRODUCTION
Within the life of any pipeline there comes a time when, for one reason or another,work must be done which requires that a normally closed pipeline system has to betemporarily interrupted. e.g. when removing in-line fittings or sections of pipeline.
Using conventional techniques, the pipeline would have to be shut down and possiblydrained before such work could proceed.
This can be a time-consuming, expensive and logistically complex business.However, by using a system of temporary stoppers, massive reductions in time andexpense can be achieved.
Pipeline Engineering manufacture a range of temporary stoppers collectively knownas Pipe Stopper Systems or simply Stoppers. Superbly engineered, they shareseveral important characteristics. All can be inserted into the pipeline to form a
reliable and re-usable temporary seal capable of safely retaining a specified pressurefor long periods. Most require no special facilities, are simple and quick to operatewith smaller diameter stoppers capable of being transported and energised by hand.The following chart indicates the general range of stoppers available from PipelineEngineering.
From the chart on page 2 we can see that there are 3 basic types of stopper:
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Piggable
Hyperbaric
Spheres
n
Piggable
Hi-d
ifferential
StopperPigs
SLHD-10
n
Inflatable
AirBags
n
T
riple
Tyre
n
Twin
Tyre
n
GasSeal
Stoppers
Single
Tyre
n
re sggable
PER
SYSTEMS
esuppliedwithwingnutsforenergisingbyhand
ksealingdiscswhichproduceapigwithahighinterferencefitinthePipeline.
rmoretyresbeinggritted
forincreasedgrip.
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Low pressure stoppers can bend like plastic if they are used beyond their strict
specifications and, when used for retaining gases, any stopper can easily take on thekilling properties of a bullet but again, only if used beyond its specification.
An efficient stopper must posses 2 essential, and quite different, characteristics. Itmust have:
1. The ability to create SEAL, retaining the d.p. acting across it2. The ability to HOLD its longitudinal position with the pipe whilst under
pressure.
Figure 2 illustrates the common factors which determine the holding, or gripping,ability of all stoppers under load. These are:
A. The differential load to which the stopper is beingsubjected
B. The maximum force with which the stopper can gripethe pipe wall
C. The coefficient of friction, or the frictional resistance,between the surfaces in contact (the type of materialand its condition are major factors rusty pipe wallsprovide a much better gripping surface than smoothpipe walls).
D. The total area of contact of the stopper with the pipewall (The area to which the gripping force can beapplied).
Fig 2. Factors influencingStopper efficiency
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At high pressures, the friction grip of the elastomeric sealing elements on the pipe
wall is insufficient to hold the stopper against the d.p. that would eventually force thestopper out of the pipe. Such stoppers must incorporate a means of anchoringthemselves within the pipe.
Figure 4 shows how Pipeline Engineerings GripLock Pipe Plugs achieve this by incorporatingsegmented, toothed vice-rings which, when thestopper is energised, expand radially and bite into
the pipe wall. These vice-ring segments aremounted circumferentially around the body of thestopper on a taper so that, as the d.p. attempts toforce the stopper out of the pipe, the effect of thetaper translates any backwards motion to the vice-rings that then bite deeper into the pipe wall,increasing the security of the stopper in proportionwith the load being applied to the stopper. Such stoppers are described as beingself-energising.
Further means of differentiating stoppers can be found in characteristics that effecttheir deployment:
1. Energising Systems
Energising systems are those used to create the sealing and holding forces betweenthe stopper and the pipe wall. There are 4 such systems used throughout the range
Fig 4. Vice-ring anchoring mechanism
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2. Methods of Deployment Within the Pipeline
Stoppers can be defined as being either piggable or non-piggable. Standard stoppers designed to be piggableinclude Piggable Hyperbaric Spheres and Hi-differentialStopper Pigs, both of which require facilities to launchand/or receive them. (Refer to section 4.5 to see howHyperbaric Spheres are used). Non-piggable stoppers areusually manipulated manually, either directly by hand or byusing Extendable rods which are used to push the stopper
into position at the work site. Wheels are often added to thestopper to make this task easier, as shown in figure 5. Forspecial applications, however, many conventional non-piggable stoppers can bedesigned to be piggable (within certain design limits). It is in situations like thesewhere the advice of an experienced manufacturer, like Pipeline Engineering, isindispensable.
3. Environmental Suitability
All stoppers, with the exception of Inflatable Air Bags, utilise an elastomeric seal usually polyurethane. Although it has many excellent physical characteristics and isuniversally popular for such applications, polyurethane is susceptible to manychemicals as well as to high temperatures. For these reasons, alternative elastomersmay need to be specified where necessary or periods of deployment carefullycontrolled and even avoided where aggressive chemicals or high temperatures areinvolved.
Fig 5. Gas Seal Stopper
(With wheels)
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HIGH PRESSURE STOPPERS
2.1 GRIP LOCK PIPE PLUGS
2.1.1 DESCRIPTION
The Grip Lock Pipe Plug is offered by Pipeline Engineering as a temporary pipelinestopper system for high pressure applications. It has a number of features thatmake it particularly suitable for repeated use at high pressure.
1. Self-energising, heavy duty gripping mechanism2. Major components either forged or machined from solid steel bar3. Rugged, square section, low hysteresis elastomeric sealing element4. Easily maintained with spares available for critical parts5. Heavy duty construction
Grip Lock Pipe Plugs are supplied with one of two energising systems, dependingupon the diameter of the pipe in which the plug is to be used:
1. Mechanical energising is typically offered on stoppers for use in pipelines upto and including 6 ns.
2. Hydraulic energising is typically offered on stoppers for use in pipelines 8 nsand over.
Plugs are offered as standard up to 16 and are capable of withstanding pressures upto 207 bar, depending upon diameter. For use in applications over 16 it is alwaysbest to seek the expert advice of the manufacturer.
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Below a certain diameter (typically 8 ns) Grip Lock Pipe Plugs incorporate a
mechanical energising system. The reason for this is that stoppers above thisdiameter are consequently heavier and are energised more efficiently usinghydraulics. Mechanical stoppers are energised either by turning a hexagonal nut inwhich a spanner or turning a wing nut by hand. Hydraulic stoppers are connected toa hand pump via fittings that can be specified by the client.
Installation is simple: Taking care not to damage the elastomeric seal, the de-energised plug is inserted into the pipe (which should have been cleared of debris,
mill scale or rust). Hydraulic plugs can be connected to the hand pump at this pointor prior to insertion. The plug is then pressurised either by turning the nut clockwiseto expand both the seal and the vice ring, or by operating the hand pump until therequired inflation pressure is reached. If the seal is not fully effective and the internalpressure is leaking, then the inflation pressure can be increased. However, it isimportant to note that it is possible to swage the pipe when applying excessivepressure. At this point the plug is fully energised and any filling and/or monitoring canbe done through the central port provided on al Grip Lock Pipe Plugs. Oncompletion, the stopper can be removed simply by venting the internal pipeline
pressure and de-energising the seal.
2.1.3 CONSTRUCTION
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2.1.3 CONSTRUCTION (Continued)
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MEDIUM PRESSURE STOPPERS
3.0 COMPRESSION PIPE PLUGS
3.1.1 DESCRIPTION
The Compression Pipe Plug is offered by Pipeline Engineering as a temporarystopper system for medium pressure applications. It has a number of features thatmake it particularly suitable for its intended use:
1. Durable elastomeric sealing elements provide large circumferential contactarea with Pipeline Engineering One or more sealing elements can be grittedto increase gripping power
2. Major components cut or machined from solid steal3. Easily maintained with spares available for critical parts4. Heavy duty construction
Compression Pipe Plugs are supplied with one of two energising systems, dependingupon the diameter of the pipe in which the plug is to be used.
1. Mechanical energising is typically offered on stoppers for use in pi0pelines upto and including 6 ns
2. Hydraulic energising is typically offered on stoppers for us in pipelines 8 nsand over
Plugs are offered as standard up to 16 and are capable of withstanding pressures up
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Installation is simple. Taking care not to damage the elastomeric seals, the de-
energised plug is inserted into the pipe (which should have been cleared of debris,mill scale or rust). Hydraulic plugs can be connected to the hand pump now or priorto insertion. The plug is then pressurised either by turning the nut clockwise toexpand the seal or by operating the hand pump until the required inflation pressure isreached. If the seal is not fully effective and the internal pressure is leaking, then theinflation pressure can be increased. At this point, the plug is fully energised and anyfilling and/or monitoring can be done through the central port provided on allCompression Pipe Plugs. On completion, the stopper can be removed by simplyventing the internal pipeline pressure and de-energising the seal.
3.1.3 CONSTRUCTION
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LOW PRESSURE STOPPERS
4.1 GAS SEAL STOPPERS
4.1.1 DESCRIPTION
The Gas Seal Stopper is offered by Pipeline Engineering as a temporary pipelinestopper system for low pressure applications. It has a number of features whichmake it particularly suitable for its intended use:
1. Inflatable rubber sealing elements provide large circumferential contact withPipeline Engineering Sealing elements will accommodate ovality, irregularityand diameter variations in pipelines/drains/sewers
2. Available in large diameters3. Easily maintained with spares available for critical parts4. Heavy duty construction
Gas Seal Stoppers are available in one, two and three seal (or tyre) versions, all of
which can be inflated pneumatically or hydraulically using a hand or foot pump. Theyare available in a range of diameters from 4 to 60 and are capable of withstandingpressures up to 10 bar, depending upon diameter. Such a stopper must have threeseals and be adequately strutted.
Typical applications include:
1. Emergency isolation for inspection/repair2. Gas exclusion at a welding site
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4.1.2 FUNCTION
All Gas Seal Stoppers are inflated either hydraulically or pneumatically using a handor foot pump. Sealing elements are braced by steel or aluminium rings supporting 3sides so that expansion is directed against the pipe wall.
Installation is simple. Taking care not to damage the sealing elements, the deflatedstopper is inserted in the pipe (which should have been cleared of debris, mill scaleor rust).
The plug is then pressurised by operating the pump until the required inflationpressure is reached. Most seals with respect to this type of equipment are gained atless than 9 bar g. If the seal is not fully effective and the internal pressure isleaking, then the inflation pressure can be increased. Caution: The inflation pressureshould never exceed 20 bar g. At this point the plug is fully energised and any fillingand/or monitoring can be done through the central port provided on all Gas SealStoppers. On completion the stopper can be removed simply by venting the internalpipeline pressure and deflating the seal.
4.1.3 CONSTRUCTION
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4.2 INFLATABLE AIR BAGS
4.2.1 DESCRIPTION
Inflatable Air Bags are offered by Pipeline Engineering as a temporary pipelinestopper system for low pressure applications. They have a number of featureswhich make them particularly suitable for their intended use:
1. Large diameters available up to 962. Inflatable bladder with accommodate ovality, irregularity and diameter
variations in pipelines/drains/sewers3. Bags can be compressed to pass through small holes in pipes4. Robust and easy to use
Inflatable air bags are available in a range of diameters from 2 to 96, although largerdiamteres are available as specials and are capable, when used with suitable
mechanical bracing in the pipe, of withstanding pressures up to 8 bar, dependingupon diameter. The primary use of Inflatable Air Bags however, is for low pressuretesting at a few pounds per square inch. A 4 diameter nylon covered bar wouldtypically be capable of withstanding 2.5 psi unsupported in a cast iron pipe. Theability of the bag to hold against higher internal pipeline pressures can be improvedby using double length bags with restraining loops for attachment of restraining wires.Properly anchored, these bags will hold against internal pipeline pressures of up to75% of their safe working pressure (inflation pressure).
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4.2.3 CONSTRUCTION
Fig 9a. Inflatable Gas Bag (Spherical)
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PIPELINE STOPPER SYSTEMS
LOW PRESSURE STOPPERS
4.3 DRAIN PLUGS
4.3.1 DESCRIPTION
Drain Plugs are offered by Pipeline Engineering as a temporary pipeline stoppersystem for low pressure applications. They have a number of features which makethem particularly suitable for their intended use:
1. Large diameters available up to 362. Cost-effective3. Robust and easy to use
Drain Plugs are available in a range of diameters from 3 to 36 and are capable ofwithstanding pressures up to 1 psi depending upon diameter. The primary use ofDrain Plugs is, however, for low pressure exclusions of liquids or gases at a fewpounds per square inch.
Typical applications include:
1. Low pressure, air, water or smoke testing of pipes and drains2. Low pressure plugging of pipes and drains3. Gas exclusion at a welding site4. Monitoring of internal pipeline pressure5. Venting and draining of pipes and drains
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4.3.3 CONSTRUCTION
Fig 10. Drain Plug
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LOW PRESSURE STOPPERS
4.4 HI-DIFFERENTIAL STOPPER PIG (SLHD-10)
4.4.1 DESCRIPTION
Hi-differential Stopper Pigs are offered by Pipeline Engineering to act as a primarypressure barrier situated deeper in the pipeline when used in conjunction with othertypes of stopper situated local to the work-site. They have a number of featureswhich make them particularly suitable for their intended use:
1. Large diameters available up to 562. Extremely hard wearing and reliable Omnithane seals3. Custom built for intended purpose4. Pigging allows access to remote work-sites
Hi-differential Stopper Pigs are available in a range of diameters from 4 to 56 andare capable of withstanding pressures up to 2 bar d.p. depending on diameter.
Fittings are available for gauging plates and transmitters (for location purposes).
Typical applications include:
1. Acting as the primary barrier in a pig train]Acting as the initial pressure barrierwhen undertaking hyperbaric repairs
4.4.2 FUNCTION
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4.4.3 CONSTRUCTION
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LOW PRESSURE STOPPERS
4.5 PIGGABLE HYPERBARIC SPHERES
4.5.1 DESCRIPTION
Piggable Hyperbaric Spheres are offered by Pipeline Engineering for subsea tie-inson pipelines. They have a number of features that make them particularly suitable fortheir intended use:
1. Specifically designed for subsea tie-ins2. Large diameters available up to 363. Cast from extremely hard wearing and reliable Omnithane4. Bi-directionally piggable
Piggable Hyperbaric Spheres are constructed from three layers of polyurethane acore, an intermediate seamless layer to provide strength and a softer outer layer toensure absolute sealing qualities. An internal tie-rod prevents excessive longitudinal
expansion and assists in increasing the pressure between the pipe wall and thesphere which enables a tight seal in the pipeline. They are available in a range ofdiameters from 4 to 36 and are capable of withstanding pressures between 1 bar gand 3 bar g, depending on diameter. 4 bar g to 6 bar g is required to pig them fromthe pipeline.
Specifically, their application is as a diver-installable stopper for hyperbaric use andwhich can subsequently be retrieved by pigging.
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Fig 12b. Piggable Hyperbaric Sphere
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SELECTION
5.0 SELECTION
To provide the user with the most suitable equipment for their application, PipelineEngineering would appreciate the following information:
Nominal Pipeline Diameter
Pipe wall thickness (ANSI pipe schedule) or minimum internal pipe diameter
Maximum internal pipeline pressure at the stopper
Pipe construction material (and whether the pipe is lined)
Pipe wall condition at the worksite
Distance to the worksite from the point if insertion
Points of ovality of deformation within the Pipeline Engineering Minimum bendradius (if the worksite lies beyond a bend)
Duty cycle of the stopper (Expected length of time under load)
Type of fittings and number of ports required
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PIG SIGNALLERS
CONTENTS - SECTION 4.0
4.1 Introduction
4.2 UniSig BossPig Signallers
4.3 UniSig FlangePig Signallers
4.4 UniSig ValvePig Signallers
4.5 Selection
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INTRODUCTION
1.0 INTRODUCTION
1.1 DESCRIPTION AND PURPOSE
Once a pig has been inserted into a pipe system its position cannot be visuallyconfirmed directly. A system is therefore required to indicate a pigs position, eithercontinuously or intermittently at pre-determined points in the pipeline. Continuousdetection is known as pig tracking whilst intermittent detection is referred to as pig
signalling. Each method involves the use of specialised equipment which, in mostinstances, must be incorporated into the pig or piping system before the pig islaunched.
Pig tracking requires an active transmitting source to be attached to the pig, withvarious technologies being used to provide that source - electro-magnetic, acousticand radioactive. Pig signalling, however, falls into two categories: intrusive and non-intrusive. Non-intrusive signallers are predominantly electro-magnetic and, along
with pig tracking techniques, are covered more fully elsewhere. Pipeline Engineeringhave applied their case experience to produce a wide range of intrusive pig signallerswhich are represented on the chart on page 2.
Intrusive pig signallers are, by definition, static, mechanically actuated and provide amomentary indication of a pigs presence at a specific point in the pipeline. Becausethe actuating mechanism is a mechanical trigger that intrudes into the pipeline, asignaller must also incorporate a satisfactory means of retaining the pressure within
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PIG SIGNALLERS
Minimum Pipe Size: 2 ns
ANSI Class 1500 (Class 2500 Specials)
UniSigBoss UniSigFlange UniSigValve
2 Flange Mounted Signaller Ball Valve Mounted Signaller
Not removable under pressure (1 Reduced Bore)
Removable under pressure
Standard Ring Type Joint Raised Face 1 Nipolet Mounted 2 Flange Mounted
Hot-Tappable (RTJ) (RF)
Removable under pressure
Extended
Non hot-tappable Ring Type Joint
Not removable under (RTJ)pressure
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Fig 1. Signaller Mounting Methods
UniSig FlangeMounted Signallers are also classified according to the flange face
type:
1. Raised Face (RF)2 Ring Type Joint (RTJ)
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1.2 FUNCTION
Installation
Signallers can be installed into the line under one or both of the following conditions:
1. When the pipeline is in-service and under line pressure
2. When the pipeline is at the construction stage or is out of service (no internalline pressure)
Installing a pig signaller directly into the pipelinewhilst that pipeline is in-service is known as hot-tapping and requires a welding boss or weld-o-flange to be attached to the pipeline through whichthe hot tapping can take place (Fig 3). Pipeline
Engineering have carefully developed their UniSigBoss Pig Signaller to be fully compatible with thehot-tapping tools of leading manufacturers, TDWilliamson and IPSCO. Hot-tapping is a detailedoperation with significant hazards and safety issuesreflected in the development of the UniSig whichallows the operational procedures of the toolmanufacturers to be followed without modification.
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When the magnet is withdrawn, themagnetic flux influencing thecomponents diminishes, the flagsprings into an upright position and/orthe proximity switch contact is broken.(This can be detected by a linkedcontroller). Immediately after the pig
has passed, the spring in the capreturns the magnet and the linkedtrigger to their respective restingpositions ready to detect the next pig from whichever direction it arrives. Theflag of an MV/MVE must be manuallyreset. Proximity switches, however, will be reset at the control panel.
Servicing and Replacement
Breakdown usually occurs as a result of scale, rust, hard waxes or sandaccumulating within the moving parts. For this reason it is essential that a regularmaintenance program is implemented. UniSig BossPig Signallers can be removedusing the relevant removal tool whilst UniSig FlangePig Signallers must be removedonly after ensuring that the pipeline is not under pressure. UniSig ValveMounted PigSignallers however are designed to be easily removable under line pressure as the
Fig 5. Intrusive Pig Signaller - Operating Principles
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UNISIG BOSSPIG SIGNALLERS
2.0 UNISIG BOSSPIG SIGNALLER
2.1 DESCRIPTION AND PURPOSE
The UniSig BossPig Signaller is an intrusive, mechanically activated pig signallerdesigned to be mounted to the pipeline via a welding boss. Its design allows it to beinstalled by hot-tapping and it has been developed to be compatible with the weldingbosses and hot-tapping tools of other leading manufacturers.
The unit is activated by a mechanical, bi-directional trigger that protrudes into thepipeline. A unique orientation locking system allows the signaller internals to bequickly fitted within the welding boss and ensures that the trigger mechanism isalways correctly positioned in the direction of pig travel.
Detected pigs are indicated by one of three methods:
1. Mechanical/Visual (MV) integral, magnetically linked, sprung flag2. Electrical (E) removable, magnetically linked, proximity switch3. Combined (MVE) MV and E systems incorporated
UniSig Bosss, along with all pig signallers manufactured by Pipeline Engineering, use
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2.2 FUNCTION
Installation
The UniSig Bosscan be installed into the pipeline under the following conditions:
1. When the pipeline is under pressure (hot tapping)
2. When the pipeline is not under pressure
Installing the UniSig Bossdirectly into a pipeline that is in-service is known as hot-tapping, a detailed operation with significant hazards and safety issues. This isreflected in the development of the UniSig Boss that allows the operationalprocedures of the tool manufacturers to be followed without modification. If, however,the pipeline is not normally pressurised, then the installation of a pig signallerrequires standard fabrication techniques and no special tools.
Operation
When a pig passes beneath a correctly installed signaller, the pig discs push theprotruding bi-directional trigger forward in the direction of the pig travel. The trigger ishinged at two points that converts the angular motion gained from contact with the piginto axial motion, withdrawing a spring loaded, permanent magnet holder downthrough the cap At rest the proximity of the magnet at the top of the cap retains a
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2.3 CONSTRUCTION
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UNISIG FLANGEPIG SIGNALLERS
3.0 UNISIG FLANGEPIG SIGNALLER
3.1 DESCRIPTION AND PURPOSE
The UniSig FlangePig Signaller is an intrusive, mechanically activated pig signaller
designed to be mounted via a 2 socket weld flange (Raised Face or Ring Type Joint)attached to the signaller welding boss. Its design allows it to be bolted to a matingflange attached to the pipeline.
The unit is activated by a mechanical bi-directional trigger that protrudes into thepipeline. (A trigger mounting extension gives the penetration necessary to accessthe pipeline through the mating flange). A unique orientation locking system allowsthe signaller internals to be quickly fitted and ensures that the trigger mechanism is
always correctly positioned in the direction of pig travel.
UniSig Flange signallers, along with all pig signallers manufactured by PipelineEngineering, use nitrile or viton O rings to withstand internal line pressures up tothose associated with ANSI Class 1500 (Class 2500 for specials). They areavailable in Raised Face (RF) and Ring Type Joint (RTJ) versions and are designedto be fitted to a minimum pipe diameter of 2ns.
Detected pigs are indicated by one of three methods:
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3.2 CONSTRUCTION
Installation
The UniSig FlangePig Signaller is installed in the line at the construction stage orwhen there is no internal line pressure. Installation requires only standard fabrication
techniques and no special tools
Operation
When a pig passes beneath a correctly installed signaller, the pig discs push theprotruding bi-directional trigger forward in the direction of the pig travel. The trigger ishinged at two points which converts the angular motion gained from contact with thepig into axial motion withdrawing a spring-loaded, permanent magnet holder down
through the cap. At rest, the proximity of the magnet at the top of the cap retains amechanical, spring-loaded flag and/or the contacts of an externally mountedproximity switch. When the magnet is withdrawn, the magnetic flux influencing thecomponents diminishes, the flag springs into an upright position and/or the proximityswitch contact is broken. (This can be detected by a linked controller or may simplybe used to activate an indicator lamp, siren, etc.) Immediately after the pig haspassed, the spring in the cap returns the magnet and the linked trigger to theirrespective resting positions ready to detect the next pig from whichever direction itarrives The flag of an MV/MVE must be manually reset proximity switches
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3.3 CONSTRUCTION
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UNISIG VALVEPIG SIGNALLERS
4.0 UNISIG VALVEPIG SIGNALLERS
4.1 DESCRIPTION AND PURPOSE
The UniSig ValvePig Signaller is an intrusive, mechanically activated pig signaller,
designed to be attached to the pipeline via one of the following methods:
1. Weld neck flange2. Nipolet
The signaller/clamp assembly is welded to a 1 reduced bore valve which is, in turn,either welded to a 2 weld-neck flange for mating to the pipeline-mounted flange or a1 Nipolet for direct attachment to the pipeline.
The unit is activated by a mechanical, bi-directional trigger which protrudes into thepipeline. A unique orientation locking system allows the signaller internals to bequickly fitted and ensures that the trigger mechanism is always correctly positioned inthe direction of pig travel.
UniSig Valve signallers, along with all pig signallers manufactured by PipelineEngineering, use nitrile or viton O rings to withstand internal line pressures up to
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PIG SIGNALLERS
4.2 FUNCTION
Installation
The UniSig Valve Pig Signaller is installed in the line at the construction stage orwhen there is no internal line pressure. Installation requires only standard fabrication
techniques and no special tools
Operation
When a pig passes beneath a correctly installed signaller, the pig discs push theprotruding bi-directional trigger forward in the direction of the pig travel. The trigger ishinged at two points which converts the angular motion gained from contact with thepig into axial motion withdrawing a spring-loaded, permanent magnet holder downthrough the cap. At rest, the proximity of the magnet at the top of the cap retains amechanical, spring-loaded flag and/or contacts and externally mounted proximityswitch. When the magnet is withdrawn, the magnetic flux influencing the componentsdiminishes, the flag springs into an upright position and/or the proximity switchcontact is broken. (This can be detected by a linked controller or may simply be usedto activate an indicator lamp, siren, etc.) Immediately after the pig has passed, thespring in the cap returns the magnet and the linked trigger to their respective restingpositions ready to detect the next pig from whichever direction it arrives. The flag ofan MV/MVE must be manually reset Proximity switches however will be reset at
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4.3 CONSTRUCTION
Fig 9. UniSig Valve Signaller
(Assembly mounted on 1 Nipolet)
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PIG SIGNALLERSFig 10. UniSig Valve Signaller (Assembly mounted on 2 weld neck flange)
5.0 SELECTION
To provide the user with the most suitable equipment for their application, PipelineEngineering would appreciate the following information:
Pipeline contents
Pipeline construction (or mating) materials Output type (MV, MVE, E)
Installation and mounting requirements (Hot-tapping, Welding Boss, Flange) Servicing requirements (Valves, In-line serviceable UniSig Boss)
Location/elevation of pipeline relative to access areas (i.e. extended versionrequired?)
Internal pipeline pressure. (If greater than pressures associated with ANSI Class1500)
Spares requirements Electrical requirements (only applies to E or MVE types)
Any special requirements
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